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class="js-profile-view-count"></span></p></div></span></div><div class="ri-section"><div class="ri-section-header"><span>Interests</span></div><div class="ri-tags-container"><a data-click-track="profile-user-info-expand-research-interests" data-has-card-for-ri-list="266870439" href="https://www.academia.edu/Documents/in/History_of_Women"><div id="js-react-on-rails-context" style="display:none" data-rails-context="{"inMailer":false,"i18nLocale":"en","i18nDefaultLocale":"en","href":"https://independent.academia.edu/BernhardSeyfang","location":"/BernhardSeyfang","scheme":"https","host":"independent.academia.edu","port":null,"pathname":"/BernhardSeyfang","search":null,"httpAcceptLanguage":null,"serverSide":false}"></div> <div class="js-react-on-rails-component" style="display:none" data-component-name="Pill" data-props="{"color":"gray","children":["History of Women"]}" data-trace="false" data-dom-id="Pill-react-component-89ed9dce-4da4-4275-8842-5f44e96da01b"></div> <div 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data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/106225171/Inhibition_of_corrosion_of_AISI_316L_steel_in_concentrated_acetic_acid_containing_NaCl_additions"><img alt="Research paper thumbnail of Inhibition of corrosion of AISI 316L steel in concentrated acetic acid containing NaCl additions" 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/106225171/Inhibition_of_corrosion_of_AISI_316L_steel_in_concentrated_acetic_acid_containing_NaCl_additions">Inhibition of corrosion of AISI 316L steel in concentrated acetic acid containing NaCl additions</a></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action 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thumbnail of Entwicklung eines industrierelevanten Ansatzes zur Modellierung von Pervaporationen" class="work-thumbnail" src="https://attachments.academia-assets.com/105477486/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/106225170/Entwicklung_eines_industrierelevanten_Ansatzes_zur_Modellierung_von_Pervaporationen">Entwicklung eines industrierelevanten Ansatzes zur Modellierung von Pervaporationen</a></div><div class="wp-workCard_item"><span>Chemie Ingenieur Technik</span><span>, 2014</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="e9264ee294246bc2ce4b995b1a2f1c66" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" 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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":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":554780,"name":"Interdisciplinary Engineering","url":"https://www.academia.edu/Documents/in/Interdisciplinary_Engineering"}],"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="106225165"><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/106225165/One_Dimensional_Modeling_of_Mass_Transfer_Processes_in_an_Annular_Centrifugal_Contactor"><img alt="Research paper thumbnail of One-Dimensional Modeling of Mass Transfer Processes in an Annular Centrifugal Contactor" class="work-thumbnail" src="https://attachments.academia-assets.com/105477467/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/106225165/One_Dimensional_Modeling_of_Mass_Transfer_Processes_in_an_Annular_Centrifugal_Contactor">One-Dimensional Modeling of Mass Transfer Processes in an Annular Centrifugal Contactor</a></div><div class="wp-workCard_item"><span>ChemEngineering</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">Due to the importance of process intensification, modeling of Annular Centrifugal Contactors (ACC...</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">Due to the importance of process intensification, modeling of Annular Centrifugal Contactors (ACCs) is becoming of increasing interest. By the current state of scientific knowledge, universal modeling without high computing power of these complex apparatuses is not possible to a satisfactory degree. In this article, a one-dimensional model to describe the mass transfer during a physical extraction process in an ACC is presented. The model is based on solely geometrical data and operating conditions of the ACC, as well as physical properties of the components. Regarding the selection of physical properties, only physical properties that are easily accessible were used. With this model, mass transfer calculations are possible and therefore, the output concentrations can be predicted. Simulations of an ACC based on the model were done by creating and running a python code. Validation of the model was conducted by varying and comparing operating conditions in both the simulation and the...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="8b813d20dc693aab38db70b37224f25a" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":105477467,"asset_id":106225165,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/105477467/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="106225165"><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="106225165"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 106225165; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=106225165]").text(description); $(".js-view-count[data-work-id=106225165]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 106225165; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='106225165']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 106225165, 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: "8b813d20dc693aab38db70b37224f25a" } } $('.js-work-strip[data-work-id=106225165]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":106225165,"title":"One-Dimensional