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Size","url":"https://www.academia.edu/Documents/in/Particle_Size?f_ri=741421"},{"id":741421,"name":"Adsorption Isotherm Models","url":"https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models?f_ri=741421"},{"id":793888,"name":"Reactive Dyes","url":"https://www.academia.edu/Documents/in/Reactive_Dyes?f_ri=741421"},{"id":835697,"name":"Lumping Kinetic Model","url":"https://www.academia.edu/Documents/in/Lumping_Kinetic_Model?f_ri=741421"},{"id":989646,"name":"Aqueous Solution","url":"https://www.academia.edu/Documents/in/Aqueous_Solution?f_ri=741421"},{"id":1004968,"name":"Semiconducting Aluminum Compounds","url":"https://www.academia.edu/Documents/in/Semiconducting_Aluminum_Compounds?f_ri=741421"},{"id":1120502,"name":"Experimental Data","url":"https://www.academia.edu/Documents/in/Experimental_Data?f_ri=741421"},{"id":1137254,"name":"Hydrogen-Ion Concentration","url":"https://www.academia.edu/Documents/in/Hydrogen-Ion_Concentration?f_ri=741421"},{"id":1436040,"name":"Potassium Compounds","url":"https://www.academia.edu/Documents/in/Potassium_Compounds?f_ri=741421"},{"id":1453161,"name":"Langmuir Isotherm","url":"https://www.academia.edu/Documents/in/Langmuir_Isotherm?f_ri=741421"},{"id":1663770,"name":"Sulfates","url":"https://www.academia.edu/Documents/in/Sulfates?f_ri=741421"}]}, }) } })();</script></ul></li></ul></div></div><div class="u-borderBottom1 u-borderColorGrayLighter"><div class="clearfix u-pv7x u-mb0x js-work-card work_3345300" data-work_id="3345300" itemscope="itemscope" itemtype="https://schema.org/ScholarlyArticle"><div class="header"><div class="title u-fontSerif u-fs22 u-lineHeight1_3"><a class="u-tcGrayDarkest js-work-link" href="https://www.academia.edu/3345300/Removal_of_fluoride_from_aqueous_solution_by_using_red_mud">Removal of fluoride from aqueous solution by using red mud</a></div></div><div class="u-pb4x u-mt3x"><div class="summary u-fs14 u-fw300 u-lineHeight1_5 u-tcGrayDarkest"><div class="summarized">The removal of fluoride from aqueous solution by using the original and activated red mud forms was studied in batch equilibration technique. Influence of pH, adsorbent dose and contact time on the adsorption were investigated. The... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_3345300" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">The removal of fluoride from aqueous solution by using the original and activated red mud forms was studied in batch equilibration technique. Influence of pH, adsorbent dose and contact time on the adsorption were investigated. The fluoride adsorption capacity of activated form was found to be higher than that of the original form. The maximum removal of fluoride ion was obtained at pH 5.5. The removal of fluoride was expressed with Langmuir and Freundlich isotherms. Langmuir adsorption isotherm curve was found to be significant. It was found that the sufficient time for adsorption equilibrium of fluoride ions is 2 h. The possibility of removal of fluoride ion by using red mud is explained on the basis of the chemical nature and specific interaction with metal oxide surfaces and the results are interpreted in terms of pH variations.</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/3345300" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="8f65a3df191220d027454a1ff74e82fb" rel="nofollow" data-download="{"attachment_id":50323222,"asset_id":3345300,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/50323222/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="2835745" href="https://selcuk.academia.edu/MErsoz">Mustafa Ersoz</a><script data-card-contents-for-user="2835745" type="text/json">{"id":2835745,"first_name":"Mustafa","last_name":"Ersoz","domain_name":"selcuk","page_name":"MErsoz","display_name":"Mustafa Ersoz","profile_url":"https://selcuk.academia.edu/MErsoz?f_ri=741421","photo":"https://0.academia-photos.com/2835745/929310/1163696/s65_mustafa.ersoz.jpg"}</script></span></span></li><li class="js-paper-rank-work_3345300 InlineList-item InlineList-item--bordered hidden"><span class="js-paper-rank-view hidden u-tcGrayDark" data-paper-rank-work-id="3345300"><i class="u-m1x fa fa-bar-chart"></i><strong class="js-paper-rank"></strong></span><script>$(function() { new Works.PaperRankView({ workId: 3345300, container: ".js-paper-rank-work_3345300", }); 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$(".js-view-count[data-work-id=3345300]").text(description); $(".js-view-count-work_3345300").attr('title', description).tooltip(); }); });</script></span><script>$(function() { $(".js-view-count-work_3345300").removeClass('hidden') })</script></div></li><li class="InlineList-item u-positionRelative" style="max-width: 250px"><div class="u-positionAbsolute" data-has-card-for-ri-list="3345300"><i class="fa fa-tag InlineList-item-icon u-positionRelative"></i> <a class="InlineList-item-text u-positionRelative">6</a> </div><span class="InlineList-item-text u-textTruncate u-pl9x"><a class="InlineList-item-text" data-has-card-for-ri="72" href="https://www.academia.edu/Documents/in/Chemical_Engineering">Chemical Engineering</a>, <script data-card-contents-for-ri="72" type="text/json">{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering?f_ri=741421","nofollow":false}</script><a class="InlineList-item-text" data-has-card-for-ri="524" href="https://www.academia.edu/Documents/in/Analytical_Chemistry">Analytical Chemistry</a>, <script data-card-contents-for-ri="524" type="text/json">{"id":524,"name":"Analytical Chemistry","url":"https://www.academia.edu/Documents/in/Analytical_Chemistry?f_ri=741421","nofollow":false}</script><a class="InlineList-item-text" data-has-card-for-ri="378291" href="https://www.academia.edu/Documents/in/Red_Mud">Red Mud</a>, <script data-card-contents-for-ri="378291" type="text/json">{"id":378291,"name":"Red Mud","url":"https://www.academia.edu/Documents/in/Red_Mud?f_ri=741421","nofollow":false}</script><a class="InlineList-item-text" data-has-card-for-ri="741421" href="https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models">Adsorption Isotherm Models</a><script data-card-contents-for-ri="741421" type="text/json">{"id":741421,"name":"Adsorption Isotherm Models","url":"https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models?f_ri=741421","nofollow":false}</script></span></li><script>(function(){ if (true) { new Aedu.ResearchInterestListCard({ el: $('*[data-has-card-for-ri-list=3345300]'), work: {"id":3345300,"title":"Removal of fluoride from aqueous solution by using red mud","created_at":"2013-04-20T19:09:09.481-07:00","url":"https://www.academia.edu/3345300/Removal_of_fluoride_from_aqueous_solution_by_using_red_mud?f_ri=741421","dom_id":"work_3345300","summary":"The