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That is all about me...<br /><span class="u-fw700">Supervisors: </span>Prof. Dr. Jan D. Miller and Prof. Dr. Mehmet S. 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id="social-redesign-work-container"><div class="upload-header"><h2 class="ds2-5-heading-sans-serif-xs">Uploads</h2></div><div class="documents-container backbone-social-profile-documents" style="width: 100%;"><div class="u-taCenter"></div><div class="profile--tab_content_container js-tab-pane tab-pane active" id="all"><div class="profile--tab_heading_container js-section-heading" data-section="Papers" id="Papers"><h3 class="profile--tab_heading_container">Papers by Behzad Vaziri Hassas</h3></div><div class="js-work-strip profile--work_container" data-work-id="78813275"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813275/Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects"><img alt="Research paper thumbnail of Effect of bubble size and velocity on collision efficiency in chalcopyrite flotation A Physicochemical and engineering aspects" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813275/Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects">Effect of bubble size and velocity on collision efficiency in chalcopyrite flotation A Physicochemical and engineering aspects</a></div><div class="wp-workCard_item"><span>Colloids and Surfaces</span><span>, 2016</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key fa...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813275"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813275"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813275; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813275]").text(description); $(".js-view-count[data-work-id=78813275]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813275; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813275']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813275, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813275]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813275,"title":"Effect of bubble size and velocity on collision efficiency in chalcopyrite flotation A Physicochemical and engineering aspects","translated_title":"","metadata":{"abstract":"In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.","publisher":"Elsevier","publication_date":{"day":null,"month":null,"year":2016,"errors":{}},"publication_name":"Colloids and Surfaces"},"translated_abstract":"In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.","internal_url":"https://www.academia.edu/78813275/Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects","translated_internal_url":"","created_at":"2022-05-08T23:40:35.405-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":3746,"name":"Colloids and Surfaces","url":"https://www.academia.edu/Documents/in/Colloids_and_Surfaces"},{"id":118582,"name":"Physical sciences","url":"https://www.academia.edu/Documents/in/Physical_sciences"},{"id":152114,"name":"Bubble","url":"https://www.academia.edu/Documents/in/Bubble"},{"id":238108,"name":"Chalcopyrite","url":"https://www.academia.edu/Documents/in/Chalcopyrite"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"}],"urls":[{"id":20345483,"url":"https://pubag.nal.usda.gov/catalog/5529472"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813271"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813271/Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage"><img alt="Research paper thumbnail of Effect of various ligands on the selective precipitation of critical and rare earth elements from acid mine drainage" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813271/Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage">Effect of various ligands on the selective precipitation of critical and rare earth elements from acid mine drainage</a></div><div class="wp-workCard_item"><span>Chemosphere</span><span>, 2021</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813271"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813271"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813271; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813271]").text(description); $(".js-view-count[data-work-id=78813271]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813271; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813271']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813271, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813271]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813271,"title":"Effect of various ligands on the selective precipitation of critical and rare earth elements from acid mine drainage","translated_title":"","metadata":{"abstract":"Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2021,"errors":{}},"publication_name":"Chemosphere"},"translated_abstract":"Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.","internal_url":"https://www.academia.edu/78813271/Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage","translated_internal_url":"","created_at":"2022-05-08T23:40:35.144-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":7967,"name":"Acid Mine Drainage","url":"https://www.academia.edu/Documents/in/Acid_Mine_Drainage"},{"id":26327,"name":"Medicine","url":"https://www.academia.edu/Documents/in/Medicine"},{"id":28235,"name":"Multidisciplinary","url":"https://www.academia.edu/Documents/in/Multidisciplinary"},{"id":395801,"name":"Rare Earth","url":"https://www.academia.edu/Documents/in/Rare_Earth"}],"urls":[{"id":20345480,"url":"https://api.elsevier.com/content/article/PII:S0045653521011553?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813268"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813268/Microwave_assisted_calcination_of_spodumene_for_efficient_low_cost_and_environmentally_friendly_extraction_of_lithium"><img alt="Research paper thumbnail of Microwave-assisted calcination of spodumene for efficient, low-cost and environmentally friendly extraction of lithium" class="work-thumbnail" src="https://attachments.academia-assets.com/85725565/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813268/Microwave_assisted_calcination_of_spodumene_for_efficient_low_cost_and_environmentally_friendly_extraction_of_lithium">Microwave-assisted calcination of spodumene for efficient, low-cost and environmentally friendly extraction of lithium</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 2021</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="23d113a911a837b6404c2740f9866819" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725565,"asset_id":78813268,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725565/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813268"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813268"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813268; 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813265"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813265/Morphological_changes_of_glass_bead_particles_upon_an_abrasive_blasting_as_characterized_by_settling_and_flotation_experiments"><img alt="Research paper thumbnail of Morphological changes of glass bead particles upon an abrasive blasting as characterized by settling and flotation experiments" class="work-thumbnail" src="https://attachments.academia-assets.com/85725568/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813265/Morphological_changes_of_glass_bead_particles_upon_an_abrasive_blasting_as_characterized_by_settling_and_flotation_experiments">Morphological changes of glass bead particles upon an abrasive blasting as characterized by settling and flotation experiments</a></div><div class="wp-workCard_item"><span>Physicochemical Problems of Mineral Processing</span><span>, 2021</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The recent developments in mineral processing led researchers to look for alternative methods and...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">The recent developments in mineral processing led researchers to look for alternative methods and propose new mechanisms for enhancing the efficiency of relatively costly processes (e.g., flotation, aggregation), where especially dealing with fine particles. Finer the particles, the higher the role of their surface on their behavior and properties. The importance of particle morphology becomes even clearer when particle-particle and particle-bubble interactions are considered. In this study, the effect of particle shape "roundness" on the surface wettability and flotation response was investigated upon producing fine particles with the "abrasion blasting" method. In order to provide a fundamental perspective, adsorption measurements were also carried out along with the flotation experiments under the same conditions. In addition to these, zeta potential measurements were also carried out with both spherical and blasted particles as a function of collector concentration. The results suggested that the roundness of particles decreased up to a certain nozzle pressure value, which was followed by higher adsorption degrees and consequently higher flotation recoveries. Additionally, settling rate tests were also performed with very fine material to show the effect of particle morphology on particle-particle interactions. The results showed that while lower settling rate values were obtained for spherical ones, higher values were obtained in the case of the ground and blasted samples in the presence of DI water. It was concluded from this study that the "Abrasive blasting method" could be an effective alternative for tuning the surface morphology of particles and their wettability, which in turn can affect the particleparticle interactions in the system.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="0220dddaeb927b02f058c682ce0da5fd" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725568,"asset_id":78813265,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725568/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813265"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813265"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813265; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813265]").text(description); $(".js-view-count[data-work-id=78813265]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813265; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813265']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813265, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "0220dddaeb927b02f058c682ce0da5fd" } } $('.js-work-strip[data-work-id=78813265]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813265,"title":"Morphological changes of glass bead particles upon an abrasive blasting as characterized by settling and flotation experiments","translated_title":"","metadata":{"publisher":"Politechnika Wroclawska Oficyna Wydawnicza","grobid_abstract":"The recent developments in mineral processing led researchers to look for alternative methods and propose new mechanisms for enhancing the efficiency of relatively costly processes (e.g., flotation, aggregation), where especially dealing with fine particles. Finer the particles, the higher the role of their surface on their behavior and properties. The importance of particle morphology becomes even clearer when particle-particle and particle-bubble interactions are considered. In this study, the effect of particle shape \"roundness\" on the surface wettability and flotation response was investigated upon producing fine particles with the \"abrasion blasting\" method. In order to provide a fundamental perspective, adsorption measurements were also carried out along with the flotation experiments under the same conditions. In addition to these, zeta potential measurements were also carried out with both spherical and blasted particles as a function of collector concentration. The results suggested that the roundness of particles decreased up to a certain nozzle pressure value, which was followed by higher adsorption degrees and consequently higher flotation recoveries. Additionally, settling rate tests were also performed with very fine material to show the effect of particle morphology on particle-particle interactions. The results showed that while lower settling rate values were obtained for spherical ones, higher values were obtained in the case of the ground and blasted samples in the presence of DI water. 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Finer the particles, the higher the role of their surface on their behavior and properties. The importance of particle morphology becomes even clearer when particle-particle and particle-bubble interactions are considered. In this study, the effect of particle shape \"roundness\" on the surface wettability and flotation response was investigated upon producing fine particles with the \"abrasion blasting\" method. In order to provide a fundamental perspective, adsorption measurements were also carried out along with the flotation experiments under the same conditions. In addition to these, zeta potential measurements were also carried out with both spherical and blasted particles as a function of collector concentration. The results suggested that the roundness of particles decreased up to a certain nozzle pressure value, which was followed by higher adsorption degrees and consequently higher flotation recoveries. Additionally, settling rate tests were also performed with very fine material to show the effect of particle morphology on particle-particle interactions. The results showed that while lower settling rate values were obtained for spherical ones, higher values were obtained in the case of the ground and blasted samples in the presence of DI water. It was concluded from this study that the \"Abrasive blasting method\" could be an effective alternative for tuning the surface morphology of particles and their wettability, which in turn can affect the particleparticle interactions in the system.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[{"id":85725568,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725568/thumbnails/1.jpg","file_name":"pdf-133288-62131.pdf","download_url":"https://www.academia.edu/attachments/85725568/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Morphological_changes_of_glass_bead_part.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725568/pdf-133288-62131-libre.pdf?1652083217=\u0026response-content-disposition=attachment%3B+filename%3DMorphological_changes_of_glass_bead_part.pdf\u0026Expires=1733935166\u0026Signature=YcDjBm6yzoV0SSUVlJw~-nxeOoyXcbac1iq7NtVYG7KIpXk9jRMcIVoW7Nma~52xZRK82Vy9nBD~eBd6VzptVv0tGnOVfxxF8fC~mCAdNaMzSDUIVB6QerGomIlfuyivGfI4cI2DFm5VXBsiHJp5fGE6zGr8Hl-3nSrTuJG6MAavSb6uj~vUudxlJgXOv2oDxVOqCoGB2lHd~lAmPuyefl~Sa8klg9uwqoHJqLUeCnc~AhBk1toyICtpICDimo--Sdjwt~0Sj~wV6k~~fIYbjJUT5cPJVYFZepN0Tyl7dCHMwuWEe-yNVbGXJkqua3TkMFvy5umAEUjnxJGRGFqYMw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813262"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813262/Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation"><img alt="Research paper thumbnail of Effect of Surface Roughness on Interaction of Particles in Flotation" class="work-thumbnail" src="https://attachments.academia-assets.com/85725513/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813262/Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation">Effect of Surface Roughness on Interaction of Particles in Flotation</a></div><div class="wp-workCard_item"><span>Physicochemical Problems of Mineral Processing</span><span>, 2015</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In this study, the effect of roughness of particles on flotation efficiency along with surface fo...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. The interaction forces between the glass beads changed from repulsion to attraction with the increasing hexadecyltrimethylammonium bromide (HTAB) concentration. ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="c2648191a6d7988a3f15bb466ff992e9" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725513,"asset_id":78813262,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725513/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813262"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813262"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813262; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813262]").text(description); $(".js-view-count[data-work-id=78813262]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813262; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813262']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813262, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "c2648191a6d7988a3f15bb466ff992e9" } } $('.js-work-strip[data-work-id=78813262]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813262,"title":"Effect of Surface Roughness on Interaction of Particles in Flotation","translated_title":"","metadata":{"abstract":"In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. The interaction forces between the glass beads changed from repulsion to attraction with the increasing hexadecyltrimethylammonium bromide (HTAB) concentration. ...","publication_date":{"day":null,"month":null,"year":2015,"errors":{}},"publication_name":"Physicochemical Problems of Mineral Processing"},"translated_abstract":"In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. The interaction forces between the glass beads changed from repulsion to attraction with the increasing hexadecyltrimethylammonium bromide (HTAB) concentration. ...","internal_url":"https://www.academia.edu/78813262/Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation","translated_internal_url":"","created_at":"2022-05-08T23:40:34.352-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":85725513,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725513/thumbnails/1.jpg","file_name":"ppmp52-1.18-34.pdf","download_url":"https://www.academia.edu/attachments/85725513/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Effect_of_Surface_Roughness_on_Interacti.