Modeling of Mass Transfer Processes in an Annular Centrifugal Contactor","translated_title":"","metadata":{"abstract":"Due to the importance of process intensification, modeling of Annular Centrifugal Contactors (ACCs) is becoming of increasing interest. By the current state of scientific knowledge, universal modeling without high computing power of these complex apparatuses is not possible to a satisfactory degree. In this article, a one-dimensional model to describe the mass transfer during a physical extraction process in an ACC is presented. The model is based on solely geometrical data and operating conditions of the ACC, as well as physical properties of the components. Regarding the selection of physical properties, only physical properties that are easily accessible were used. With this model, mass transfer calculations are possible and therefore, the output concentrations can be predicted. Simulations of an ACC based on the model were done by creating and running a python code. 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Simulations of an ACC based on the model were done by creating and running a python code. 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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="100631008"><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/100631008/Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers"><img alt="Research paper thumbnail of Continuous Nanoprecipitation of Polycaprolactone in Additively Manufactured Micromixers" class="work-thumbnail" src="https://attachments.academia-assets.com/101399021/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/100631008/Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers">Continuous Nanoprecipitation of Polycaprolactone in Additively Manufactured Micromixers</a></div><div class="wp-workCard_item"><span>Polymers</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with b...</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 polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with biologically degradable polymers. Usually, a discontinuous or semi-continuous process is employed due to its low technical effort and the fact that the amount of dispersions needed in a laboratory is relatively small. However, the number of particles produced in this method is not enough to make this process economically feasible. Therefore, it is necessary to improve the productivity of the process and create a controllable and robust continuous process with the potential to control parameters, such as the particle size or surface properties. In this study, nanoparticles were formulated from polycaprolactone (PCL) in a continuous process using additively manufactured micromixers. The main goal was to be able to exert control on the particle parameters in terms of size and zeta potential. The results showed that particle size could be adjusted in the range of 130 to 465 nm by using differ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="65acfb3e439e40413a323cc63b98c73f" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399021,"asset_id":100631008,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399021/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100631008"><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="100631008"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100631008; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100631008]").text(description); $(".js-view-count[data-work-id=100631008]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100631008; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100631008']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100631008, 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: "65acfb3e439e40413a323cc63b98c73f" } } $('.js-work-strip[data-work-id=100631008]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100631008,"title":"Continuous Nanoprecipitation of Polycaprolactone in Additively Manufactured Micromixers","translated_title":"","metadata":{"abstract":"The polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with biologically degradable polymers. Usually, a discontinuous or semi-continuous process is employed due to its low technical effort and the fact that the amount of dispersions needed in a laboratory is relatively small. However, the number of particles produced in this method is not enough to make this process economically feasible. Therefore, it is necessary to improve the productivity of the process and create a controllable and robust continuous process with the potential to control parameters, such as the particle size or surface properties. In this study, nanoparticles were formulated from polycaprolactone (PCL) in a continuous process using additively manufactured micromixers. The main goal was to be able to exert control on the particle parameters in terms of size and zeta potential. The results showed that particle size could be adjusted in the range of 130 to 465 nm by using differ...","publisher":"MDPI AG","publication_name":"Polymers"},"translated_abstract":"The polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with biologically degradable polymers. Usually, a discontinuous or semi-continuous process is employed due to its low technical effort and the fact that the amount of dispersions needed in a laboratory is relatively small. However, the number of particles produced in this method is not enough to make this process economically feasible. Therefore, it is necessary to improve the productivity of the process and create a controllable and robust continuous process with the potential