removal of fluoride from aqueous solution by using the original and activated red mud forms was studied in batch equilibration technique. Influence of pH, adsorbent dose and contact time on the adsorption were investigated. The fluoride adsorption capacity of activated form was found to be higher than that of the original form. The maximum removal of fluoride ion was obtained at pH 5.5. The removal of fluoride was expressed with Langmuir and Freundlich isotherms. Langmuir adsorption isotherm curve was found to be significant. It was found that the sufficient time for adsorption equilibrium of fluoride ions is 2 h. The possibility of removal of fluoride ion by using red mud is explained on the basis of the chemical nature and specific interaction with metal oxide surfaces and the results are interpreted in terms of pH variations.","downloadable_attachments":[{"id":50323222,"asset_id":3345300,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":2835745,"first_name":"Mustafa","last_name":"Ersoz","domain_name":"selcuk","page_name":"MErsoz","display_name":"Mustafa Ersoz","profile_url":"https://selcuk.academia.edu/MErsoz?f_ri=741421","photo":"https://0.academia-photos.com/2835745/929310/1163696/s65_mustafa.ersoz.jpg"}],"research_interests":[{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering?f_ri=741421","nofollow":false},{"id":524,"name":"Analytical Chemistry","url":"https://www.academia.edu/Documents/in/Analytical_Chemistry?f_ri=741421","nofollow":false},{"id":378291,"name":"Red 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Chatterjee","profile_url":"https://independent.academia.edu/SudiptaChatterjee1?f_ri=741421","photo":"/images/s65_no_pic.png"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering?f_ri=741421","nofollow":false},{"id":522,"name":"Thermodynamics","url":"https://www.academia.edu/Documents/in/Thermodynamics?f_ri=741421","nofollow":false},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling?f_ri=741421","nofollow":false},{"id":6515,"name":"Water Purification","url":"https://www.academia.edu/Documents/in/Water_Purification?f_ri=741421","nofollow":false},{"id":9130,"name":"Chitosan","url":"https://www.academia.edu/Documents/in/Chitosan?f_ri=741421"},{"id":11432,"name":"Collagen Cross-linking","url":"https://www.academia.edu/Documents/in/Collagen_Cross-linking?f_ri=741421"},{"id":39752,"name":"Adsorption","url":"https://www.academia.edu/Documents/in/Adsorption?f_ri=741421"},{"id":84278,"name":"Ph","url":"https://www.academia.edu/Documents/in/Ph?f_ri=741421"},{"id":122402,"name":"Nitrates","url":"https://www.academia.edu/Documents/in/Nitrates?f_ri=741421"},{"id":149625,"name":"Hazardous Materials","url":"https://www.academia.edu/Documents/in/Hazardous_Materials?f_ri=741421"},{"id":410194,"name":"Waste Treatment","url":"https://www.academia.edu/Documents/in/Waste_Treatment?f_ri=741421"},{"id":474134,"name":"Conditioning","url":"https://www.academia.edu/Documents/in/Conditioning?f_ri=741421"},{"id":584724,"name":"Electrostatic force","url":"https://www.academia.edu/Documents/in/Electrostatic_force?f_ri=741421"},{"id":741421,"name":"Adsorption Isotherm 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u-tcGrayDarkest"><div class="summarized">The water-binding properties of wheat starch films were studied through the determination of water vapour adsorption isotherms at 20°C. Starch films were obtained by casting after mixing native starch at 95°C for 15min with different... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_13972343" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">The water-binding properties of wheat starch films were studied through the determination of water vapour adsorption isotherms at 20°C. Starch films were obtained by casting after mixing native starch at 95°C for 15min with different ratios of plasticizer (glycerol).Unplasticized starch film was found to adsorb less water than native starch granules. The effect of glycerol on water vapour adsorption by</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/13972343" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="f25202af3a910a8a78ce21356d5ee989" rel="nofollow" data-download="{"attachment_id":44749203,"asset_id":13972343,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/44749203/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="38752309" href="https://independent.academia.edu/PatriceDole">Patrice Dole</a><script data-card-contents-for-user="38752309" type="text/json">{"id":38752309,"first_name":"Patrice","last_name":"Dole","domain_name":"independent","page_name":"PatriceDole","display_name":"Patrice Dole","profile_url":"https://independent.academia.edu/PatriceDole?f_ri=741421","photo":"/images/s65_no_pic.png"}</script></span></span><span class="u-displayInlineBlock InlineList-item-text"> and <span class="u-textDecorationUnderline u-clickable InlineList-item-text js-work-more-authors-13972343">+1</span><div class="hidden js-additional-users-13972343"><div><span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a href="https://independent.academia.edu/CatherineJoly">Catherine Joly</a></span></div></div></span><script>(function(){ var popoverSettings = { el: $('.js-work-more-authors-13972343'), placement: 'bottom', hide_delay: 200, html: true, content: function(){ return $('.js-additional-users-13972343').html(); 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Starch films were obtained by casting after mixing native starch at 95°C for 15min with different ratios of plasticizer (glycerol).Unplasticized starch film was found to adsorb less water than native starch granules. The effect of glycerol on water vapour adsorption by","downloadable_attachments":[{"id":44749203,"asset_id":13972343,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":38752309,"first_name":"Patrice","last_name":"Dole","domain_name":"independent","page_name":"PatriceDole","display_name":"Patrice Dole","profile_url":"https://independent.academia.edu/PatriceDole?f_ri=741421","photo":"/images/s65_no_pic.png"},{"id":33020003,"first_name":"Catherine","last_name":"Joly","domain_name":"independent","page_name":"CatherineJoly","display_name":"Catherine Joly","profile_url":"https://independent.academia.edu/CatherineJoly?f_ri=741421","photo":"/images/s65_no_pic.png"}],"research_interests":[{"id":16137,"name":"Food Chemistry","url":"https://www.academia.edu/Documents/in/Food_Chemistry?f_ri=741421","nofollow":false},{"id":28235,"name":"Multidisciplinary","url":"https://www.academia.edu/Documents/in/Multidisciplinary?f_ri=741421","nofollow":false},{"id":230744,"name":"Relative Humidity","url":"https://www.academia.edu/Documents/in/Relative_Humidity?f_ri=741421","nofollow":false},{"id":415784,"name":"Phase