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725513/ppmp52-1.18-34-libre.pdf?1652083971=\u0026response-content-disposition=attachment%3B+filename%3DEffect_of_Surface_Roughness_on_Interacti.pdf\u0026Expires=1733935166\u0026Signature=MlLQsHYjoIuuHifcRn~6oYjRxwtbK6LVbC95NkfpwdLmWrn8vLACY44ehk2Z172reFkCDNtkHpe2fNJQPQhABNyxGos0h6G15tuvZTcS4zNaeyd6tpwaXJ6iTDHZGns7shiLkSbv9U9-kbjL6hnOXK7SV1pNwzUp8ZGUxz4sKEC4XWsiJ8i9ZG6n0SLBv~riwSx~UbJTg1onSAxH14yngRiYmgQRFi3LEzZ1DpOa7QmAdegz2ZRyo0BN8rJ6GURDOfVX3EyigmcQ~hbDSG48-D0sVH9-wRLyWZp7z~26FQKfzc32Y1sGDeThiiPikHRNd63FtAMfi4D8uhCHdq9nug__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation","translated_slug":"","page_count":17,"language":"en","content_type":"Work","summary":"In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. The interaction forces between the glass beads changed from repulsion to attraction with the increasing hexadecyltrimethylammonium bromide (HTAB) concentration. ...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[{"id":85725513,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725513/thumbnails/1.jpg","file_name":"ppmp52-1.18-34.pdf","download_url":"https://www.academia.edu/attachments/85725513/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Effect_of_Surface_Roughness_on_Interacti.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725513/ppmp52-1.18-34-libre.pdf?1652083971=\u0026response-content-disposition=attachment%3B+filename%3DEffect_of_Surface_Roughness_on_Interacti.pdf\u0026Expires=1733935166\u0026Signature=MlLQsHYjoIuuHifcRn~6oYjRxwtbK6LVbC95NkfpwdLmWrn8vLACY44ehk2Z172reFkCDNtkHpe2fNJQPQhABNyxGos0h6G15tuvZTcS4zNaeyd6tpwaXJ6iTDHZGns7shiLkSbv9U9-kbjL6hnOXK7SV1pNwzUp8ZGUxz4sKEC4XWsiJ8i9ZG6n0SLBv~riwSx~UbJTg1onSAxH14yngRiYmgQRFi3LEzZ1DpOa7QmAdegz2ZRyo0BN8rJ6GURDOfVX3EyigmcQ~hbDSG48-D0sVH9-wRLyWZp7z~26FQKfzc32Y1sGDeThiiPikHRNd63FtAMfi4D8uhCHdq9nug__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":33296,"name":"Surface Roughness","url":"https://www.academia.edu/Documents/in/Surface_Roughness"},{"id":1342788,"name":"Surface Finish","url":"https://www.academia.edu/Documents/in/Surface_Finish"}],"urls":[{"id":20345475,"url":"http://www.minproc.pwr.wroc.pl/journal/pdf/ppmp52-1.18-34.pdf"}]}, dispatcherData: dispatcherData }); 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813257"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813257/The_significance_of_positive_and_negative_inertial_forces_in_Particle_Bubble_interaction_and_their_role_in_the_general_flotation_kinetics_model"><img alt="Research paper thumbnail of The significance of positive and negative inertial forces in Particle-Bubble interaction and their role in the general flotation kinetics model" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813257/The_significance_of_positive_and_negative_inertial_forces_in_Particle_Bubble_interaction_and_their_role_in_the_general_flotation_kinetics_model">The significance of positive and negative inertial forces in Particle-Bubble interaction and their role in the general flotation kinetics model</a></div><div class="wp-workCard_item"><span>Minerals Engineering</span><span>, 2021</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bub...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bubble interactions during the flotation process is presented and supported by the experimental data. The effects of positive and negative inertial forces were analyzed by comparing the differences between the models, which either consider or neglect the inertial forces. The Sutherland collision model and the Nguyen attachment model that completely ignore the effect of particle’s inertial forces (inertialess models) were implemented into the general flotation kinetic model. The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. It was shown that the inertial forces should not be omitted in any flotation model amidst concerns over the complexity.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813257"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813257"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813257; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813257]").text(description); $(".js-view-count[data-work-id=78813257]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813257; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813257']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813257, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813257]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813257,"title":"The significance of positive and negative inertial forces in Particle-Bubble interaction and their role in the general flotation kinetics model","translated_title":"","metadata":{"abstract":"Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bubble interactions during the flotation process is presented and supported by the experimental data. The effects of positive and negative inertial forces were analyzed by comparing the differences between the models, which either consider or neglect the inertial forces. The Sutherland collision model and the Nguyen attachment model that completely ignore the effect of particle’s inertial forces (inertialess models) were implemented into the general flotation kinetic model. The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. 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The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. 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The effects of positive and negative inertial forces were analyzed by comparing the differences between the models, which either consider or neglect the inertial forces. The Sutherland collision model and the Nguyen attachment model that completely ignore the effect of particle’s inertial forces (inertialess models) were implemented into the general flotation kinetic model. The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. It was shown that the inertial forces should not be omitted in any flotation model amidst concerns over the complexity.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":498,"name":"Physics","url":"https://www.academia.edu/Documents/in/Physics"},{"id":512,"name":"Mechanics","url":"https://www.academia.edu/Documents/in/Mechanics"},{"id":20929,"name":"Minerals Engineering","url":"https://www.academia.edu/Documents/in/Minerals_Engineering"},{"id":152114,"name":"Bubble","url":"https://www.academia.edu/Documents/in/Bubble"},{"id":651530,"name":"Froth Flotation","url":"https://www.academia.edu/Documents/in/Froth_Flotation"}],"urls":[{"id":20345474,"url":"https://api.elsevier.com/content/article/PII:S0892687521002351?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813255"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813255/Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces"><img alt="Research paper thumbnail of Attachment, Coalescence, and Spreading of Carbon Dioxide Nanobubbles at Pyrite Surfaces" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813255/Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces">Attachment, Coalescence, and Spreading of Carbon Dioxide Nanobubbles at Pyrite Surfaces</a></div><div class="wp-workCard_item"><span>Langmuir</span><span>, 2018</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813255"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813255"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813255; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813255]").text(description); $(".js-view-count[data-work-id=78813255]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813255; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813255']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813255, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813255]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813255,"title":"Attachment, Coalescence, and Spreading of Carbon Dioxide Nanobubbles at Pyrite Surfaces","translated_title":"","metadata":{"abstract":"Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.","publisher":"American Chemical Society (ACS)","publication_date":{"day":null,"month":null,"year":2018,"errors":{}},"publication_name":"Langmuir"},"translated_abstract":"Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.","internal_url":"https://www.academia.edu/78813255/Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces","translated_internal_url":"","created_at":"2022-05-08T23:40:32.720-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":511,"name":"Materials 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$a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813254"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813254/Effect_of_roughness_and_shape_factor_on_flotation_characteristics_of_glass_beads"><img alt="Research paper thumbnail of Effect of roughness and shape factor on flotation characteristics of glass beads" class="work-thumbnail" src="https://attachments.academia-assets.com/85725586/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813254/Effect_of_roughness_and_shape_factor_on_flotation_characteristics_of_glass_beads">Effect of roughness and shape factor on flotation characteristics of glass beads</a></div><div class="wp-workCard_item"><span>Colloids and Surfaces A: Physicochemical and Engineering Aspects</span><span>, 2016</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">h i g h l i g h t s • Both roughness and shape factor stimulate the bubble particle attachment.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="f55c5cf044fb1ddec33cf1ddf0873fc3" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725586,"asset_id":78813254,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725586/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: 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class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813253/Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings"><img alt="Research paper thumbnail of Recovery of Petcock From Lime Calcination Process Tailings" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813253/Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings">Recovery of Petcock From Lime Calcination Process Tailings</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Having access to cheap and sustainable energy source is crucial for mineral processing plants. Th...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Having access to cheap and sustainable energy source is crucial for mineral processing plants. This fact becomes more critical in calcination processes like lime plants. Nowadays, due to its low price and high calorific value Petroleum coke (petcoke) is a quite fair alternative energy source for such plants. Unburned carbon is the main byproduct of lime calcination process which has significant calorific value and can be reused in system. This byproduct is thrown out by heat flux from flue of vertical furnace. This flux has also considerable amounts of lime which is stacked in petcoke layers forming waste mixture in the flue dust. Recently the recovery of this unburned carbon from exhausted gas stacks with flotation and some physical separation methods is conducted. As more reliable way to recover petcoke from waste mixture is found to be flotation process, in this study the effects of feed size, pH, frother and collectors in flotation is investigated and an optimum condition for pr...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813253"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813253"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813253; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813253]").text(description); $(".js-view-count[data-work-id=78813253]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813253; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813253']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813253, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813253]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813253,"title":"Recovery of Petcock From Lime Calcination Process Tailings","translated_title":"","metadata":{"abstract":"Having access to cheap and sustainable energy source is crucial for mineral processing plants. This fact becomes more critical in calcination processes like lime plants. Nowadays, due to its low price and high calorific value Petroleum coke (petcoke) is a quite fair alternative energy source for such plants. Unburned carbon is the main byproduct of lime calcination process which has significant calorific value and can be reused in system. This byproduct is thrown out by heat flux from flue of vertical furnace. This flux has also considerable amounts of lime which is stacked in petcoke layers forming waste mixture in the flue dust. Recently the recovery of this unburned carbon from exhausted gas stacks with flotation and some physical separation methods is conducted. As more reliable way to recover petcoke from waste mixture is found to be flotation process, in this study the effects of feed size, pH, frother and collectors in flotation is investigated and an optimum condition for pr..."},"translated_abstract":"Having access to cheap and sustainable energy source is crucial for mineral processing plants. This fact becomes more critical in calcination processes like lime plants. Nowadays, due to its low price and high calorific value Petroleum coke (petcoke) is a quite fair alternative energy source for such plants. Unburned carbon is the main byproduct of lime calcination process which has significant calorific value and can be reused in system. This byproduct is thrown out by heat flux from flue of vertical furnace. This flux has also considerable amounts of lime which is stacked in petcoke layers forming waste mixture in the flue dust. Recently the recovery of this unburned carbon from exhausted gas stacks with flotation and some physical separation methods is conducted. As more reliable way to recover petcoke from waste mixture is found to be flotation process, in this study the effects of feed size, pH, frother and collectors in flotation is investigated and an optimum condition for pr...","internal_url":"https://www.academia.edu/78813253/Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings","translated_internal_url":"","created_at":"2022-05-08T23:40:32.448-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Having access to cheap and sustainable energy source is crucial for mineral processing plants. This fact becomes more critical in calcination processes like lime plants. Nowadays, due to its low price and high calorific value Petroleum coke (petcoke) is a quite fair alternative energy source for such plants. Unburned carbon is the main byproduct of lime calcination process which has significant calorific value and can be reused in system. This byproduct is thrown out by heat flux from flue of vertical furnace. This flux has also considerable amounts of lime which is stacked in petcoke layers forming waste mixture in the flue dust. Recently the recovery of this unburned carbon from exhausted gas stacks with flotation and some physical separation methods is conducted. As more reliable way to recover petcoke from waste mixture is found to be flotation process, in this study the effects of feed size, pH, frother and collectors in flotation is investigated and an optimum condition for pr...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813252"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813252/Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant"><img alt="Research paper thumbnail of Utilization of Colemanite In Exterior Water Borne Paints As A Filler and Fire Retardant" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813252/Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant">Utilization of Colemanite In Exterior Water Borne Paints As A Filler and Fire Retardant</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Paint is mainly used for protection of a substrate; it is applied to prevent the surface from cor...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. Especially in exterior applications, the hydrophobic characteristic of the paints lead to protection against air humidity; moreover, some other properties such as fire retardancy and antibacterial effect of the paints may be required based on its utilization area. Mineral additives in paint constitute anywhere from 20 to 50% of the paint formulation. Due to such high proportion of mineral constituents in the paint system, the required properties of paints can be achieved by properly selecting minerals as fillers. In the present paper, the effect of colemanite, calcium containing boron mineral, has been tested as filler in architectural exterior paints. Paints produced using colemanite were subjected to both wet and dry paint analysis and found that this mineral has favorable effect on opacity and viscosity of the system. Furthermore; colemanite has a remarkable effect on retardin...