to control parameters, such as the particle size or surface properties. In this study, nanoparticles were formulated from polycaprolactone (PCL) in a continuous process using additively manufactured micromixers. The main goal was to be able to exert control on the particle parameters in terms of size and zeta potential. The results showed that particle size could be adjusted in the range of 130 to 465 nm by using differ...","internal_url":"https://www.academia.edu/100631008/Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers","translated_internal_url":"","created_at":"2023-04-23T08:35:46.381-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":101399021,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/101399021/thumbnails/1.jpg","file_name":"pdf.pdf","download_url":"https://www.academia.edu/attachments/101399021/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Continuous_Nanoprecipitation_of_Polycapr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/101399021/pdf-libre.pdf?1682280002=\u0026response-content-disposition=attachment%3B+filename%3DContinuous_Nanoprecipitation_of_Polycapr.pdf\u0026Expires=1732466740\u0026Signature=WFTf9FD6M8RgMp4s5E7Rxwr9ZUdV3BJnrSAyf7IHiKdr~3NSkMXwsl79zLKR6CP9fgWw1h66ofzSXYnfGGjCBRzkFJxxkYnBnR6jslgMqUQn6wh0-Gy9Z4fYBSHNQTKaEQh1PS179ypAE6UgTvfoKdv8rCqyLgxROrA59X~LyJBEH3b8p1QN3g~JrReXCEV2P2YXZ5BfxSRKrqvsVS9y6GHNkhWMtE65Zw0zG9Dj7EkBgn-72y6KJ0NYjRe-rMQzOprbcaMuT4~NPrRVfOO9unXKG2ztr9B53fGKrhnKWjuWWcu07H-78P8q9B3BGqmMSYjRlORppjqy0yDcbv5lEw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers","translated_slug":"","page_count":14,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[{"id":101399021,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/101399021/thumbnails/1.jpg","file_name":"pdf.pdf","download_url":"https://www.academia.edu/attachments/101399021/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Continuous_Nanoprecipitation_of_Polycapr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/101399021/pdf-libre.pdf?1682280002=\u0026response-content-disposition=attachment%3B+filename%3DContinuous_Nanoprecipitation_of_Polycapr.pdf\u0026Expires=1732466740\u0026Signature=WFTf9FD6M8RgMp4s5E7Rxwr9ZUdV3BJnrSAyf7IHiKdr~3NSkMXwsl79zLKR6CP9fgWw1h66ofzSXYnfGGjCBRzkFJxxkYnBnR6jslgMqUQn6wh0-Gy9Z4fYBSHNQTKaEQh1PS179ypAE6UgTvfoKdv8rCqyLgxROrA59X~LyJBEH3b8p1QN3g~JrReXCEV2P2YXZ5BfxSRKrqvsVS9y6GHNkhWMtE65Zw0zG9Dj7EkBgn-72y6KJ0NYjRe-rMQzOprbcaMuT4~NPrRVfOO9unXKG2ztr9B53fGKrhnKWjuWWcu07H-78P8q9B3BGqmMSYjRlORppjqy0yDcbv5lEw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":8950,"name":"Nanoparticle","url":"https://www.academia.edu/Documents/in/Nanoparticle"},{"id":21466,"name":"Polymers","url":"https://www.academia.edu/Documents/in/Polymers"},{"id":26327,"name":"Medicine","url":"https://www.academia.edu/Documents/in/Medicine"},{"id":177878,"name":"Polycaprolactone","url":"https://www.academia.edu/Documents/in/Polycaprolactone"},{"id":390245,"name":"Particle Size","url":"https://www.academia.edu/Documents/in/Particle_Size"},{"id":983062,"name":"Zeta Potential","url":"https://www.academia.edu/Documents/in/Zeta_Potential"}],"urls":[{"id":30851811,"url":"https://www.mdpi.com/2073-4360/14/8/1509/pdf"}]}, 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="100631007"><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/100631007/Prediction_of_Excess_Enthalpy_Using_Volume_Translated_Peng_Robinson_Equation_of_State"><img alt="Research paper thumbnail of Prediction of Excess Enthalpy Using Volume-Translated Peng–Robinson Equation of State" class="work-thumbnail" src="https://attachments.academia-assets.com/101399060/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/100631007/Prediction_of_Excess_Enthalpy_Using_Volume_Translated_Peng_Robinson_Equation_of_State">Prediction of Excess Enthalpy Using Volume-Translated Peng–Robinson Equation of State</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In this work volume-translated Peng–Robinson group contribution equation of state was used to cal...</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 work volume-translated Peng–Robinson group contribution equation of state was used to calculate excess enthalpies. Four model systems were selected with the purpose to compare experimental and predicted enthalpy values at different temperatures. After the calculations were performed in Matlab software, results were verified with free software tool of Dortmunder Datenbank (DDB). In a next step, the mixing process and interaction forces were described on the basis of the sign and course of enthalpy values. The endothermic behavior of three systems could be well predicted, while for the most polar system, predictions were less precise. Furthermore, the discrepancy between experimental data from the literature and predicted values was discussed to evaluate the accuracy of the selected model. Lowest mean deviations (&lt;75 J/mol and &lt;15% at all temperatures) could be stated for alkane/benzene mixtures, while highest deviations could be again observed for the most polar mixture...