Separation","url":"https://www.academia.edu/Documents/in/Phase_Separation?f_ri=741421","nofollow":false},{"id":500343,"name":"Water vapour","url":"https://www.academia.edu/Documents/in/Water_vapour?f_ri=741421"},{"id":741421,"name":"Adsorption Isotherm Models","url":"https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models?f_ri=741421"},{"id":1458758,"name":"Molecular Interactions","url":"https://www.academia.edu/Documents/in/Molecular_Interactions?f_ri=741421"}]}, }) } })();</script></ul></li></ul></div></div><div class="u-borderBottom1 u-borderColorGrayLighter"><div class="clearfix u-pv7x u-mb0x js-work-card work_45312227" data-work_id="45312227" itemscope="itemscope" itemtype="https://schema.org/ScholarlyArticle"><div class="header"><div class="title u-fontSerif u-fs22 u-lineHeight1_3"><a class="u-tcGrayDarkest js-work-link" href="https://www.academia.edu/45312227/CI_7_2_">CI 7(2)</a></div></div><div class="u-pb4x u-mt3x"><div class="summary u-fs14 u-fw300 u-lineHeight1_5 u-tcGrayDarkest"><div class="summarized">Adsorption of crystal violet dye from aqueous solutions applying olive leaves powder (OLP) as a biosorbent has been examined under various experimental circumstances. The influence of contact time, pH, initial concentration of studied dye... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_45312227" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">Adsorption of crystal violet dye from aqueous solutions applying olive leaves powder (OLP) as a biosorbent has been examined under various experimental circumstances. The influence of contact time, pH, initial concentration of studied dye and adsorbent dose on the adsorption process has been investigated applying batch experiments. The concentration of remaining dye has been determined using molecular absorption spectrometry at wave length of 580 nm. The maximum removal of studied dye has been realized at pH 7.5 with a percent removal of 99.2% after 20 min of agitation time. Langmuir, Freundlich,and Temkin isotherm models exemplify the best fit for the experimental data; while the elevated adsorption capacity was 181.1 mg.g1. Adsorption kinetics of crystal violet was expected sufficiently with the empirical pseudo-second-order model. Corresponding to the adsorption capacity, olive leaves powder thought as a low cost, effective, and environmentally friendly biosorbent for the removal of crystal violet dye from aqueous solutions.</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/45312227" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="f007dee0a37ed1f3e469f2887f83581d" rel="nofollow" data-download="{"attachment_id":65859920,"asset_id":45312227,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/65859920/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="9584721" href="https://benghazi.academia.edu/KhaledElsherif">Khaled Elsherif</a><script data-card-contents-for-user="9584721" type="text/json">{"id":9584721,"first_name":"Khaled","last_name":"Elsherif","domain_name":"benghazi","page_name":"KhaledElsherif","display_name":"Khaled Elsherif","profile_url":"https://benghazi.academia.edu/KhaledElsherif?f_ri=741421","photo":"https://0.academia-photos.com/9584721/3028376/5672406/s65_khaled.elsherif.jpg"}</script></span></span></li><li class="js-paper-rank-work_45312227 InlineList-item InlineList-item--bordered hidden"><span class="js-paper-rank-view hidden u-tcGrayDark" data-paper-rank-work-id="45312227"><i class="u-m1x fa fa-bar-chart"></i><strong class="js-paper-rank"></strong></span><script>$(function() { new Works.PaperRankView({ workId: 45312227, container: ".js-paper-rank-work_45312227", }); 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The influence of contact time, pH, initial concentration of studied dye and adsorbent dose on the adsorption process has been investigated applying batch experiments. The concentration of remaining dye has been determined using molecular absorption spectrometry at wave length of 580 nm. The maximum removal of studied dye has been realized at pH 7.5 with a percent removal of 99.2% after 20 min of agitation time. Langmuir, Freundlich,and Temkin isotherm models exemplify the best fit for the experimental data; while the elevated adsorption capacity was 181.1 mg.g1. Adsorption kinetics of crystal violet was expected sufficiently with the empirical pseudo-second-order model. Corresponding to the adsorption capacity, olive leaves powder thought as a low cost, effective, and environmentally friendly biosorbent for the removal of crystal violet dye from aqueous solutions.","downloadable_attachments":[{"id":65859920,"asset_id":45312227,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":9584721,"first_name":"Khaled","last_name":"Elsherif","domain_name":"benghazi","page_name":"KhaledElsherif","display_name":"Khaled Elsherif","profile_url":"https://benghazi.academia.edu/KhaledElsherif?f_ri=741421","photo":"https://0.academia-photos.com/9584721/3028376/5672406/s65_khaled.elsherif.jpg"}],"research_interests":[{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics?f_ri=741421","nofollow":false},{"id":113095,"name":"Adsorption and wastewater treatment","url":"https://www.academia.edu/Documents/in/Adsorption_and_wastewater_treatment?f_ri=741421","nofollow":false},{"id":288313,"name":"Biosorption of water pollutants 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spinning drop method. The results qualitatively and quantitatively agreed with... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_9993853" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">The adsorption isotherms between aqueous solutions of sodium dodecylsulphate and gelatin against air, toluene, or diethylphthalate were determined using the spinning drop method. The results qualitatively and quantitatively agreed with those found by surface tension measurements on sodium dodecylsulphate/gelatin solutions using the ring method in the version of Du Noüy. Interaction between gelatin and the surfactant will yield complexes which are more interfacially active than the components by themselves. 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and kinetics</a></div></div><div class="u-pb4x u-mt3x"><div class="summary u-fs14 u-fw300 u-lineHeight1_5 u-tcGrayDarkest"><div class="summarized">Physico-chemical investigation on adsorption of congo red, an anionic azo dye by chitosan hydrobeads has been carried out. Adsorption process has been found to be dependant on temperature with optimum activity at 30 °C. Both ionic... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_3890948" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">Physico-chemical investigation on adsorption of congo red, an anionic azo dye by chitosan hydrobeads has been carried out. Adsorption process has been found to be dependant on temperature with optimum activity at 30 °C. Both ionic interaction as well as physical forces is responsible for binding of congo red with chitosan. Theoretical correlation of the experimental equilibrium adsorption data for congo red–chitosan hydrobeads system would be best explained by linearized form of Langmuir isotherm model. The kinetic results follow pseudo second-order rate equation. pH of the experimental solution influenced congo red adsorption inversely, and ∼20.0% of the dye could be desorbed from the loaded beads by changing the pH of the solution to alkaline range (∼pH 12.0). Both sodium chloride and sodium dodecyl sulfate significantly influenced the adsorption process.</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/3890948" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="07d140c3ff1b471f804b77cf0c1f14c0" rel="nofollow" data-download="{"attachment_id":50106301,"asset_id":3890948,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/50106301/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="4774690" href="https://clri.academia.edu/SandipanChatterjee">Sandipan Chatterjee</a><script data-card-contents-for-user="4774690" type="text/json">{"id":4774690,"first_name":"Sandipan","last_name":"Chatterjee","domain_name":"clri","page_name":"SandipanChatterjee","display_name":"Sandipan Chatterjee","profile_url":"https://clri.academia.edu/SandipanChatterjee?f_ri=741421","photo":"https://0.academia-photos.com/4774690/2029733/2392629/s65_sandipan.chatterjee.jpg"}</script></span></span></li><li class="js-paper-rank-work_3890948 InlineList-item InlineList-item--bordered hidden"><span class="js-paper-rank-view hidden u-tcGrayDark" data-paper-rank-work-id="3890948"><i class="u-m1x fa fa-bar-chart"></i><strong class="js-paper-rank"></strong></span><script>$(function() { new Works.PaperRankView({ workId: 3890948, container: ".js-paper-rank-work_3890948", }); 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Adsorption process has been found to be dependant on temperature with optimum activity at 30 °C. Both ionic interaction as well as physical forces is responsible for binding of congo red with chitosan. Theoretical correlation of the experimental equilibrium adsorption data for congo red–chitosan hydrobeads system would be best explained by linearized form of Langmuir isotherm model. The kinetic results follow pseudo second-order rate equation. pH of the experimental solution influenced congo red adsorption inversely, and ∼20.0% of the dye could be desorbed from the loaded beads by changing the pH of the solution to alkaline range (∼pH 12.0). 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})();</script></ul></li></ul></div></div><div class="u-borderBottom1 u-borderColorGrayLighter"><div class="clearfix u-pv7x u-mb0x js-work-card work_5480415" data-work_id="5480415" itemscope="itemscope" itemtype="https://schema.org/ScholarlyArticle"><div class="header"><div class="title u-fontSerif u-fs22 u-lineHeight1_3"><a class="u-tcGrayDarkest js-work-link" href="https://www.academia.edu/5480415/A_Study_of_Adsorption_of_Water_Vapour_on_Wool_under_Static_and_Dynamic_Conditions">A Study of Adsorption of Water Vapour on Wool under Static and Dynamic Conditions</a></div></div><div class="u-pb4x u-mt3x"><div class="summary u-fs14 u-fw300 u-lineHeight1_5 u-tcGrayDarkest"><div class="summarized">Adsorption of water vapour on wool provides not only textile comfort, but also convenience in transportation due to increase in its bulk density. The adsorption and desorption isotherms of water vapour for wool were determined by both... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_5480415" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">Adsorption of water vapour on wool provides not only textile comfort, but also convenience in transportation due to increase in its bulk density. The adsorption and desorption isotherms of water vapour for wool were determined by both volumetric technique using a Coulter Omnisorp 100CX instrument and gravimetric method employing a Cahn 2000 electronic microbalance. Adsorption isotherm fitting to B.E.T. model and hysteresis on desorption was observed. The average effective diffusion coefficient of water in wool was found to be 8.4 × 10-14 m2s-1 at 25°C from gravimetric data. The effects of packing height and air velocity on the breakthrough curves were also investigated in the wool packed columns. For pseudo first order model, k values changing between 0.33 × 10-6 − 69 × 10-6 s-1 was obtained for 2.2–6.4 cm s-1 air velocity and 0.05–0.20 m packing height ranges.</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/5480415" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="bdc1f722381268e7127c60019de30f81" rel="nofollow" data-download="{"attachment_id":49276952,"asset_id":5480415,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/49276952/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="7705124" href="https://independent.academia.edu/Semra%C3%9Clk%C3%BC">Semra Ülkü</a><script data-card-contents-for-user="7705124" type="text/json">{"id":7705124,"first_name":"Semra","last_name":"Ülkü","domain_name":"independent","page_name":"SemraÜlkü","display_name":"Semra Ülkü","profile_url":"https://independent.academia.edu/Semra%C3%9Clk%C3%BC?f_ri=741421","photo":"/images/s65_no_pic.png"}</script></span></span></li><li class="js-paper-rank-work_5480415 InlineList-item InlineList-item--bordered hidden"><span class="js-paper-rank-view hidden u-tcGrayDark" data-paper-rank-work-id="5480415"><i class="u-m1x fa fa-bar-chart"></i><strong class="js-paper-rank"></strong></span><script>$(function() { new Works.PaperRankView({ workId: 5480415, container: ".js-paper-rank-work_5480415", }); 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The adsorption and desorption isotherms of water vapour for wool were determined by both volumetric technique using a Coulter Omnisorp 100CX instrument and gravimetric method employing a Cahn 2000 electronic microbalance. Adsorption isotherm fitting to B.E.T. model and hysteresis on desorption was observed. The average effective diffusion coefficient of water in wool was found to be 8.4 × 10-14 m2s-1 at 25°C from gravimetric data. The effects of packing height and air velocity on the breakthrough curves were also investigated in the wool packed columns. For pseudo first order model, k values changing between 0.33 × 10-6 − 69 × 10-6 s-1 was obtained for 2.2–6.4 cm s-1 air velocity and 0.05–0.20 m packing height