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813252"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813252"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813252; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813252]").text(description); $(".js-view-count[data-work-id=78813252]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813252; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813252']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813252, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813252]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813252,"title":"Utilization of Colemanite In Exterior Water Borne Paints As A Filler and Fire Retardant","translated_title":"","metadata":{"abstract":"Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. Especially in exterior applications, the hydrophobic characteristic of the paints lead to protection against air humidity; moreover, some other properties such as fire retardancy and antibacterial effect of the paints may be required based on its utilization area. Mineral additives in paint constitute anywhere from 20 to 50% of the paint formulation. Due to such high proportion of mineral constituents in the paint system, the required properties of paints can be achieved by properly selecting minerals as fillers. In the present paper, the effect of colemanite, calcium containing boron mineral, has been tested as filler in architectural exterior paints. Paints produced using colemanite were subjected to both wet and dry paint analysis and found that this mineral has favorable effect on opacity and viscosity of the system. Furthermore; colemanite has a remarkable effect on retardin..."},"translated_abstract":"Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. Especially in exterior applications, the hydrophobic characteristic of the paints lead to protection against air humidity; moreover, some other properties such as fire retardancy and antibacterial effect of the paints may be required based on its utilization area. Mineral additives in paint constitute anywhere from 20 to 50% of the paint formulation. Due to such high proportion of mineral constituents in the paint system, the required properties of paints can be achieved by properly selecting minerals as fillers. In the present paper, the effect of colemanite, calcium containing boron mineral, has been tested as filler in architectural exterior paints. Paints produced using colemanite were subjected to both wet and dry paint analysis and found that this mineral has favorable effect on opacity and viscosity of the system. Furthermore; colemanite has a remarkable effect on retardin...","internal_url":"https://www.academia.edu/78813252/Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant","translated_internal_url":"","created_at":"2022-05-08T23:40:32.315-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. Especially in exterior applications, the hydrophobic characteristic of the paints lead to protection against air humidity; moreover, some other properties such as fire retardancy and antibacterial effect of the paints may be required based on its utilization area. Mineral additives in paint constitute anywhere from 20 to 50% of the paint formulation. Due to such high proportion of mineral constituents in the paint system, the required properties of paints can be achieved by properly selecting minerals as fillers. In the present paper, the effect of colemanite, calcium containing boron mineral, has been tested as filler in architectural exterior paints. Paints produced using colemanite were subjected to both wet and dry paint analysis and found that this mineral has favorable effect on opacity and viscosity of the system. Furthermore; colemanite has a remarkable effect on retardin...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813251"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813251/Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints"><img alt="Research paper thumbnail of Interaction Between TiO2 and Calcite-Calcined Kaolin Mixture During Grinding of Pigment in Water Based Paints" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813251/Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints">Interaction Between TiO2 and Calcite-Calcined Kaolin Mixture During Grinding of Pigment in Water Based Paints</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Water based paint formulations consist of some industrial minerals with quantities varying from 2...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813251"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813251"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813251; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813251]").text(description); $(".js-view-count[data-work-id=78813251]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813251; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813251']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813251, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813251]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813251,"title":"Interaction Between TiO2 and Calcite-Calcined Kaolin Mixture During Grinding of Pigment in Water Based Paints","translated_title":"","metadata":{"abstract":"Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c..."},"translated_abstract":"Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c...","internal_url":"https://www.academia.edu/78813251/Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints","translated_internal_url":"","created_at":"2022-05-08T23:40:32.143-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813250"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813250/The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites"><img alt="Research paper thumbnail of The Usage of Sodium Bentonite In Styrene Butyl Acrylate Composites" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813250/The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites">The Usage of Sodium Bentonite In Styrene Butyl Acrylate Composites</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In recent years, research on polymer composites with mineral fillers have received great interest...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813250"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813250"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813250; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813250]").text(description); $(".js-view-count[data-work-id=78813250]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813250; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813250']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813250, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813250]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813250,"title":"The Usage of Sodium Bentonite In Styrene Butyl Acrylate Composites","translated_title":"","metadata":{"abstract":"In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix."},"translated_abstract":"In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix.","internal_url":"https://www.academia.edu/78813250/The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites","translated_internal_url":"","created_at":"2022-05-08T23:40:31.984-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813246"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813246/Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints"><img alt="Research paper thumbnail of Substitution of TiO2 With PCC (Precipitated Calcium Carbonate) in Waterborne Paints" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813246/Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints">Substitution of TiO2 With PCC (Precipitated Calcium Carbonate) in Waterborne Paints</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Paints provide protection against any possible corrosion by forming a thin film layer on the mate...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813246"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813246"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813246; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813246]").text(description); $(".js-view-count[data-work-id=78813246]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813246; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813246']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813246, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813246]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813246,"title":"Substitution of TiO2 With PCC (Precipitated Calcium Carbonate) in Waterborne Paints","translated_title":"","metadata":{"abstract":"Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h..."},"translated_abstract":"Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h...","internal_url":"https://www.academia.edu/78813246/Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints","translated_internal_url":"","created_at":"2022-05-08T23:40:31.809-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813244"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813244/Kolemanit_ve_Bentonit_Katk%C4%B1l%C4%B1_Stiren_B%C3%BCtil_Akrilat_Kopolimeri_%C3%9Cretimi_ve_Karakterizasyonu"><img alt="Research paper thumbnail of Kolemanit ve Bentonit Katkılı Stiren-Bütil Akrilat Kopolimeri Üretimi ve Karakterizasyonu" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813244/Kolemanit_ve_Bentonit_Katk%C4%B1l%C4%B1_Stiren_B%C3%BCtil_Akrilat_Kopolimeri_%C3%9Cretimi_ve_Karakterizasyonu">Kolemanit ve Bentonit Katkılı Stiren-Bütil Akrilat Kopolimeri Üretimi ve Karakterizasyonu</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813244"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813244"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813244; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813244]").text(description); $(".js-view-count[data-work-id=78813244]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813244; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813244']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813244, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813244]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813244,"title":"Kolemanit ve Bentonit Katkılı Stiren-Bütil Akrilat Kopolimeri Üretimi ve Karakterizasyonu","translated_title":"","metadata":{"abstract":"Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo..."},"translated_abstract":"Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo...","internal_url":"https://www.academia.edu/78813244/Kolemanit_ve_Bentonit_Katk%C4%B1l%C4%B1_Stiren_B%C3%BCtil_Akrilat_Kopolimeri_%C3%9Cretimi_ve_Karakterizasyonu","translated_internal_url":"","created_at":"2022-05-08T23:40:31.664-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Kolemanit_ve_Bentonit_Katkılı_Stiren_Bütil_Akrilat_Kopolimeri_Üretimi_ve_Karakterizasyonu","translated_slug":"","page_count":null,"language":"tr","content_type":"Work","summary":"Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813242"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813242/Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings"><img alt="Research paper thumbnail of Flotation kinetics for Recovery of Petcoke from Lime Calcination Plant Tailings" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813242/Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings">Flotation kinetics for Recovery of Petcoke from Lime Calcination Plant Tailings</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Flotation models are very useful for quantifying the practical work and also to assist in the des...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813242"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813242"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813242; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813242]").text(description); $(".js-view-count[data-work-id=78813242]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813242; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813242']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813242, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813242]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813242,"title":"Flotation kinetics for Recovery of Petcoke from Lime Calcination Plant Tailings","translated_title":"","metadata":{"abstract":"Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution."},"translated_abstract":"Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution.","internal_url":"https://www.academia.edu/78813242/Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings","translated_internal_url":"","created_at":"2022-05-08T23:40:31.534-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813241"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813241/Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering"><img alt="Research paper thumbnail of Effect of hydrophilic lipophilic balance (HLB) of nonionic surfactants on ultrafine lignite dewatering" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813241/Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering">Effect of hydrophilic lipophilic balance (HLB) of nonionic surfactants on ultrafine lignite dewatering</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Since dewatering is a costly process, removal of moisture from relatively fine size lignites is a...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813241"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813241"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813241; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813241]").text(description); $(".js-view-count[data-work-id=78813241]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813241; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813241']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813241, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813241]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813241,"title":"Effect of hydrophilic lipophilic balance (HLB) of nonionic surfactants on ultrafine lignite dewatering","translated_title":"","metadata":{"abstract":"Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom..."},"translated_abstract":"Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom...","internal_url":"https://www.academia.edu/78813241/Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering","translated_internal_url":"","created_at":"2022-05-08T23:40:31.380-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813240"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813240/Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints"><img alt="Research paper thumbnail of Calcined Kaolin and Calcite as a Pigment and Substitute for TiO2 in Water Based Paints" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813240/Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints">Calcined Kaolin and Calcite as a Pigment and Substitute for TiO2 in Water Based Paints</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particul...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813240"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813240"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813240; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813240]").text(description); $(".js-view-count[data-work-id=78813240]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813240; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813240']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813240, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813240]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813240,"title":"Calcined Kaolin and Calcite as a Pigment and Substitute for TiO2 in Water Based Paints","translated_title":"","metadata":{"abstract":"Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality."},"translated_abstract":"Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality.","internal_url":"https://www.academia.edu/78813240/Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints","translated_internal_url":"","created_at":"2022-05-08T23:40:31.258-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813239"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813239/Effect_of_precipitated_calcium_carbonate_additions_on_waterborne_paints_at_different_pigment_volume_concentrations"><img alt="Research paper thumbnail of Effect of precipitated calcium carbonate additions on waterborne paints at different pigment volume concentrations" class="work-thumbnail" src="https://attachments.academia-assets.com/85725573/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813239/Effect_of_precipitated_calcium_carbonate_additions_on_waterborne_paints_at_different_pigment_volume_concentrations">Effect of precipitated calcium carbonate additions on waterborne paints at different pigment volume concentrations</a></div><div class="wp-workCard_item"><span>Progress in Organic Coatings</span><span>, 2015</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Titanium dioxide (TiO 2) due to its high refractive index, is widely used in paint industry as a ...