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="be20ae17d21c8d7caac92a94eff80d5c" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399060,"asset_id":100631007,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399060/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100631007"><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="100631007"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100631007; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100631007]").text(description); $(".js-view-count[data-work-id=100631007]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100631007; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100631007']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100631007, 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: "be20ae17d21c8d7caac92a94eff80d5c" } } $('.js-work-strip[data-work-id=100631007]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100631007,"title":"Prediction of Excess Enthalpy Using Volume-Translated Peng–Robinson Equation of State","translated_title":"","metadata":{"abstract":"In this work volume-translated Peng–Robinson group contribution equation of state was used to calculate excess enthalpies. 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Engineering Chemistry Research</span><span>, 2020</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="5f24d585f5d8d3c076da1643860d5ffa" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399059,"asset_id":100631000,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399059/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100631000"><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="100631000"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100631000; 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$(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="100630997"><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/100630997/Extraction_Centrifuges_Intensified_Equipment_Facilitating_Modular_and_Flexible_Plant_Concepts"><img alt="Research paper thumbnail of Extraction Centrifuges—Intensified Equipment Facilitating Modular and Flexible Plant Concepts" class="work-thumbnail" src="https://attachments.academia-assets.com/101399020/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/100630997/Extraction_Centrifuges_Intensified_Equipment_Facilitating_Modular_and_Flexible_Plant_Concepts">Extraction Centrifuges—Intensified Equipment Facilitating Modular and Flexible Plant Concepts</a></div><div class="wp-workCard_item"><span>ChemEngineering</span><span>, 2019</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In recent years, modularization of chemical production plants has become a widely discussed trend...</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, modularization of chemical production plants has become a widely discussed trend to overcome some of key issues the chemical industry struggles with. High volatility in raw material and customer markets, shorter product life cycles, cost pressure and increasing competition are just a few of them. Modularization of chemical production offers the opportunity to deal with these issues. The unit operations, which are capable to be applied in modular plant concepts, are subject of on-going research. On the reaction side, tubular continuous flow reactors are typical assets and methods for design and operation are available on a high technical level. Separation units on the downstream side are not yet developed to technical maturity. This paper focuses on extraction centrifuges, which are promising devices due to their large range of application, small volumes, high separation efficiency and excellent scalability. Industrial examples show the performance of extraction cent...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="b45259eec1c22e1fa5ae644c72754602" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399020,"asset_id":100630997,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399020/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100630997"><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="100630997"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630997; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630997]").text(description); $(".js-view-count[data-work-id=100630997]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630997; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630997']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630997, 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: "b45259eec1c22e1fa5ae644c72754602" } } $('.js-work-strip[data-work-id=100630997]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630997,"title":"Extraction Centrifuges—Intensified Equipment Facilitating Modular and Flexible Plant Concepts","translated_title":"","metadata":{"abstract":"In recent years, modularization of chemical production plants has become a widely discussed trend to overcome some of key issues the chemical industry struggles with. 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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="100630992"><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/100630992/2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures"><img alt="Research paper thumbnail of 2+1D modelling of a polymer electrolyte fuel cell with glassy-carbon microstructures" 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/100630992/2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures">2+1D modelling of a polymer electrolyte fuel cell with glassy-carbon microstructures</a></div><div class="wp-workCard_item"><span>Mathematical and Computer Modelling of Dynamical Systems</span><span>, 2012</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">ABSTRACT A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented...</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 A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented, based on a 2+1D FEM modelling approach. This approach is suitable to take the high aspect ratio between the in-plane and the through-plane dimensions of fuel cells into account, and to avoid expensive 3D calculations. The anode and cathode are described by 2D transport models. The coupling between the anode and cathode side is established by a nonlinear point-to-point 1D model representing the membrane electrode assembly (MEA). This 1D boundary value problem is formulated using the computer algebra software Mathematica. The approach is based on the symbolic weak form expressions of a nonlinear system of PDEs. The integrands of the tangential element stiffness matrix and the element residual vector of the coupled FEM problem are computed analytically. These integrands are converted to C code automatically. The model is applied to simulate a micro PEFC without gas diffusion layers (GDLs). The simulations reveal an inhomogeneous in-plane electric current density. Further, neutron radiography data obtained with the micro fuel cell is compared to the calculated water flux between the 1D MEA model and the 2D domains. The model is used to explain the locations where water condensation is found.</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="100630992"><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="100630992"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630992; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630992]").text(description); $(".js-view-count[data-work-id=100630992]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630992; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630992']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630992, 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" } } $('.js-work-strip[data-work-id=100630992]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630992,"title":"2+1D modelling of a polymer electrolyte fuel cell with glassy-carbon microstructures","translated_title":"","metadata":{"abstract":"ABSTRACT A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented, based on a 2+1D FEM modelling approach. This approach is suitable to take the high aspect ratio between the in-plane and the through-plane dimensions of fuel cells into account, and to avoid expensive 3D calculations. The anode and cathode are described by 2D transport models. The coupling between the anode and cathode side is established by a nonlinear point-to-point 1D model representing the membrane electrode assembly (MEA). This 1D boundary value problem is formulated using the computer algebra software Mathematica. The approach is based on the symbolic weak form expressions of a nonlinear system of PDEs. The integrands of the tangential element stiffness matrix and the element residual vector of the coupled FEM problem are computed analytically. These integrands are converted to C code automatically. The model is applied to simulate a micro PEFC without gas diffusion layers (GDLs). The simulations reveal an inhomogeneous in-plane electric current density. Further, neutron radiography data obtained with the micro fuel cell is compared to the calculated water flux between the 1D MEA model and the 2D domains. The model is used to explain the locations where water condensation is found.","publisher":"Informa UK Limited","publication_date":{"day":null,"month":null,"year":2012,"errors":{}},"publication_name":"Mathematical and Computer Modelling of Dynamical Systems"},"translated_abstract":"ABSTRACT A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented, based on a 2+1D FEM modelling approach. This approach is suitable to take the high aspect ratio between the in-plane and the through-plane dimensions of fuel cells into account, and to avoid expensive 3D calculations. The anode and cathode are described by 2D transport models. The coupling between the anode and cathode side is established by a nonlinear point-to-point 1D model representing the membrane electrode assembly (MEA). This 1D boundary value problem is formulated using the computer algebra software Mathematica. The approach is based on the symbolic weak form expressions of a nonlinear system of PDEs. The integrands of the tangential element stiffness matrix and the element residual vector of the coupled FEM problem are computed analytically. These integrands are converted to C code automatically. The model is applied to simulate a micro PEFC without gas diffusion layers (GDLs). The simulations reveal an inhomogeneous in-plane electric current density. Further, neutron radiography data obtained with the micro fuel cell is compared to the calculated water flux between the 1D MEA model and the 2D domains. The model is used to explain the locations where water condensation is found.","internal_url":"https://www.academia.edu/100630992/2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures","translated_internal_url":"","created_at":"2023-04-23T08:35:45.299-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[],"research_interests":[{"id":237,"name":"Cognitive Science","url":"https://www.academia.edu/Documents/in/Cognitive_Science"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":2161,"name":"Microstructure","url":"https://www.academia.edu/Documents/in/Microstructure"},{"id":7477,"name":"Fuel Cells","url":"https://www.academia.edu/Documents/in/Fuel_Cells"},{"id":58527,"name":"Polymer","url":"https://www.academia.edu/Documents/in/Polymer"},{"id":173959,"name":"Current Density","url":"https://www.academia.edu/Documents/in/Current_Density"},{"id":201678,"name":"Computer Algebra","url":"https://www.academia.edu/Documents/in/Computer_Algebra"},{"id":352783,"name":"Glassy Carbon","url":"https://www.academia.edu/Documents/in/Glassy_Carbon"},{"id":473797,"name":"Microstructures","url":"https://www.academia.edu/Documents/in/Microstructures"},{"id":506858,"name":"Nonlinear