ranges.","downloadable_attachments":[{"id":49276952,"asset_id":5480415,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":7705124,"first_name":"Semra","last_name":"Ülkü","domain_name":"independent","page_name":"SemraÜlkü","display_name":"Semra Ülkü","profile_url":"https://independent.academia.edu/Semra%C3%9Clk%C3%BC?f_ri=741421","photo":"/images/s65_no_pic.png"}],"research_interests":[{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering?f_ri=741421","nofollow":false},{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering?f_ri=741421","nofollow":false},{"id":39752,"name":"Adsorption","url":"https://www.academia.edu/Documents/in/Adsorption?f_ri=741421","nofollow":false},{"id":181847,"name":"First-Order 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Science","url":"https://www.academia.edu/Documents/in/Environmental_Science?f_ri=741421","nofollow":false},{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics?f_ri=741421","nofollow":false},{"id":6177,"name":"Modeling","url":"https://www.academia.edu/Documents/in/Modeling?f_ri=741421","nofollow":false},{"id":8937,"name":"Utilities","url":"https://www.academia.edu/Documents/in/Utilities?f_ri=741421"},{"id":10655,"name":"Scanning Electron Microscopy","url":"https://www.academia.edu/Documents/in/Scanning_Electron_Microscopy?f_ri=741421"},{"id":10866,"name":"Morphology","url":"https://www.academia.edu/Documents/in/Morphology?f_ri=741421"},{"id":39752,"name":"Adsorption","url":"https://www.academia.edu/Documents/in/Adsorption?f_ri=741421"},{"id":84278,"name":"Ph","url":"https://www.academia.edu/Documents/in/Ph?f_ri=741421"},{"id":168701,"name":"Sorption","url":"https://www.academia.edu/Documents/in/Sorption?f_ri=741421"},{"id":347272,"name":"Second Order","url":"https://www.academia.edu/Documents/in/Second_Order?f_ri=741421"},{"id":741421,"name":"Adsorption Isotherm Models","url":"https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models?f_ri=741421"},{"id":835697,"name":"Lumping Kinetic Model","url":"https://www.academia.edu/Documents/in/Lumping_Kinetic_Model?f_ri=741421"},{"id":989646,"name":"Aqueous Solution","url":"https://www.academia.edu/Documents/in/Aqueous_Solution?f_ri=741421"},{"id":1453161,"name":"Langmuir Isotherm","url":"https://www.academia.edu/Documents/in/Langmuir_Isotherm?f_ri=741421"}]}, }) } })();</script></ul></li></ul></div></div><div class="u-borderBottom1 u-borderColorGrayLighter"><div class="clearfix u-pv7x u-mb0x js-work-card work_13355817" data-work_id="13355817" itemscope="itemscope" itemtype="https://schema.org/ScholarlyArticle"><div class="header"><div class="title u-fontSerif u-fs22 u-lineHeight1_3"><a class="u-tcGrayDarkest js-work-link" href="https://www.academia.edu/13355817/Adsorption_behavior_and_activity_of_horseradish_peroxidase_onto_polysaccharide_decorated_particles">Adsorption behavior and activity of horseradish peroxidase onto polysaccharide-decorated particles</a></div></div><div class="u-pb4x u-mt3x"></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/13355817" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="cd4de07013c120eb9536bfcd76695c38" rel="nofollow" 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work: {"id":13355817,"title":"Adsorption behavior and activity of horseradish peroxidase onto polysaccharide-decorated particles","created_at":"2015-06-27T11:10:36.447-07:00","url":"https://www.academia.edu/13355817/Adsorption_behavior_and_activity_of_horseradish_peroxidase_onto_polysaccharide_decorated_particles?f_ri=741421","dom_id":"work_13355817","summary":null,"downloadable_attachments":[{"id":45436928,"asset_id":13355817,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":32590711,"first_name":"Denise","last_name":"Petri","domain_name":"independent","page_name":"DenisePetri","display_name":"Denise Petri","profile_url":"https://independent.academia.edu/DenisePetri?f_ri=741421","photo":"/images/s65_no_pic.png"}],"research_interests":[{"id":4512,"name":"Light Scattering","url":"https://www.academia.edu/Documents/in/Light_Scattering?f_ri=741421","nofollow":false},{"id":4749,"name":"Catalysis","url":"https://www.academia.edu/Documents/in/Catalysis?f_ri=741421","nofollow":false},{"id":10655,"name":"Scanning Electron Microscopy","url":"https://www.academia.edu/Documents/in/Scanning_Electron_Microscopy?f_ri=741421","nofollow":false},{"id":16061,"name":"Polysaccharides","url":"https://www.academia.edu/Documents/in/Polysaccharides?f_ri=741421","nofollow":false},{"id":39752,"name":"Adsorption","url":"https://www.academia.edu/Documents/in/Adsorption?f_ri=741421"},{"id":128057,"name":"Light","url":"https://www.academia.edu/Documents/in/Light?f_ri=741421"},{"id":231661,"name":"Enzyme","url":"https://www.academia.edu/Documents/in/Enzyme?f_ri=741421"},{"id":322549,"name":"Activity","url":"https://www.academia.edu/Documents/in/Activity?f_ri=741421"},{"id":413195,"name":"Time 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(PMMA)","url":"https://www.academia.edu/Documents/in/Polymethyl_Methacrylate_PMMA_?f_ri=741421"},{"id":1483261,"name":"Sodium Carboxymethylcellulose","url":"https://www.academia.edu/Documents/in/Sodium_Carboxymethylcellulose?f_ri=741421"},{"id":1681026,"name":"Biochemistry and cell biology","url":"https://www.academia.edu/Documents/in/Biochemistry_and_cell_biology?f_ri=741421"}]}, }) } })();</script></ul></li></ul></div></div><div class="u-borderBottom1 u-borderColorGrayLighter"><div class="clearfix u-pv7x u-mb0x js-work-card work_37599717" data-work_id="37599717" itemscope="itemscope" itemtype="https://schema.org/ScholarlyArticle"><div class="header"><div class="title u-fontSerif u-fs22 u-lineHeight1_3"><a class="u-tcGrayDarkest js-work-link" href="https://www.academia.edu/37599717/KOH_modified_Thevetia_peruviana_shell_activated_carbon_for_sorption_of_dimethoate_from_aqueous_solution">KOH modified Thevetia peruviana shell activated carbon for sorption of dimethoate from aqueous solution</a></div></div><div class="u-pb4x u-mt3x"><div class="summary u-fs14 u-fw300 u-lineHeight1_5 u-tcGrayDarkest"><div class="summarized">Modified Thevetia peruviana shell activated carbon for sorption of dimethoate from aqueous solution derived with potassium hydroxide (KOH) was studied at different concentrations for its potential application in water treatment. The batch... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_37599717" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">Modified Thevetia peruviana shell activated carbon for sorption of dimethoate from aqueous solution derived with potassium hydroxide (KOH) was studied at different concentrations for its potential application in water treatment. The batch sorption was investigated using dimethoate solution of 10–100mg/L concentrations. Proximate analysis was determined and changes on the surfaces and structure of the TPS were characterized after chemical activation with KOH using XRD, FTIR, SEM–EDAX, pHpzc, BET. The quantum chemical calculation for dimethoate yielded molecule associated energies of –9.8421 (HOMO) and –2.3879 (LUMO) and a total energy of –53,376.2. The kinetic of the sorption was modeled which indicated the sorption equilibrium time as 90min and pseudo-first order kinetics model showing R2=0.994 provided a better description of the process. Analysis of sorption equilibrium revealed that the data fitted well to Freundlich sorption isotherm model (R2=0.966), indicating multi-layer sorption of dimethoate on the surface of sorbent. The sorption of dimethoate onto KOHTPS shows 92.60% removal efficiency.</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/37599717" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="22b015df5f51fb36c355973dbd8a7dfa" rel="nofollow" data-download="{"attachment_id":57581080,"asset_id":37599717,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/57581080/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="23476191" href="https://ciu-tr.academia.edu/NdywilsluvWilliams">WILLIAMS E ND</a><script data-card-contents-for-user="23476191" type="text/json">{"id":23476191,"first_name":"WILLIAMS","last_name":"ND","domain_name":"ciu-tr","page_name":"NdywilsluvWilliams","display_name":"WILLIAMS E ND","profile_url":"https://ciu-tr.academia.edu/NdywilsluvWilliams?f_ri=741421","photo":"https://0.academia-photos.com/23476191/6364390/32292704/s65_ndifreke.williams.jpeg"}</script></span></span></li><li class="js-paper-rank-work_37599717 InlineList-item InlineList-item--bordered hidden"><span class="js-paper-rank-view hidden u-tcGrayDark" data-paper-rank-work-id="37599717"><i class="u-m1x fa fa-bar-chart"></i><strong class="js-paper-rank"></strong></span><script>$(function() { new Works.PaperRankView({ workId: 37599717, container: ".js-paper-rank-work_37599717", }); 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$(".js-view-count[data-work-id=37599717]").text(description); $(".js-view-count-work_37599717").attr('title', description).tooltip(); }); });</script></span><script>$(function() { $(".js-view-count-work_37599717").removeClass('hidden') })</script></div></li><li class="InlineList-item u-positionRelative" style="max-width: 250px"><div class="u-positionAbsolute" data-has-card-for-ri-list="37599717"><i class="fa fa-tag InlineList-item-icon u-positionRelative"></i> <a class="InlineList-item-text u-positionRelative">7</a> </div><span class="InlineList-item-text u-textTruncate u-pl9x"><a class="InlineList-item-text" data-has-card-for-ri="4987" href="https://www.academia.edu/Documents/in/Kinetics">Kinetics</a>, <script data-card-contents-for-ri="4987" type="text/json">{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics?f_ri=741421","nofollow":false}</script><a class="InlineList-item-text" data-has-card-for-ri="39752" href="https://www.academia.edu/Documents/in/Adsorption">Adsorption</a>, <script data-card-contents-for-ri="39752" type="text/json">{"id":39752,"name":"Adsorption","url":"https://www.academia.edu/Documents/in/Adsorption?f_ri=741421","nofollow":false}</script><a class="InlineList-item-text" data-has-card-for-ri="85437" href="https://www.academia.edu/Documents/in/Pesticides">Pesticides</a>, <script data-card-contents-for-ri="85437" type="text/json">{"id":85437,"name":"Pesticides","url":"https://www.academia.edu/Documents/in/Pesticides?f_ri=741421","nofollow":false}</script><a class="InlineList-item-text" data-has-card-for-ri="741421" href="https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models">Adsorption Isotherm Models</a><script data-card-contents-for-ri="741421" type="text/json">{"id":741421,"name":"Adsorption Isotherm Models","url":"https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models?f_ri=741421","nofollow":false}</script></span></li><script>(function(){ if (true) { new Aedu.ResearchInterestListCard({ el: $('*[data-has-card-for-ri-list=37599717]'), work: {"id":37599717,"title":"KOH modified Thevetia peruviana shell activated carbon for sorption of dimethoate from aqueous solution","created_at":"2018-10-17T05:39:20.595-07:00","url":"https://www.academia.edu/37599717/KOH_modified_Thevetia_peruviana_shell_activated_carbon_for_sorption_of_dimethoate_from_aqueous_solution?f_ri=741421","dom_id":"work_37599717","summary":"Modified Thevetia peruviana shell activated carbon for sorption of dimethoate from aqueous solution derived with potassium hydroxide (KOH) was studied at different concentrations for its potential application in water treatment. The batch sorption was investigated using dimethoate solution of 10–100mg/L concentrations. Proximate analysis was determined and changes on the surfaces and structure of the TPS were characterized after chemical activation with KOH using XRD, FTIR, SEM–EDAX, pHpzc, BET. The quantum chemical calculation for dimethoate yielded molecule associated energies of –9.8421 (HOMO) and –2.3879 (LUMO) and a total energy of –53,376.2. The kinetic of the sorption was modeled which indicated the sorption equilibrium time as 90min and pseudo-first order kinetics model showing R2=0.994 provided a better description of the process. Analysis of sorption equilibrium revealed that the data fitted well to Freundlich sorption isotherm model (R2=0.966), indicating multi-layer sorption of dimethoate on the surface of sorbent. The sorption of dimethoate onto KOHTPS shows 92.60% removal efficiency.","downloadable_attachments":[{"id":57581080,"asset_id":37599717,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":23476191,"first_name":"WILLIAMS","last_name":"ND","domain_name":"ciu-tr","page_name":"NdywilsluvWilliams","display_name":"WILLIAMS E ND","profile_url":"https://ciu-tr.academia.edu/NdywilsluvWilliams?f_ri=741421","photo":"https://0.academia-photos.com/23476191/6364390/32292704/s65_ndifreke.williams.jpeg"}],"research_interests":[{"id":4987,"name":"Kinetics","url":"https://www.academia.edu/Documents/in/Kinetics?f_ri=741421","nofollow":false},{"id":39752,"name":"Adsorption","url":"https://www.academia.edu/Documents/in/Adsorption?f_ri=741421","nofollow":false},{"id":85437,"name":"Pesticides","url":"https://www.academia.edu/Documents/in/Pesticides?f_ri=741421","nofollow":false},{"id":741421,"name":"Adsorption Isotherm Models","url":"https://www.academia.edu/Documents/in/Adsorption_Isotherm_Models?f_ri=741421","nofollow":false},{"id":858307,"name":"Quantum Chemical Studies","url":"https://www.academia.edu/Documents/in/Quantum_Chemical_Studies?f_ri=741421"},{"id":972790,"name":"Adsorbent","url":"https://www.academia.edu/Documents/in/Adsorbent?f_ri=741421"},{"id":1686960,"name":"Thevetia