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Titanium dioxide (TiO 2) due to its high refractive index, is widely used in paint industry as a white pigment. In order to reduce this high cost of TiO 2 , a part of TiO 2 is generally substituted by some other industrial mineral fillers such as calcite and calcined kaolin; however, this substitution affects the quality of paints in terms of stability, coverage (opacity), brightness (gloss), scrub resistance (film toughness), etc. In the present paper, precipitated calcium carbonate (PCC) was substituted for TiO 2 in paint mixture at three different pigment volume concentrations (PVC). It was observed that substitution of TiO 2 by PCC depends on PVC value at which there is an optimum PCC amount. The quality of paints produced by PCC along with its rheological properties was evaluated based on standard features in both wet and dry paints such as viscosity, density, opacity and gloss values. Addition of PCC increases the opacity to a certain point. Similarly, scrub resistance and viscosity increases with the addition of PCC at all PVCs, however, viscosity is not as much critical for the paint production. On the other hand, there is no any systematic effect of PCC on gloss value of the paint. This study overall demonstrates that PCC can be successfully used to substitute TiO 2 only with a careful adjustment of PVC and other extenders used in the paint formulation.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="e022fe2a04d990df6583580363663bbc" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725573,"asset_id":78813239,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725573/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813239"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813239"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813239; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813239]").text(description); $(".js-view-count[data-work-id=78813239]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813239; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813239']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813239, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "e022fe2a04d990df6583580363663bbc" } } $('.js-work-strip[data-work-id=78813239]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813239,"title":"Effect of precipitated calcium carbonate additions on waterborne paints at different pigment volume concentrations","translated_title":"","metadata":{"publisher":"Elsevier BV","grobid_abstract":"Titanium dioxide (TiO 2) due to its high refractive index, is widely used in paint industry as a white pigment. In order to reduce this high cost of TiO 2 , a part of TiO 2 is generally substituted by some other industrial mineral fillers such as calcite and calcined kaolin; however, this substitution affects the quality of paints in terms of stability, coverage (opacity), brightness (gloss), scrub resistance (film toughness), etc. In the present paper, precipitated calcium carbonate (PCC) was substituted for TiO 2 in paint mixture at three different pigment volume concentrations (PVC). It was observed that substitution of TiO 2 by PCC depends on PVC value at which there is an optimum PCC amount. The quality of paints produced by PCC along with its rheological properties was evaluated based on standard features in both wet and dry paints such as viscosity, density, opacity and gloss values. Addition of PCC increases the opacity to a certain point. Similarly, scrub resistance and viscosity increases with the addition of PCC at all PVCs, however, viscosity is not as much critical for the paint production. On the other hand, there is no any systematic effect of PCC on gloss value of the paint. This study overall demonstrates that PCC can be successfully used to substitute TiO 2 only with a careful adjustment of PVC and other extenders used in the paint formulation.","publication_date":{"day":null,"month":null,"year":2015,"errors":{}},"publication_name":"Progress in Organic Coatings","grobid_abstract_attachment_id":85725573},"translated_abstract":null,"internal_url":"https://www.academia.edu/78813239/Effect_of_precipitated_calcium_carbonate_additions_on_waterborne_paints_at_different_pigment_volume_concentrations","translated_internal_url":"","created_at":"2022-05-08T23:40:31.105-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":85725573,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725573/thumbnails/1.jpg","file_name":"j.porgcoat.2015.02.00320220509-1-1yrp1te.pdf","download_url":"https://www.academia.edu/attachments/85725573/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Effect_of_precipitated_calcium_carbonate.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725573/j.porgcoat.2015.02.00320220509-1-1yrp1te-libre.pdf?1652083236=\u0026response-content-disposition=attachment%3B+filename%3DEffect_of_precipitated_calcium_carbonate.pdf\u0026Expires=1733935166\u0026Signature=YcCLzRd0BlZrh3mjQYyHARzp3G4~og55bvaXy4GofuryDifkH~2bAgkPXdKwSmpErOvHVQ7SSZ8ZFAQW-SLirGevt-5Ne5DpfieMLQ9BSdvJ6mtxIRSWME5pSfVWxjnMei1JMNxpx7NG5lfs4F1MYELWzPjqS1MwwLQMYoSx0Db7xJ~qcsBeaipHIRp56XQAQ0VBKgS7TVpwm8izDbC3GSiMOTEhq2GLw3obQwmKHhHljHggmB9oCGzmEYbsW9iV1XQAjYrfJLmAYD2Nj~lHAIbzeJUNhUK5LIhCogCV175wMTk9udCePnmWzoA8hZ~EjpF5IAKpT9rxCaEGtBJ4lw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Effect_of_precipitated_calcium_carbonate_additions_on_waterborne_paints_at_different_pigment_volume_concentrations","translated_slug":"","page_count":7,"language":"en","content_type":"Work","summary":"Titanium dioxide (TiO 2) due to its high refractive index, is widely used in paint industry as a white pigment. In order to reduce this high cost of TiO 2 , a part of TiO 2 is generally substituted by some other industrial mineral fillers such as calcite and calcined kaolin; however, this substitution affects the quality of paints in terms of stability, coverage (opacity), brightness (gloss), scrub resistance (film toughness), etc. In the present paper, precipitated calcium carbonate (PCC) was substituted for TiO 2 in paint mixture at three different pigment volume concentrations (PVC). It was observed that substitution of TiO 2 by PCC depends on PVC value at which there is an optimum PCC amount. The quality of paints produced by PCC along with its rheological properties was evaluated based on standard features in both wet and dry paints such as viscosity, density, opacity and gloss values. Addition of PCC increases the opacity to a certain point. Similarly, scrub resistance and viscosity increases with the addition of PCC at all PVCs, however, viscosity is not as much critical for the paint production. On the other hand, there is no any systematic effect of PCC on gloss value of the paint. This study overall demonstrates that PCC can be successfully used to substitute TiO 2 only with a careful adjustment of PVC and other extenders used in the paint formulation.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[{"id":85725573,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725573/thumbnails/1.jpg","file_name":"j.porgcoat.2015.02.00320220509-1-1yrp1te.pdf","download_url":"https://www.academia.edu/attachments/85725573/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Effect_of_precipitated_calcium_carbonate.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725573/j.porgcoat.2015.02.00320220509-1-1yrp1te-libre.pdf?1652083236=\u0026response-content-disposition=attachment%3B+filename%3DEffect_of_precipitated_calcium_carbonate.pdf\u0026Expires=1733935166\u0026Signature=YcCLzRd0BlZrh3mjQYyHARzp3G4~og55bvaXy4GofuryDifkH~2bAgkPXdKwSmpErOvHVQ7SSZ8ZFAQW-SLirGevt-5Ne5DpfieMLQ9BSdvJ6mtxIRSWME5pSfVWxjnMei1JMNxpx7NG5lfs4F1MYELWzPjqS1MwwLQMYoSx0Db7xJ~qcsBeaipHIRp56XQAQ0VBKgS7TVpwm8izDbC3GSiMOTEhq2GLw3obQwmKHhHljHggmB9oCGzmEYbsW9iV1XQAjYrfJLmAYD2Nj~lHAIbzeJUNhUK5LIhCogCV175wMTk9udCePnmWzoA8hZ~EjpF5IAKpT9rxCaEGtBJ4lw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering"},{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813237"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813237/Ultrafine_coal_dewatering_Relationship_between_hydrophilic_lipophilic_balance_HLB_of_surfactants_and_coal_rank"><img alt="Research paper thumbnail of Ultrafine coal dewatering: Relationship between hydrophilic lipophilic balance (HLB) of surfactants and coal rank" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813237/Ultrafine_coal_dewatering_Relationship_between_hydrophilic_lipophilic_balance_HLB_of_surfactants_and_coal_rank">Ultrafine coal dewatering: Relationship between hydrophilic lipophilic balance (HLB) of surfactants and coal rank</a></div><div class="wp-workCard_item"><span>International Journal of Mineral Processing</span><span>, 2014</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washin...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washing plants. This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. The governing mechanisms are discussed in the light of hydrophilicity index and modification of physicochemical conditions.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813237"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813237"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813237; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813237]").text(description); $(".js-view-count[data-work-id=78813237]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813237; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813237']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813237, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813237]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813237,"title":"Ultrafine coal dewatering: Relationship between hydrophilic lipophilic balance (HLB) of surfactants and coal rank","translated_title":"","metadata":{"abstract":"ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washing plants. This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. The governing mechanisms are discussed in the light of hydrophilicity index and modification of physicochemical conditions.","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2014,"errors":{}},"publication_name":"International Journal of Mineral Processing"},"translated_abstract":"ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washing plants. This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. The governing mechanisms are discussed in the light of hydrophilicity index and modification of physicochemical conditions.","internal_url":"https://www.academia.edu/78813237/Ultrafine_coal_dewatering_Relationship_between_hydrophilic_lipophilic_balance_HLB_of_surfactants_and_coal_rank","translated_internal_url":"","created_at":"2022-05-08T23:40:30.941-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Ultrafine_coal_dewatering_Relationship_between_hydrophilic_lipophilic_balance_HLB_of_surfactants_and_coal_rank","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washing plants. This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. The governing mechanisms are discussed in the light of hydrophilicity index and modification of physicochemical conditions.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":10743,"name":"Coal","url":"https://www.academia.edu/Documents/in/Coal"},{"id":14366,"name":"Mineral Processing","url":"https://www.academia.edu/Documents/in/Mineral_Processing"},{"id":48526,"name":"Surfactants","url":"https://www.academia.edu/Documents/in/Surfactants"},{"id":449951,"name":"Lignite","url":"https://www.academia.edu/Documents/in/Lignite"},{"id":911313,"name":"Dewatering","url":"https://www.academia.edu/Documents/in/Dewatering"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> </div><div class="profile--tab_content_container js-tab-pane tab-pane" data-section-id="247700" id="papers"><div class="js-work-strip profile--work_container" data-work-id="78813275"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813275/Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects"><img alt="Research paper thumbnail of Effect of bubble size and velocity on collision efficiency in chalcopyrite flotation A Physicochemical and engineering aspects" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813275/Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects">Effect of bubble size and velocity on collision efficiency in chalcopyrite flotation A Physicochemical and engineering aspects</a></div><div class="wp-workCard_item"><span>Colloids and Surfaces</span><span>, 2016</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key fa...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813275"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813275"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813275; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813275]").text(description); $(".js-view-count[data-work-id=78813275]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813275; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813275']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813275, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813275]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813275,"title":"Effect of bubble size and velocity on collision efficiency in chalcopyrite flotation A Physicochemical and engineering aspects","translated_title":"","metadata":{"abstract":"In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.","publisher":"Elsevier","publication_date":{"day":null,"month":null,"year":2016,"errors":{}},"publication_name":"Colloids and Surfaces"},"translated_abstract":"In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.","internal_url":"https://www.academia.edu/78813275/Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects","translated_internal_url":"","created_at":"2022-05-08T23:40:35.405-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Effect_of_bubble_size_and_velocity_on_collision_efficiency_in_chalcopyrite_flotation_A_Physicochemical_and_engineering_aspects","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"In flotation processes, bubble diameter (db), bubble velocity (vb), and turbulence are the key factors involved in particle-bubble interactions. The collision efficiency (EC) is used as an indicator to assess the extent of these interactions. In this work, the bubble surface is assumed mobile with potential flow conditions dominating the particle-bubble collision efficiency. The collision probability has been determined by Schulze and Generalized Sutherland Equation (GSE) models in the particle size range of 1–100 μm. Bubble diameters of 0.08, 0.12, and 0.15 cm and bubble velocities of 10, 20 and 30 cm/s were selected to study the flotation of chalcopyrite. The results reveal that the collision efficiency of ultra-fine particles (1–10 μm) is generally improved with bubbles of finer sizes, e.g. db = 0.08 cm compared to those of larger sizes, i.e. db = 0.12 and db = 0.15 cm. Also, in the same particle size range, EC decreases with increasing the bubble velocity. The best agreement between Schulze and GSE models for ultra-fine particles at all bubble sizes is achieved at the bubble velocity of 30 cm/s. The maximum EC of chalcopyrite (0.12) using the GSE model is found to occur for coarser particles of 70–100 μm in size at bubble conditions of vb = 30 cm/s and db = 0.12 cm. Results reveal that for a given bubble diameter increasing the bubble velocity from 10 to 30 cm/s makes the inertial force more effective on finer particles. A detailed interpretation of the effect of bubble diameter and its velocity on particle-bubble interaction of chalcopyrite is discussed from a theoretical point of view.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":3746,"name":"Colloids and Surfaces","url":"https://www.academia.edu/Documents/in/Colloids_and_Surfaces"},{"id":118582,"name":"Physical sciences","url":"https://www.academia.edu/Documents/in/Physical_sciences"},{"id":152114,"name":"Bubble","url":"https://www.academia.edu/Documents/in/Bubble"},{"id":238108,"name":"Chalcopyrite","url":"https://www.academia.edu/Documents/in/Chalcopyrite"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"}],"urls":[{"id":20345483,"url":"https://pubag.nal.usda.gov/catalog/5529472"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813271"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813271/Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage"><img alt="Research paper thumbnail of Effect of various ligands on the selective precipitation of critical and rare earth elements from acid mine drainage" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813271/Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage">Effect of various ligands on the selective precipitation of critical and rare earth elements from acid mine drainage</a></div><div class="wp-workCard_item"><span>Chemosphere</span><span>, 2021</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813271"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813271"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813271; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813271]").text(description); $(".js-view-count[data-work-id=78813271]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813271; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813271']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813271, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813271]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813271,"title":"Effect of various ligands on the selective precipitation of critical and rare earth elements from acid mine drainage","translated_title":"","metadata":{"abstract":"Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2021,"errors":{}},"publication_name":"Chemosphere"},"translated_abstract":"Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.","internal_url":"https://www.academia.edu/78813271/Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage","translated_internal_url":"","created_at":"2022-05-08T23:40:35.144-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Effect_of_various_ligands_on_the_selective_precipitation_of_critical_and_rare_earth_elements_from_acid_mine_drainage","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Acid mine drainage (AMD) has been of environmental concern for decades but recently found to be a viable source of critical elements including rare earth elements (REEs). Recovery of these elements while treating AMD for environmental compliance improves the sustainability of the treatment process. The precipitation behavior of the REEs and other cations during the AMD neutralization process depends strongly on the solution chemistry, available ligands, and concentration of elements. Several chemicals were used to study the effect of various ions/ligands (i.e., OH-, SO42-, NH4+, CO32-, and PO43-) on precipitation behavior of REEs and other elements from AMD as a function of pH. It was found that only up to 70% of total REEs can be recovered using NaOH at circumneutral pH. (NH4)OH suppressed the precipitation of REEs up to pH 8. The presence of phosphate and carbonate ions in the solution increased the precipitation yield of REEs at lower pH values. Both Na2HPO4 and Na2CO3 were found to increase the precipitation of REEs at pH below 7, as over 85% of REEs were recovered. Calculated saturation indices and speciation diagrams for selected REEs confirmed the experimental data. Considering the elemental recovery values, environmental effects, as well as chemical consumption and cost, a two-step AMD treatment process using Na2CO3 was formulated. Through the proposed process, 90% of the aluminum was recovered in the first step (at pH 5), while 85% of REEs was recovered in the second step (at pH 7) with a significantly high concentration of 1.6%.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":7967,"name":"Acid Mine Drainage","url":"https://www.academia.edu/Documents/in/Acid_Mine_Drainage"},{"id":26327,"name":"Medicine","url":"https://www.academia.edu/Documents/in/Medicine"},{"id":28235,"name":"Multidisciplinary","url":"https://www.academia.edu/Documents/in/Multidisciplinary"},{"id":395801,"name":"Rare Earth","url":"https://www.academia.edu/Documents/in/Rare_Earth"}],"urls":[{"id":20345480,"url":"https://api.elsevier.com/content/article/PII:S0045653521011553?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813268"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813268/Microwave_assisted_calcination_of_spodumene_for_efficient_low_cost_and_environmentally_friendly_extraction_of_lithium"><img alt="Research paper thumbnail of Microwave-assisted calcination of spodumene for efficient, low-cost and environmentally friendly extraction of lithium" class="work-thumbnail" src="https://attachments.academia-assets.com/85725565/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813268/Microwave_assisted_calcination_of_spodumene_for_efficient_low_cost_and_environmentally_friendly_extraction_of_lithium">Microwave-assisted calcination of spodumene for efficient, low-cost and environmentally friendly extraction of lithium</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 2021</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="23d113a911a837b6404c2740f9866819" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725565,"asset_id":78813268,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725565/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813268"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813268"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813268; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813268]").text(description); $(".js-view-count[data-work-id=78813268]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813268; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813268']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813268, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813265"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813265/Morphological_changes_of_glass_bead_particles_upon_an_abrasive_blasting_as_characterized_by_settling_and_flotation_experiments"><img alt="Research paper thumbnail of Morphological changes of glass bead particles upon an abrasive blasting as characterized by settling and flotation experiments" class="work-thumbnail" src="https://attachments.academia-assets.com/85725568/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813265/Morphological_changes_of_glass_bead_particles_upon_an_abrasive_blasting_as_characterized_by_settling_and_flotation_experiments">Morphological changes of glass bead particles upon an abrasive blasting as characterized by settling and flotation experiments</a></div><div class="wp-workCard_item"><span>Physicochemical Problems of Mineral Processing</span><span>, 2021</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The recent developments in mineral processing led researchers to look for alternative methods and...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">The recent developments in mineral processing led researchers to look for alternative methods and propose new mechanisms for enhancing the efficiency of relatively costly processes (e.g., flotation, aggregation), where especially dealing with fine particles. Finer the particles, the higher the role of their surface on their behavior and properties. The importance of particle morphology becomes even clearer when particle-particle and particle-bubble interactions are considered. In this study, the effect of particle shape "roundness" on the surface wettability and flotation response was investigated upon producing fine particles with the "abrasion blasting" method. In order to provide a fundamental perspective, adsorption measurements were also carried out along with the flotation experiments under the same conditions. In addition to these, zeta potential measurements were also carried out with both spherical and blasted particles as a function of collector concentration. The results suggested that the roundness of particles decreased up to a certain nozzle pressure value, which was followed by higher adsorption degrees and consequently higher flotation recoveries. Additionally, settling rate tests were also performed with very fine material to show the effect of particle morphology on particle-particle interactions. The results showed that while lower settling rate values were obtained for spherical ones, higher values were obtained in the case of the ground and blasted samples in the presence of DI water. It was concluded from this study that the "Abrasive blasting method" could be an effective alternative for tuning the surface morphology of particles and their wettability, which in turn can affect the particleparticle interactions in the system.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="0220dddaeb927b02f058c682ce0da5fd" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725568,"asset_id":78813265,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725568/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813265"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813265"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813265; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813265]").text(description); $(".js-view-count[data-work-id=78813265]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813265; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813265']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813265, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "0220dddaeb927b02f058c682ce0da5fd" } } $('.js-work-strip[data-work-id=78813265]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813265,"title":"Morphological changes of glass bead particles upon an abrasive blasting as characterized by settling and flotation experiments","translated_title":"","metadata":{"publisher":"Politechnika Wroclawska Oficyna Wydawnicza","grobid_abstract":"The recent developments in mineral processing led researchers to look for alternative methods and propose new mechanisms for enhancing the efficiency of relatively costly processes (e.g., flotation, aggregation), where especially dealing with fine particles. Finer the particles, the higher the role of their surface on their behavior and properties. The importance of particle morphology becomes even clearer when particle-particle and particle-bubble interactions are considered. In this study, the effect of particle shape \"roundness\" on the surface wettability and flotation response was investigated upon producing fine particles with the \"abrasion blasting\" method. In order to provide a fundamental perspective, adsorption measurements were also carried out along with the flotation experiments under the same conditions. In addition to these, zeta potential measurements were also carried out with both spherical and blasted particles as a function of collector concentration. The results suggested that the roundness of particles decreased up to a certain nozzle pressure value, which was followed by higher adsorption degrees and consequently higher flotation recoveries. Additionally, settling rate tests were also performed with very fine material to show the effect of particle morphology on particle-particle interactions. The results showed that while lower settling rate values were obtained for spherical ones, higher values were obtained in the case of the ground and blasted samples in the presence of DI water. It was concluded from this study that the \"Abrasive blasting method\" could be an effective alternative for tuning the surface morphology of particles and their wettability, which in turn can affect the particleparticle interactions in the system.","publication_date":{"day":null,"month":null,"year":2021,"errors":{}},"publication_name":"Physicochemical Problems of Mineral Processing","grobid_abstract_attachment_id":85725568},"translated_abstract":null,"internal_url":"https://www.academia.edu/78813265/Morphological_changes_of_glass_bead_particles_upon_an_abrasive_blasting_as_characterized_by_settling_and_flotation_experiments","translated_internal_url":"","created_at":"2022-05-08T23:40:34.605-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":85725568,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725568/thumbnails/1.jpg","file_name":"pdf-133288-62131.pdf","download_url":"https://www.academia.edu/attachments/85725568/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Morphological_changes_of_glass_bead_part.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725568/pdf-133288-62131-libre.pdf?1652083217=\u0026response-content-disposition=attachment%3B+filename%3DMorphological_changes_of_glass_bead_part.pdf\u0026Expires=1733935166\u0026Signature=YcDjBm6yzoV0SSUVlJw~-nxeOoyXcbac1iq7NtVYG7KIpXk9jRMcIVoW7Nma~52xZRK82Vy9nBD~eBd6VzptVv0tGnOVfxxF8fC~mCAdNaMzSDUIVB6QerGomIlfuyivGfI4cI2DFm5VXBsiHJp5fGE6zGr8Hl-3nSrTuJG6MAavSb6uj~vUudxlJgXOv2oDxVOqCoGB2lHd~lAmPuyefl~Sa8klg9uwqoHJqLUeCnc~AhBk1toyICtpICDimo--Sdjwt~0Sj~wV6k~~fIYbjJUT5cPJVYFZepN0Tyl7dCHMwuWEe-yNVbGXJkqua3TkMFvy5umAEUjnxJGRGFqYMw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Morphological_changes_of_glass_bead_particles_upon_an_abrasive_blasting_as_characterized_by_settling_and_flotation_experiments","translated_slug":"","page_count":12,"language":"en","content_type":"Work","summary":"The recent developments in mineral processing led researchers to look for alternative methods and propose new mechanisms for enhancing the efficiency of relatively costly processes (e.g., flotation, aggregation), where especially dealing with fine particles. Finer the particles, the higher the role of their surface on their behavior and properties. The importance of particle morphology becomes even clearer when particle-particle and particle-bubble interactions are considered. In this study, the effect of particle shape \"roundness\" on the surface wettability and flotation response was investigated upon producing fine particles with the \"abrasion blasting\" method. In order to provide a fundamental perspective, adsorption measurements were also carried out along with the flotation experiments under the same conditions. In addition to these, zeta potential measurements were also carried out with both spherical and blasted particles as a function of collector concentration. The results suggested that the roundness of particles decreased up to a certain nozzle pressure value, which was followed by higher adsorption degrees and consequently higher flotation recoveries. Additionally, settling rate tests were also performed with very fine material to show the effect of particle morphology on particle-particle interactions. The results showed that while lower settling rate values were obtained for spherical ones, higher values were obtained in the case of the ground and blasted samples in the presence of DI water. It was concluded from this study that the \"Abrasive blasting method\" could be an effective alternative for tuning the surface morphology of particles and their wettability, which in turn can affect the particleparticle interactions in the system.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[{"id":85725568,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725568/thumbnails/1.jpg","file_name":"pdf-133288-62131.pdf","download_url":"https://www.academia.edu/attachments/85725568/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Morphological_changes_of_glass_bead_part.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725568/pdf-133288-62131-libre.pdf?1652083217=\u0026response-content-disposition=attachment%3B+filename%3DMorphological_changes_of_glass_bead_part.pdf\u0026Expires=1733935166\u0026Signature=YcDjBm6yzoV0SSUVlJw~-nxeOoyXcbac1iq7NtVYG7KIpXk9jRMcIVoW7Nma~52xZRK82Vy9nBD~eBd6VzptVv0tGnOVfxxF8fC~mCAdNaMzSDUIVB6QerGomIlfuyivGfI4cI2DFm5VXBsiHJp5fGE6zGr8Hl-3nSrTuJG6MAavSb6uj~vUudxlJgXOv2oDxVOqCoGB2lHd~lAmPuyefl~Sa8klg9uwqoHJqLUeCnc~AhBk1toyICtpICDimo--Sdjwt~0Sj~wV6k~~fIYbjJUT5cPJVYFZepN0Tyl7dCHMwuWEe-yNVbGXJkqua3TkMFvy5umAEUjnxJGRGFqYMw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813262"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813262/Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation"><img alt="Research paper thumbnail of Effect of Surface Roughness on Interaction of Particles in Flotation" class="work-thumbnail" src="https://attachments.academia-assets.com/85725513/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813262/Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation">Effect of Surface Roughness on Interaction of Particles in Flotation</a></div><div class="wp-workCard_item"><span>Physicochemical Problems of Mineral Processing</span><span>, 2015</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In this study, the effect of roughness of particles on flotation efficiency along with surface fo...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. The interaction forces between the glass beads changed from repulsion to attraction with the increasing hexadecyltrimethylammonium bromide (HTAB) concentration. ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="c2648191a6d7988a3f15bb466ff992e9" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725513,"asset_id":78813262,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725513/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813262"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813262"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813262; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813262]").text(description); $(".js-view-count[data-work-id=78813262]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813262; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813262']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813262, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "c2648191a6d7988a3f15bb466ff992e9" } } $('.js-work-strip[data-work-id=78813262]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813262,"title":"Effect of Surface Roughness on Interaction of Particles in Flotation","translated_title":"","metadata":{"abstract":"In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. The interaction forces between the glass beads changed from repulsion to attraction with the increasing hexadecyltrimethylammonium bromide (HTAB) concentration. ...","publication_date":{"day":null,"month":null,"year":2015,"errors":{}},"publication_name":"Physicochemical Problems of Mineral Processing"},"translated_abstract":"In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. The interaction forces between the glass beads changed from repulsion to attraction with the increasing hexadecyltrimethylammonium bromide (HTAB) concentration. ...","internal_url":"https://www.academia.edu/78813262/Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation","translated_internal_url":"","created_at":"2022-05-08T23:40:34.352-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":85725513,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/85725513/thumbnails/1.jpg","file_name":"ppmp52-1.18-34.pdf","download_url":"https://www.academia.edu/attachments/85725513/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Effect_of_Surface_Roughness_on_Interacti.