Peruviana (yellow Aleander)","url":"https://www.academia.edu/Documents/in/Thevetia_Peruviana_yellow_Aleander_?f_ri=741421"}]}, }) } })();</script></ul></li></ul></div></div><div class="u-borderBottom1 u-borderColorGrayLighter"><div class="clearfix u-pv7x u-mb0x js-work-card work_4969872 coauthored" data-work_id="4969872" itemscope="itemscope" itemtype="https://schema.org/ScholarlyArticle"><div class="header"><div class="title u-fontSerif u-fs22 u-lineHeight1_3"><a class="u-tcGrayDarkest js-work-link" href="https://www.academia.edu/4969872/The_Inhibition_of_aluminium_corrosion_in_hydrochloric_acid_solution_by_exudate_gum_from_Raphia_hookeri">The Inhibition of aluminium corrosion in hydrochloric acid solution by exudate gum from Raphia hookeri</a></div></div><div class="u-pb4x u-mt3x"></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/4969872" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="ecfc57e2060f36515f7ff783dcd16ee6" rel="nofollow" data-download="{"attachment_id":49508025,"asset_id":4969872,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/49508025/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="2294129" href="https://uniuyo.academia.edu/SaviourUmoren">Saviour Umoren</a><script data-card-contents-for-user="2294129" type="text/json">{"id":2294129,"first_name":"Saviour","last_name":"Umoren","domain_name":"uniuyo","page_name":"SaviourUmoren","display_name":"Saviour Umoren","profile_url":"https://uniuyo.academia.edu/SaviourUmoren?f_ri=741421","photo":"https://0.academia-photos.com/2294129/2623642/130223355/s65_saviour.umoren.jpg"}</script></span></span><span class="u-displayInlineBlock InlineList-item-text"> and <span class="u-textDecorationUnderline u-clickable InlineList-item-text js-work-more-authors-4969872">+1</span><div class="hidden js-additional-users-4969872"><div><span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a href="https://unisouthafr.academia.edu/EEbenso">E. 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The bamboo was cut into sizes, washing and drying was carbonized at 400oC-500oC and activated... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_8673650" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">Kinetics of batch adsorption of iron II ions from aqueous solution using activated carbon from waste Nigerian based Nigerian bamboo was studied. The bamboo was cut into sizes, washing and drying was carbonized at 400oC-500oC and activated at 800oC using nitric acid. The effect of process parameters such as particle size, carbon dosage, initial concentration of adsorbate and contact time were also investigated and were found to significantly affect the adsorption capacity. The adsorption process obeyed the Freundlich, Temkin and Langmuir isotherm model indicating a monolayer formation over the surface of the material. Langmuir isotherm had a better fit than Freundlich and Temkin models with maximum monolayer saturation capacity of 166.7 mg of iron II ions adsorbed per g of bamboo activated carbon. In order to determine the mechanism of sorption, kinetic data were modeled using the pseudo first order, pseudo second order kinetic equations, and intra-particle diffusion model. The pseudo second order equation was the best applicable model to describe the sorption process. Hence the pseudo second order kinetic reaction is the rate controlling step with some intra particle diffusion taking place.<br />Keywords: Nigerian Bamboo, Activated Carbon, Iron</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/8673650" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="b669a55a7c969762069ad2274a094d3a" rel="nofollow" data-download="{"attachment_id":35028842,"asset_id":8673650,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/35028842/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="4189959" href="https://rsust.academia.edu/AwajiogakUjile">Awajiogak A Ujile</a><script data-card-contents-for-user="4189959" type="text/json">{"id":4189959,"first_name":"Awajiogak","last_name":"Ujile","domain_name":"rsust","page_name":"AwajiogakUjile","display_name":"Awajiogak A Ujile","profile_url":"https://rsust.academia.edu/AwajiogakUjile?f_ri=741421","photo":"https://0.academia-photos.com/4189959/1642803/18719382/s65_awajiogak.ujile.jpg"}</script></span></span></li><li class="js-paper-rank-work_8673650 InlineList-item InlineList-item--bordered hidden"><span class="js-paper-rank-view hidden u-tcGrayDark" data-paper-rank-work-id="8673650"><i class="u-m1x fa fa-bar-chart"></i><strong class="js-paper-rank"></strong></span><script>$(function() { new Works.PaperRankView({ workId: 8673650, container: ".js-paper-rank-work_8673650", }); 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The bamboo was cut into sizes, washing and drying was carbonized at 400oC-500oC and activated at 800oC using nitric acid. The effect of process parameters such as particle size, carbon dosage, initial concentration of adsorbate and contact time were also investigated and were found to significantly affect the adsorption capacity. The adsorption process obeyed the Freundlich, Temkin and Langmuir isotherm model indicating a monolayer formation over the surface of the material. Langmuir isotherm had a better fit than Freundlich and Temkin models with maximum monolayer saturation capacity of 166.7 mg of iron II ions adsorbed per g of bamboo activated carbon. In order to determine the mechanism of sorption, kinetic data were modeled using the pseudo first order, pseudo second order kinetic equations, and intra-particle diffusion model. The pseudo second order equation was the best applicable model to describe the sorption process. Hence the pseudo second order kinetic reaction is the rate controlling step with some intra particle diffusion taking place.\nKeywords: Nigerian Bamboo, Activated Carbon, Iron","downloadable_attachments":[{"id":35028842,"asset_id":8673650,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":4189959,"first_name":"Awajiogak","last_name":"Ujile","domain_name":"rsust","page_name":"AwajiogakUjile","display_name":"Awajiogak A Ujile","profile_url":"https://rsust.academia.edu/AwajiogakUjile?f_ri=741421","photo":"https://0.academia-photos.com/4189959/1642803/18719382/s65_awajiogak.ujile.jpg"}],"research_interests":[{"id":55,"name":"Environmental Engineering","url":"https://www.academia.edu/Documents/in/Environmental_Engineering?f_ri=741421","nofollow":false},{"id":72,"name":"Chemical 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href="https://www.academia.edu/69792843/Adsorption_Isotherm_Analysis_for_CO2_Capture_Using_Barium_Oxide_Impregnated_Iron_III_Oxide_by_Ultrasonic_Assisted_Synthesis">Adsorption Isotherm Analysis for CO2 Capture Using Barium Oxide Impregnated Iron(III) Oxide by Ultrasonic-Assisted Synthesis</a></div></div><div class="u-pb4x u-mt3x"><div class="summary u-fs14 u-fw300 u-lineHeight1_5 u-tcGrayDarkest"><div class="summarized">The barium oxide impregnated iron(III) oxide (BaO/Fe2O3) adsorbent was synthesized by an ultrasonic-assisted method. The adsorbent was calcined at 200-500 °C and its adsorption capacity was measured. The ultrasonic-assisted synthesis... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_69792843" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">The barium oxide impregnated iron(III) oxide (BaO/Fe2O3) adsorbent was synthesized by an ultrasonic-assisted method. The adsorbent was calcined at 200-500 °C and its adsorption capacity was measured. The ultrasonic-assisted synthesis generated well-dispersed of BaO on Fe2O3 by giving none of the BaO peaks were observed through the XRD pattern. The most efficient adsorbent of BaO/Fe2O3200 was calcined at 200 °C with adsorption capacity for physisorption and chemisorption of 5.01 and 88.81 mg/g respectively. Besides other carbonate species, it was believed the presence of the hydroxyl group could enhance the sorption by forming bicarbonate upon CO2 chemisorption. It is also possessed a lower desorption range compared to BaO and Fe2O3 alone. The experimental CO2 adsorption isotherm at 25 °C fit better with the Freundlich isotherm model. It implies a favorable adsorption process with multilayer adsorption occurs onto the heterogeneous surface.</div></div></div><ul class="InlineList u-ph0x u-fs13"><li class="InlineList-item logged_in_only"><div class="share_on_academia_work_button"><a class="academia_share Button Button--inverseBlue Button--sm js-bookmark-button" data-academia-share="Work/69792843" data-share-source="work_strip" data-spinner="small_white_hide_contents"><i class="fa fa-plus"></i><span class="work-strip-link-text u-ml1x" data-content="button_text">Bookmark</span></a></div></li><li class="InlineList-item"><div class="download"><a id="0b4cf6bec18fb8e443fd67766e116bb1" rel="nofollow" data-download="{"attachment_id":79752229,"asset_id":69792843,"asset_type":"Work","always_allow_download":false,"track":null,"button_location":"work_strip","source":null,"hide_modal":null}" class="Button Button--sm Button--inverseGreen js-download-button prompt_button doc_download" href="https://www.academia.edu/attachments/79752229/download_file?st=MTczMzI2Njk0Miw4LjIyMi4yMDguMTQ2&s=work_strip"><i class="fa fa-arrow-circle-o-down fa-lg"></i><span class="u-textUppercase u-ml1x" data-content="button_text">Download</span></a></div></li><li class="InlineList-item"><ul class="InlineList InlineList--bordered u-ph0x"><li class="InlineList-item InlineList-item--bordered"><span class="InlineList-item-text">by <span itemscope="itemscope" itemprop="author" itemtype="https://schema.org/Person"><a class="u-tcGrayDark u-fw700" data-has-card-for-user="25928676" href="https://upm.academia.edu/AzizulHakimLahuri">Azizul Hakim Lahuri</a><script data-card-contents-for-user="25928676" type="text/json">{"id":25928676,"first_name":"Azizul Hakim","last_name":"Lahuri","domain_name":"upm","page_name":"AzizulHakimLahuri","display_name":"Azizul Hakim Lahuri","profile_url":"https://upm.academia.edu/AzizulHakimLahuri?f_ri=741421","photo":"https://0.academia-photos.com/25928676/7111313/8124402/s65_azizul_hakim.lahuri.jpg"}</script></span></span></li><li class="js-paper-rank-work_69792843 InlineList-item InlineList-item--bordered hidden"><span class="js-paper-rank-view hidden u-tcGrayDark" data-paper-rank-work-id="69792843"><i class="u-m1x fa fa-bar-chart"></i><strong class="js-paper-rank"></strong></span><script>$(function() { new Works.PaperRankView({ workId: 69792843, container: ".js-paper-rank-work_69792843", }); 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The adsorbent was calcined at 200-500 °C and its adsorption capacity was measured. The ultrasonic-assisted synthesis generated well-dispersed of BaO on Fe2O3 by giving none of the BaO peaks were observed through the XRD pattern. The most efficient adsorbent of BaO/Fe2O3200 was calcined at 200 °C with adsorption capacity for physisorption and chemisorption of 5.01 and 88.81 mg/g respectively. Besides other carbonate species, it was believed the presence of the hydroxyl group could enhance the sorption by forming bicarbonate upon CO2 chemisorption. It is also possessed a lower desorption range compared to BaO and Fe2O3 alone. The experimental CO2 adsorption isotherm at 25 °C fit better with the Freundlich isotherm model. It implies a favorable adsorption process with multilayer adsorption occurs onto the heterogeneous surface.","downloadable_attachments":[{"id":79752229,"asset_id":69792843,"asset_type":"Work","always_allow_download":false}],"ordered_authors":[{"id":25928676,"first_name":"Azizul Hakim","last_name":"Lahuri","domain_name":"upm","page_name":"AzizulHakimLahuri","display_name":"Azizul Hakim Lahuri","profile_url":"https://upm.academia.edu/AzizulHakimLahuri?f_ri=741421","photo":"https://0.academia-photos.com/25928676/7111313/8124402/s65_azizul_hakim.lahuri.jpg"}],"research_interests":[{"id":39752,"name":"Adsorption","url":"https://www.academia.edu/Documents/in/Adsorption?f_ri=741421","nofollow":false},{"id":43832,"name":"CO2 capture and storage","url":"https://www.academia.edu/Documents/in/CO2_capture_and_storage?f_ri=741421","nofollow":false},{"id":83593,"name":"CO2 Capturing 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The data were analyzed using the Hailwood Horrobin model for isotherm fitting and determination of monolayer... <a class="more_link u-tcGrayDark u-linkUnstyled" data-container=".work_6693274" data-show=".complete" data-hide=".summarized" data-more-link-behavior="true" href="#">more</a></div><div class="complete hidden">The water vapor sorption behavior of a range of natural fibers (jute, flax, coir, cotton, hemp, Sitka spruce) has been studied. The data were analyzed using the Hailwood Horrobin model for isotherm fitting and determination of monolayer moisture content. The Hailwood Horrobin model was found to provide good fits to the experimental data. The extent of hysteresis exhibited between the adsorption and desorption isotherms was dependent on fiber type studied and was larger with high lignin compared with low lignin content fibers. The area bounded by the hysteresis loop decreased as the isotherms were performed at progressively higher temperatures. This behavior is consistent with sorption interactions occurring with a glassy solid below the glass transition temperature. © 2009 Wiley Periodicals, Inc. 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