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/85725513/ppmp52-1.18-34-libre.pdf?1652083971=\u0026response-content-disposition=attachment%3B+filename%3DEffect_of_Surface_Roughness_on_Interacti.pdf\u0026Expires=1733935166\u0026Signature=MlLQsHYjoIuuHifcRn~6oYjRxwtbK6LVbC95NkfpwdLmWrn8vLACY44ehk2Z172reFkCDNtkHpe2fNJQPQhABNyxGos0h6G15tuvZTcS4zNaeyd6tpwaXJ6iTDHZGns7shiLkSbv9U9-kbjL6hnOXK7SV1pNwzUp8ZGUxz4sKEC4XWsiJ8i9ZG6n0SLBv~riwSx~UbJTg1onSAxH14yngRiYmgQRFi3LEzZ1DpOa7QmAdegz2ZRyo0BN8rJ6GURDOfVX3EyigmcQ~hbDSG48-D0sVH9-wRLyWZp7z~26FQKfzc32Y1sGDeThiiPikHRNd63FtAMfi4D8uhCHdq9nug__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Effect_of_Surface_Roughness_on_Interaction_of_Particles_in_Flotation","translated_slug":"","page_count":17,"language":"en","content_type":"Work","summary":"In this study, the effect of roughness of particles on flotation efficiency along with surface forces among interacting particles was investigated. Glass beads representing smooth spherical particles with a size fraction of -150+90 μm were used. The etching technique was used to produce roughness of different degrees. Microflotation of round+smooth, and its corresponding etched samples were used to evaluate the efficiency of flotation in the case of smooth and rough systems. Atomic Force Microscope (AFM) was used to reveal the interaction forces between the smooth and rough surfaces. According to the results, roughness of particles increased the flotation efficiency. Although the roughness of particles increased with the etching, excess etching time caused a decrease on the roughness and in turn in the flotation recoveries. 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813257"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813257/The_significance_of_positive_and_negative_inertial_forces_in_Particle_Bubble_interaction_and_their_role_in_the_general_flotation_kinetics_model"><img alt="Research paper thumbnail of The significance of positive and negative inertial forces in Particle-Bubble interaction and their role in the general flotation kinetics model" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813257/The_significance_of_positive_and_negative_inertial_forces_in_Particle_Bubble_interaction_and_their_role_in_the_general_flotation_kinetics_model">The significance of positive and negative inertial forces in Particle-Bubble interaction and their role in the general flotation kinetics model</a></div><div class="wp-workCard_item"><span>Minerals Engineering</span><span>, 2021</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bub...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bubble interactions during the flotation process is presented and supported by the experimental data. The effects of positive and negative inertial forces were analyzed by comparing the differences between the models, which either consider or neglect the inertial forces. The Sutherland collision model and the Nguyen attachment model that completely ignore the effect of particle’s inertial forces (inertialess models) were implemented into the general flotation kinetic model. The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. It was shown that the inertial forces should not be omitted in any flotation model amidst concerns over the complexity.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813257"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813257"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813257; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813257]").text(description); $(".js-view-count[data-work-id=78813257]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813257; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813257']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813257, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813257]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813257,"title":"The significance of positive and negative inertial forces in Particle-Bubble interaction and their role in the general flotation kinetics model","translated_title":"","metadata":{"abstract":"Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bubble interactions during the flotation process is presented and supported by the experimental data. The effects of positive and negative inertial forces were analyzed by comparing the differences between the models, which either consider or neglect the inertial forces. The Sutherland collision model and the Nguyen attachment model that completely ignore the effect of particle’s inertial forces (inertialess models) were implemented into the general flotation kinetic model. The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. It was shown that the inertial forces should not be omitted in any flotation model amidst concerns over the complexity.","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2021,"errors":{}},"publication_name":"Minerals Engineering"},"translated_abstract":"Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bubble interactions during the flotation process is presented and supported by the experimental data. The effects of positive and negative inertial forces were analyzed by comparing the differences between the models, which either consider or neglect the inertial forces. The Sutherland collision model and the Nguyen attachment model that completely ignore the effect of particle’s inertial forces (inertialess models) were implemented into the general flotation kinetic model. The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. It was shown that the inertial forces should not be omitted in any flotation model amidst concerns over the complexity.","internal_url":"https://www.academia.edu/78813257/The_significance_of_positive_and_negative_inertial_forces_in_Particle_Bubble_interaction_and_their_role_in_the_general_flotation_kinetics_model","translated_internal_url":"","created_at":"2022-05-08T23:40:33.950-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"The_significance_of_positive_and_negative_inertial_forces_in_Particle_Bubble_interaction_and_their_role_in_the_general_flotation_kinetics_model","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Abstract In this study, a theoretical evaluation of the effect of inertial forces in particle-bubble interactions during the flotation process is presented and supported by the experimental data. The effects of positive and negative inertial forces were analyzed by comparing the differences between the models, which either consider or neglect the inertial forces. The Sutherland collision model and the Nguyen attachment model that completely ignore the effect of particle’s inertial forces (inertialess models) were implemented into the general flotation kinetic model. The modified model was then compared with one of the most accurate inertial models, which considers the Generalized Sutherland Equation (GSE) for collision efficiency along with the Dobby-Finch model for attachment efficiency. The flotation kinetics of chalcopyrite and galena particles were estimated using the general flotation kinetic model in order to demonstrate the effect of particle density on the model, which emphasizes the effect of inertial forces. The influence of positive and negative inertial forces on flotation kinetics was evaluated for various explicit parameters such as particle density, turbulence (energy dissipation), and bubble size and velocity. Obtained theoretical results clearly showed the potential of the particle density to counterbalance the negative effects of the inertial forces. The capability of the positive inertial forces for galena particles (high density) to overcome its negative effect was shown when the general flotation kinetic model was used. Theoretical calculations were further confirmed by experimental bubble loading measurements. It was shown that the inertial forces should not be omitted in any flotation model amidst concerns over the complexity.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":498,"name":"Physics","url":"https://www.academia.edu/Documents/in/Physics"},{"id":512,"name":"Mechanics","url":"https://www.academia.edu/Documents/in/Mechanics"},{"id":20929,"name":"Minerals Engineering","url":"https://www.academia.edu/Documents/in/Minerals_Engineering"},{"id":152114,"name":"Bubble","url":"https://www.academia.edu/Documents/in/Bubble"},{"id":651530,"name":"Froth Flotation","url":"https://www.academia.edu/Documents/in/Froth_Flotation"}],"urls":[{"id":20345474,"url":"https://api.elsevier.com/content/article/PII:S0892687521002351?httpAccept=text/xml"}]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813255"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813255/Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces"><img alt="Research paper thumbnail of Attachment, Coalescence, and Spreading of Carbon Dioxide Nanobubbles at Pyrite Surfaces" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813255/Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces">Attachment, Coalescence, and Spreading of Carbon Dioxide Nanobubbles at Pyrite Surfaces</a></div><div class="wp-workCard_item"><span>Langmuir</span><span>, 2018</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813255"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813255"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813255; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813255]").text(description); $(".js-view-count[data-work-id=78813255]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813255; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813255']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813255, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813255]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813255,"title":"Attachment, Coalescence, and Spreading of Carbon Dioxide Nanobubbles at Pyrite Surfaces","translated_title":"","metadata":{"abstract":"Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.","publisher":"American Chemical Society (ACS)","publication_date":{"day":null,"month":null,"year":2018,"errors":{}},"publication_name":"Langmuir"},"translated_abstract":"Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.","internal_url":"https://www.academia.edu/78813255/Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces","translated_internal_url":"","created_at":"2022-05-08T23:40:32.720-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Attachment_Coalescence_and_Spreading_of_Carbon_Dioxide_Nanobubbles_at_Pyrite_Surfaces","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Recently, it was reported that using CO2 as a flotation gas increases the flotation of auriferous pyrite from high carbonate gold ores of the Carlin Trend. In this regard, the influence of CO2 on bubble attachment at fresh pyrite surfaces was measured in the absence of collector using an induction timer, and it was found that nitrogen bubble attachment time was significantly reduced from 30 ms to less than 10 ms in CO2 saturated solutions. Details of CO2 bubble attachment at a fresh pyrite surface have been examined by atomic force microscopy (AFM) measurements and molecular dynamics (MD) simulations, and the results used to describe the subsequent attachment of a N2 bubble. As found from MD simulations, unlike the attached N2 bubble, which is stable and has a contact angle of about 90°, the CO2 bubble attaches, and spreads, wetting the fresh pyrite surface and forming a multilayer of CO2 molecules, corresponding to a contact angle of almost 180°. These MDS results are complemented by in situ AFM images, which show that, after attachment, CO2 nano-/microbubbles spread to form pancake bubbles at the fresh pyrite surface. In summary, it seems that CO2 bubbles have a propensity to spread, and whether CO2 exists as layers of CO2 molecules (gas pancakes) or as nano-/microbubbles, their presence at the fresh pyrite surface subsequently facilitates film rupture and attachment of millimeter N2 bubbles and, in this way, improves the flotation of pyrite.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":511,"name":"Materials 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$a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813254"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813254/Effect_of_roughness_and_shape_factor_on_flotation_characteristics_of_glass_beads"><img alt="Research paper thumbnail of Effect of roughness and shape factor on flotation characteristics of glass beads" class="work-thumbnail" src="https://attachments.academia-assets.com/85725586/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813254/Effect_of_roughness_and_shape_factor_on_flotation_characteristics_of_glass_beads">Effect of roughness and shape factor on flotation characteristics of glass beads</a></div><div class="wp-workCard_item"><span>Colloids and Surfaces A: Physicochemical and Engineering Aspects</span><span>, 2016</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">h i g h l i g h t s • Both roughness and shape factor stimulate the bubble particle attachment.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="f55c5cf044fb1ddec33cf1ddf0873fc3" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725586,"asset_id":78813254,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725586/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner 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class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813253/Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings"><img alt="Research paper thumbnail of Recovery of Petcock From Lime Calcination Process Tailings" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813253/Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings">Recovery of Petcock From Lime Calcination Process Tailings</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Having access to cheap and sustainable energy source is crucial for mineral processing plants. Th...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Having access to cheap and sustainable energy source is crucial for mineral processing plants. This fact becomes more critical in calcination processes like lime plants. Nowadays, due to its low price and high calorific value Petroleum coke (petcoke) is a quite fair alternative energy source for such plants. Unburned carbon is the main byproduct of lime calcination process which has significant calorific value and can be reused in system. This byproduct is thrown out by heat flux from flue of vertical furnace. This flux has also considerable amounts of lime which is stacked in petcoke layers forming waste mixture in the flue dust. Recently the recovery of this unburned carbon from exhausted gas stacks with flotation and some physical separation methods is conducted. As more reliable way to recover petcoke from waste mixture is found to be flotation process, in this study the effects of feed size, pH, frother and collectors in flotation is investigated and an optimum condition for pr...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813253"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813253"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813253; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813253]").text(description); $(".js-view-count[data-work-id=78813253]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813253; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813253']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813253, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813253]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813253,"title":"Recovery of Petcock From Lime Calcination Process Tailings","translated_title":"","metadata":{"abstract":"Having access to cheap and sustainable energy source is crucial for mineral processing plants. 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Recently the recovery of this unburned carbon from exhausted gas stacks with flotation and some physical separation methods is conducted. As more reliable way to recover petcoke from waste mixture is found to be flotation process, in this study the effects of feed size, pH, frother and collectors in flotation is investigated and an optimum condition for pr...","internal_url":"https://www.academia.edu/78813253/Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings","translated_internal_url":"","created_at":"2022-05-08T23:40:32.448-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Recovery_of_Petcock_From_Lime_Calcination_Process_Tailings","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Having access to cheap and sustainable energy source is crucial for mineral processing plants. 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As more reliable way to recover petcoke from waste mixture is found to be flotation process, in this study the effects of feed size, pH, frother and collectors in flotation is investigated and an optimum condition for pr...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813252"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813252/Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant"><img alt="Research paper thumbnail of Utilization of Colemanite In Exterior Water Borne Paints As A Filler and Fire Retardant" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813252/Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant">Utilization of Colemanite In Exterior Water Borne Paints As A Filler and Fire Retardant</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Paint is mainly used for protection of a substrate; it is applied to prevent the surface from cor...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. Especially in exterior applications, the hydrophobic characteristic of the paints lead to protection against air humidity; moreover, some other properties such as fire retardancy and antibacterial effect of the paints may be required based on its utilization area. Mineral additives in paint constitute anywhere from 20 to 50% of the paint formulation. Due to such high proportion of mineral constituents in the paint system, the required properties of paints can be achieved by properly selecting minerals as fillers. In the present paper, the effect of colemanite, calcium containing boron mineral, has been tested as filler in architectural exterior paints. Paints produced using colemanite were subjected to both wet and dry paint analysis and found that this mineral has favorable effect on opacity and viscosity of the system. Furthermore; colemanite has a remarkable effect on retardin...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813252"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813252"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813252; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813252]").text(description); $(".js-view-count[data-work-id=78813252]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813252; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813252']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813252, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813252]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813252,"title":"Utilization of Colemanite In Exterior Water Borne Paints As A Filler and Fire Retardant","translated_title":"","metadata":{"abstract":"Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. 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Furthermore; colemanite has a remarkable effect on retardin..."},"translated_abstract":"Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. Especially in exterior applications, the hydrophobic characteristic of the paints lead to protection against air humidity; moreover, some other properties such as fire retardancy and antibacterial effect of the paints may be required based on its utilization area. Mineral additives in paint constitute anywhere from 20 to 50% of the paint formulation. Due to such high proportion of mineral constituents in the paint system, the required properties of paints can be achieved by properly selecting minerals as fillers. In the present paper, the effect of colemanite, calcium containing boron mineral, has been tested as filler in architectural exterior paints. Paints produced using colemanite were subjected to both wet and dry paint analysis and found that this mineral has favorable effect on opacity and viscosity of the system. Furthermore; colemanite has a remarkable effect on retardin...","internal_url":"https://www.academia.edu/78813252/Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant","translated_internal_url":"","created_at":"2022-05-08T23:40:32.315-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Utilization_of_Colemanite_In_Exterior_Water_Borne_Paints_As_A_Filler_and_Fire_Retardant","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Paint is mainly used for protection of a substrate; it is applied to prevent the surface from corrosion. Especially in exterior applications, the hydrophobic characteristic of the paints lead to protection against air humidity; moreover, some other properties such as fire retardancy and antibacterial effect of the paints may be required based on its utilization area. Mineral additives in paint constitute anywhere from 20 to 50% of the paint formulation. Due to such high proportion of mineral constituents in the paint system, the required properties of paints can be achieved by properly selecting minerals as fillers. In the present paper, the effect of colemanite, calcium containing boron mineral, has been tested as filler in architectural exterior paints. Paints produced using colemanite were subjected to both wet and dry paint analysis and found that this mineral has favorable effect on opacity and viscosity of the system. Furthermore; colemanite has a remarkable effect on retardin...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813251"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813251/Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints"><img alt="Research paper thumbnail of Interaction Between TiO2 and Calcite-Calcined Kaolin Mixture During Grinding of Pigment in Water Based Paints" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813251/Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints">Interaction Between TiO2 and Calcite-Calcined Kaolin Mixture During Grinding of Pigment in Water Based Paints</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Water based paint formulations consist of some industrial minerals with quantities varying from 2...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813251"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813251"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813251; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813251]").text(description); $(".js-view-count[data-work-id=78813251]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813251; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813251']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813251, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813251]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813251,"title":"Interaction Between TiO2 and Calcite-Calcined Kaolin Mixture During Grinding of Pigment in Water Based Paints","translated_title":"","metadata":{"abstract":"Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c..."},"translated_abstract":"Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c...","internal_url":"https://www.academia.edu/78813251/Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints","translated_internal_url":"","created_at":"2022-05-08T23:40:32.143-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Interaction_Between_TiO2_and_Calcite_Calcined_Kaolin_Mixture_During_Grinding_of_Pigment_in_Water_Based_Paints","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Water based paint formulations consist of some industrial minerals with quantities varying from 20 to 50 %. Quality of paint is directly related to these minerals used as pigment or filler in the production. Titanium dioxide is the most important and expensive pigment in paint formulations. Other minerals such as calcite and calcined kaolin are used as filler and mainly as a substitute for TiO2. Consequently, particle-particle interactions including adsorption, coating and size distribution of pigment mixture directly affects the paint quality. In the present paper, a new type of pigment mixture for possible use in architectural water based paints was developed through grinding. The effect of different types of grinding methods on physical properties of TiO2 and calcite mixture and the quality of paint produced by these mixtures have been revealed. Three different types of mills; conventional ball mill, vibratory ball mill and high speed attritor were used for grinding of TiO2 and c...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813250"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813250/The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites"><img alt="Research paper thumbnail of The Usage of Sodium Bentonite In Styrene Butyl Acrylate Composites" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813250/The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites">The Usage of Sodium Bentonite In Styrene Butyl Acrylate Composites</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In recent years, research on polymer composites with mineral fillers have received great interest...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813250"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813250"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813250; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813250]").text(description); $(".js-view-count[data-work-id=78813250]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813250; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813250']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813250, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813250]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813250,"title":"The Usage of Sodium Bentonite In Styrene Butyl Acrylate Composites","translated_title":"","metadata":{"abstract":"In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix."},"translated_abstract":"In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix.","internal_url":"https://www.academia.edu/78813250/The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites","translated_internal_url":"","created_at":"2022-05-08T23:40:31.984-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"The_Usage_of_Sodium_Bentonite_In_Styrene_Butyl_Acrylate_Composites","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"In recent years, research on polymer composites with mineral fillers have received great interest in terms of improved characteristics on mechanical, rheological and thermal properties. In particular, the usage of layered silicates in composites stems from its distribution characteristics varied upon interlaminar distance within its structure. In this study, the effect of sodium bentonite on mechanical and rheological properties of the composites based on styrene butyl acrylate copolymer which is generally used as binder in different industrial applications depending on its viscosity value. Mechanical properties of the composite such as tensile stress, elongation and elasticity were improved upon addition of sodium bentonite. At the end of the study, optimum amount of sodium bentonite was found considering both mechanical properties and viscosity of the matrix.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813246"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813246/Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints"><img alt="Research paper thumbnail of Substitution of TiO2 With PCC (Precipitated Calcium Carbonate) in Waterborne Paints" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813246/Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints">Substitution of TiO2 With PCC (Precipitated Calcium Carbonate) in Waterborne Paints</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Paints provide protection against any possible corrosion by forming a thin film layer on the mate...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813246"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813246"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813246; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813246]").text(description); $(".js-view-count[data-work-id=78813246]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813246; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813246']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813246, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813246]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813246,"title":"Substitution of TiO2 With PCC (Precipitated Calcium Carbonate) in Waterborne Paints","translated_title":"","metadata":{"abstract":"Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h..."},"translated_abstract":"Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h...","internal_url":"https://www.academia.edu/78813246/Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints","translated_internal_url":"","created_at":"2022-05-08T23:40:31.809-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Substitution_of_TiO2_With_PCC_Precipitated_Calcium_Carbonate_in_Waterborne_Paints","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Paints provide protection against any possible corrosion by forming a thin film layer on the material surface. Paint is a colloidal system consisting of four main parts: binders, pigments or minerals, solvents or water, and additives. Minerals or so-called pigments with a proportion of 20 to 50 % by weight play a fundamental role on paint properties. The variation of these constituents gives rise to a fluctuation in paint type and its quality. In a general architectural paint, titanium dioxide (TiO2) is used as a main white pigment with high refractive index but is quite expensive compared to the rest. Other minerals such as calcite and calcined kaolin are also used as filler or substitute for TiO2. Various researches on these minerals have been carried out in order to reduce TiO2 consumption without affecting the paint quality. In present paper, the behavior of precipitated calcium carbonate (PCC) which differs from ground calcium carbonate (GCC) in terms of morphology and purity h...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813244"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813244/Kolemanit_ve_Bentonit_Katk%C4%B1l%C4%B1_Stiren_B%C3%BCtil_Akrilat_Kopolimeri_%C3%9Cretimi_ve_Karakterizasyonu"><img alt="Research paper thumbnail of Kolemanit ve Bentonit Katkılı Stiren-Bütil Akrilat Kopolimeri Üretimi ve Karakterizasyonu" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813244/Kolemanit_ve_Bentonit_Katk%C4%B1l%C4%B1_Stiren_B%C3%BCtil_Akrilat_Kopolimeri_%C3%9Cretimi_ve_Karakterizasyonu">Kolemanit ve Bentonit Katkılı Stiren-Bütil Akrilat Kopolimeri Üretimi ve Karakterizasyonu</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813244"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813244"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813244; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813244]").text(description); $(".js-view-count[data-work-id=78813244]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813244; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813244']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813244, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813244]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813244,"title":"Kolemanit ve Bentonit Katkılı Stiren-Bütil Akrilat Kopolimeri Üretimi ve Karakterizasyonu","translated_title":"","metadata":{"abstract":"Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo..."},"translated_abstract":"Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo...","internal_url":"https://www.academia.edu/78813244/Kolemanit_ve_Bentonit_Katk%C4%B1l%C4%B1_Stiren_B%C3%BCtil_Akrilat_Kopolimeri_%C3%9Cretimi_ve_Karakterizasyonu","translated_internal_url":"","created_at":"2022-05-08T23:40:31.664-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Kolemanit_ve_Bentonit_Katkılı_Stiren_Bütil_Akrilat_Kopolimeri_Üretimi_ve_Karakterizasyonu","translated_slug":"","page_count":null,"language":"tr","content_type":"Work","summary":"Kompozit malzemeler, matrislerinde mikron boyutlarında katı partiküller içeren, heterojen karışım gösteren malzemelerdir. İnorganik dolgu ve çeşitli polimer matrikslerinden imal edilen kompozitler giderek artan oranda endüstriyel uygulamalarda yer almaktadır. Bu ilginin artmasının nedeni bu malzemelerin dolgu olarak katıldıkları sistemlere viskozite ayarlayıcı, akış düzenleyici, yüksek mekanik dayanım, alev geciktirici, termal dayanım gibi özellikleri kazandırmasının yanı sıra maliyeti önemli oranlarda düşürmeleridir. Son zamanlarda bu tip sistemlerin hazırlanması hakkında çeşitli araştırmalar yapılmaktadır. Bu çalışmada dış cephe boyalarında bağlayıcı olarak kullanılan stiren-bütil akrilat kopolimeri matris, tabakalı bir silikat olan smektit türü kil grubuna ait ve su ile şişme kapasitesi nispeten düşük olan kalsiyum bentonit ve yüksek kalsiyum oranına sahip bir bor minerali olan kolemanit cevheri katkı maddeleri olarak seçilmiştir.Kompozit malzeme üretimi stiren-bütil akrilat kopo...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813242"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813242/Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings"><img alt="Research paper thumbnail of Flotation kinetics for Recovery of Petcoke from Lime Calcination Plant Tailings" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813242/Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings">Flotation kinetics for Recovery of Petcoke from Lime Calcination Plant Tailings</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Flotation models are very useful for quantifying the practical work and also to assist in the des...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813242"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813242"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813242; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813242]").text(description); $(".js-view-count[data-work-id=78813242]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813242; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813242']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813242, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813242]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813242,"title":"Flotation kinetics for Recovery of Petcoke from Lime Calcination Plant Tailings","translated_title":"","metadata":{"abstract":"Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution."},"translated_abstract":"Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution.","internal_url":"https://www.academia.edu/78813242/Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings","translated_internal_url":"","created_at":"2022-05-08T23:40:31.534-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Flotation_kinetics_for_Recovery_of_Petcoke_from_Lime_Calcination_Plant_Tailings","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Flotation models are very useful for quantifying the practical work and also to assist in the design of new equipment and process. The analyses of ash content and calorific value of the petroleum coke in lime calcinations tailings were used to detect its floatability and product quality. The flotation rate constants “k” values of the four traditional kinetics models parameters were calculated by software MATLAB 2013. The k value reflects the floatability and in view of different parameters, in proportion to the decrease on k parameter, the flotation process worsens. As a result, an optimum dosage for both collector and frother was found considering maximum recovery value as well as minimum ash content, and highest calorific values of products. A statistical analysis of data showed that the flotation rate constant values give excellent fit to the Classical First-Order Model distribution.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813241"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813241/Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering"><img alt="Research paper thumbnail of Effect of hydrophilic lipophilic balance (HLB) of nonionic surfactants on ultrafine lignite dewatering" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813241/Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering">Effect of hydrophilic lipophilic balance (HLB) of nonionic surfactants on ultrafine lignite dewatering</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Since dewatering is a costly process, removal of moisture from relatively fine size lignites is a...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813241"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813241"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813241; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813241]").text(description); $(".js-view-count[data-work-id=78813241]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813241; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813241']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813241, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813241]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813241,"title":"Effect of hydrophilic lipophilic balance (HLB) of nonionic surfactants on ultrafine lignite dewatering","translated_title":"","metadata":{"abstract":"Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom..."},"translated_abstract":"Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom...","internal_url":"https://www.academia.edu/78813241/Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering","translated_internal_url":"","created_at":"2022-05-08T23:40:31.380-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Effect_of_hydrophilic_lipophilic_balance_HLB_of_nonionic_surfactants_on_ultrafine_lignite_dewatering","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Since dewatering is a costly process, removal of moisture from relatively fine size lignites is an important industrial problem. As the lignite gets finer, the presence of micropores and relatively low hydrophobic nature of lignite lead to trapping of large quantities of water in the coal matrix. Lignites used in power stations need to be dried to a certain degree of humidity before it is transferred to the combustion chamber. It is generally wise to dewater coal as much as possible by physical means before it is dried. However, dewatering cost in some cases may be prohibitive. Thus, sometimes removal of even little percent moisture may be of great help in such operations. Surfactants have been used to increase the efficiency of coal dewatering. It is crucial to select appropriate type and amount of surfactants in order to get higher efficiency. Since the hydrophobic characteristic of coals increases with increasing the coal rank, dewatering of bituminous and anthracite can be accom...","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813240"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" rel="nofollow" href="https://www.academia.edu/78813240/Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints"><img alt="Research paper thumbnail of Calcined Kaolin and Calcite as a Pigment and Substitute for TiO2 in Water Based Paints" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" rel="nofollow" href="https://www.academia.edu/78813240/Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints">Calcined Kaolin and Calcite as a Pigment and Substitute for TiO2 in Water Based Paints</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particul...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813240"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813240"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813240; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813240]").text(description); $(".js-view-count[data-work-id=78813240]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813240; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813240']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813240, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813240]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813240,"title":"Calcined Kaolin and Calcite as a Pigment and Substitute for TiO2 in Water Based Paints","translated_title":"","metadata":{"abstract":"Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality."},"translated_abstract":"Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality.","internal_url":"https://www.academia.edu/78813240/Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints","translated_internal_url":"","created_at":"2022-05-08T23:40:31.258-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Calcined_Kaolin_and_Calcite_as_a_Pigment_and_Substitute_for_TiO2_in_Water_Based_Paints","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"Mineral additives in paint constitute anywhere from 20 to 50 % of the paint formulation. Particularly, water based paint formulations utilize maximum quantities of mineral additives particularly those titanium dioxide (rutile and anatase), calcite, mica, clay minerals (thickeners), quartz, feldspar, barite and pigments. In the present paper, the effect of calcined kaolin and calcite as an extender and substitute for TiO2, one of the most expensive pigments in paint formulations, has been revealed. The quality of paint was compared with the properties based on both wet and dry paints such as viscosity, density, opacity, gloss and fineness of fillers and pigments. The paint recipe prepared with calcined kaolin and calcite showed improved in physical properties especially because the mineral particles effectively filled the gaps among TiO2 particles and kept them apart via physical interactions. Overall, a new paint formulation has been developed with low cost and good quality.","owner":{"id":1308754,"first_name":"Behzad","middle_initials":null,"last_name":"Vaziri Hassas","page_name":"BehzadVaziriHassas","domain_name":"pennstate","created_at":"2012-03-16T05:53:50.316-07:00","display_name":"Behzad Vaziri Hassas","url":"https://pennstate.academia.edu/BehzadVaziriHassas"},"attachments":[],"research_interests":[],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="78813239"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/78813239/Effect_of_precipitated_calcium_carbonate_additions_on_waterborne_paints_at_different_pigment_volume_concentrations"><img alt="Research paper thumbnail of Effect of precipitated calcium carbonate additions on waterborne paints at different pigment volume concentrations" class="work-thumbnail" src="https://attachments.academia-assets.com/85725573/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/78813239/Effect_of_precipitated_calcium_carbonate_additions_on_waterborne_paints_at_different_pigment_volume_concentrations">Effect of precipitated calcium carbonate additions on waterborne paints at different pigment volume concentrations</a></div><div class="wp-workCard_item"><span>Progress in Organic Coatings</span><span>, 2015</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Titanium dioxide (TiO 2) due to its high refractive index, is widely used in paint industry as a ...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">Titanium dioxide (TiO 2) due to its high refractive index, is widely used in paint industry as a white pigment. In order to reduce this high cost of TiO 2 , a part of TiO 2 is generally substituted by some other industrial mineral fillers such as calcite and calcined kaolin; however, this substitution affects the quality of paints in terms of stability, coverage (opacity), brightness (gloss), scrub resistance (film toughness), etc. In the present paper, precipitated calcium carbonate (PCC) was substituted for TiO 2 in paint mixture at three different pigment volume concentrations (PVC). It was observed that substitution of TiO 2 by PCC depends on PVC value at which there is an optimum PCC amount. The quality of paints produced by PCC along with its rheological properties was evaluated based on standard features in both wet and dry paints such as viscosity, density, opacity and gloss values. Addition of PCC increases the opacity to a certain point. Similarly, scrub resistance and viscosity increases with the addition of PCC at all PVCs, however, viscosity is not as much critical for the paint production. On the other hand, there is no any systematic effect of PCC on gloss value of the paint. This study overall demonstrates that PCC can be successfully used to substitute TiO 2 only with a careful adjustment of PVC and other extenders used in the paint formulation.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="e022fe2a04d990df6583580363663bbc" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":85725573,"asset_id":78813239,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/85725573/download_file?st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&st=MTczMzkzMTU2Niw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813239"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813239"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813239; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813239]").text(description); $(".js-view-count[data-work-id=78813239]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813239; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813239']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813239, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "e022fe2a04d990df6583580363663bbc" } } $('.js-work-strip[data-work-id=78813239]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813239,"title":"Effect of precipitated calcium carbonate additions on waterborne paints at different pigment volume concentrations","translated_title":"","metadata":{"publisher":"Elsevier BV","grobid_abstract":"Titanium dioxide (TiO 2) due to its high refractive index, is widely used in paint industry as a white pigment. In order to reduce this high cost of TiO 2 , a part of TiO 2 is generally substituted by some other industrial mineral fillers such as calcite and calcined kaolin; however, this substitution affects the quality of paints in terms of stability, coverage (opacity), brightness (gloss), scrub resistance (film toughness), etc. In the present paper, precipitated calcium carbonate (PCC) was substituted for TiO 2 in paint mixture at three different pigment volume concentrations (PVC). It was observed that substitution of TiO 2 by PCC depends on PVC value at which there is an optimum PCC amount. The quality of paints produced by PCC along with its rheological properties was evaluated based on standard features in both wet and dry paints such as viscosity, density, opacity and gloss values. Addition of PCC increases the opacity to a certain point. Similarly, scrub resistance and viscosity increases with the addition of PCC at all PVCs, however, viscosity is not as much critical for the paint production. On the other hand, there is no any systematic effect of PCC on gloss value of the paint. 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In order to reduce this high cost of TiO 2 , a part of TiO 2 is generally substituted by some other industrial mineral fillers such as calcite and calcined kaolin; however, this substitution affects the quality of paints in terms of stability, coverage (opacity), brightness (gloss), scrub resistance (film toughness), etc. In the present paper, precipitated calcium carbonate (PCC) was substituted for TiO 2 in paint mixture at three different pigment volume concentrations (PVC). It was observed that substitution of TiO 2 by PCC depends on PVC value at which there is an optimum PCC amount. The quality of paints produced by PCC along with its rheological properties was evaluated based on standard features in both wet and dry paints such as viscosity, density, opacity and gloss values. Addition of PCC increases the opacity to a certain point. 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This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. The governing mechanisms are discussed in the light of hydrophilicity index and modification of physicochemical conditions.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="78813237"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="78813237"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 78813237; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=78813237]").text(description); $(".js-view-count[data-work-id=78813237]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 78813237; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='78813237']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 78813237, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=78813237]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":78813237,"title":"Ultrafine coal dewatering: Relationship between hydrophilic lipophilic balance (HLB) of surfactants and coal rank","translated_title":"","metadata":{"abstract":"ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washing plants. This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. The governing mechanisms are discussed in the light of hydrophilicity index and modification of physicochemical conditions.","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2014,"errors":{}},"publication_name":"International Journal of Mineral Processing"},"translated_abstract":"ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washing plants. This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. The governing mechanisms are discussed in the light of hydrophilicity index and modification of physicochemical conditions.","internal_url":"https://www.academia.edu/78813237/Ultrafine_coal_dewatering_Relationship_between_hydrophilic_lipophilic_balance_HLB_of_surfactants_and_coal_rank","translated_internal_url":"","created_at":"2022-05-08T23:40:30.941-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":1308754,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Ultrafine_coal_dewatering_Relationship_between_hydrophilic_lipophilic_balance_HLB_of_surfactants_and_coal_rank","translated_slug":"","page_count":null,"language":"en","content_type":"Work","summary":"ABSTRACT Dewatering process is one of the most costly steps in mineral processing and coal washing plants. This fact becomes an important industrial challenge in lignite cleaning. The presence of micropores and relatively low hydrophobic nature of lignitic coal lead to trapping of large quantities of water in the coal matrix especially in fine sizes. Since lignites are used as a common fuel in power stations, they need to be dried to a certain moisture level before feeding to the combustion chamber. Dump feeding in power plants cause inevitable loss of efficiency and may be deleterious for combustion sections. It is thus generally wise to dewater coal as much as possible by physical means before it is dried. However, further dewatering cost in some cases may be prohibitive particularly for fine and hydrophilic particles. In this study, various type and amount of surfactants have been tested to increase the efficiency of coal dewatering. As the hydrophobic characteristic of coals varies and increases with increasing the coal rank, dewatering of bituminous and anthracite type coals can be accomplished using low HLB surfactants (Oily), however, these surfactants are not efficient in the case of low rank coals like lignites and brown coals. A special set-up has been designed to study the effect of high HLB surfactants on dewatering of ultrafine lignite particles. It is shown that, while surfactants with lower HLB number and oily characteristics are the most convenient dewatering reagents for slightly hydrophobic surfaces such as hard coals, surfactants with higher HLB values especially those with HLB of around 10 are the most efficient reagents for dewatering of ultrafine lignite and lower rank coals. 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