system","url":"https://www.academia.edu/Documents/in/Nonlinear_system"},{"id":863497,"name":"Carbon Fibers","url":"https://www.academia.edu/Documents/in/Carbon_Fibers"},{"id":939537,"name":"Boundary Value Problem","url":"https://www.academia.edu/Documents/in/Boundary_Value_Problem"},{"id":1214993,"name":"Neutron Radiography","url":"https://www.academia.edu/Documents/in/Neutron_Radiography"},{"id":1276642,"name":"Electrolyte","url":"https://www.academia.edu/Documents/in/Electrolyte"},{"id":2742746,"name":"High aspect ratio","url":"https://www.academia.edu/Documents/in/High_aspect_ratio"}],"urls":[{"id":30851799,"url":"http://www.tandfonline.com/doi/pdf/10.1080/13873954.2011.642390"}]}, 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="100630991"><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/100630991/Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties"><img alt="Research paper thumbnail of Using2H labeling with neutron radiography for the study of solid polymer electrolyte water transport properties" 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/100630991/Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties">Using2H labeling with neutron radiography for the study of solid polymer electrolyte water transport properties</a></div><div class="wp-workCard_item"><span>Journal of Physics: Condensed Matter</span><span>, 2011</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neu...</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">A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neutron imaging for the analysis of transport parameters in the bulk and at the interfaces of Nafion polymer electrolyte membranes is proposed. The use of different isotope compositions in the steady state allows evaluation of the relation between bulk and interface transport parameters, but relies on literature data for evaluating absolute values. By using transients of isotope composition, absolute values of these parameters including the self-diffusion coefficient of H can be extracted, making this method an attractive alternative to self-diffusion measurements using nuclear magnetic resonance (NMR), allowing measurements in precisely controlled conditions in real fuel cell structures. First measurements were realized on samples with and without electrodes and we report values of the self-diffusion coefficient of the same order of magnitude as values measured using NMR, although with slightly higher numbers. In our particular case, lower interfacial exchange rates for water transport were observed for samples with an electrode.</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="100630991"><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="100630991"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630991; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630991]").text(description); $(".js-view-count[data-work-id=100630991]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630991; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630991']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630991, 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" } } $('.js-work-strip[data-work-id=100630991]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630991,"title":"Using2H labeling with neutron radiography for the study of solid polymer electrolyte water transport properties","translated_title":"","metadata":{"abstract":"A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neutron imaging for the analysis of transport parameters in the bulk and at the interfaces of Nafion polymer electrolyte membranes is proposed. 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In our particular case, lower interfacial exchange rates for water transport were observed for samples with an electrode.","publisher":"IOP Publishing","publication_date":{"day":null,"month":null,"year":2011,"errors":{}},"publication_name":"Journal of Physics: Condensed Matter"},"translated_abstract":"A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neutron imaging for the analysis of transport parameters in the bulk and at the interfaces of Nafion polymer electrolyte membranes is proposed. The use of different isotope compositions in the steady state allows evaluation of the relation between bulk and interface transport parameters, but relies on literature data for evaluating absolute values. By using transients of isotope composition, absolute values of these parameters including the self-diffusion coefficient of H can be extracted, making this method an attractive alternative to self-diffusion measurements using nuclear magnetic resonance (NMR), allowing measurements in precisely controlled conditions in real fuel cell structures. First measurements were realized on samples with and without electrodes and we report values of the self-diffusion coefficient of the same order of magnitude as values measured using NMR, although with slightly higher numbers. In our particular case, lower interfacial exchange rates for water transport were observed for samples with an electrode.","internal_url":"https://www.academia.edu/100630991/Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties","translated_internal_url":"","created_at":"2023-04-23T08:35:45.146-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[],"research_interests":[{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering"},{"id":505,"name":"Condensed Matter Physics","url":"https://www.academia.edu/Documents/in/Condensed_Matter_Physics"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":7333,"name":"Nuclear Magnetic Resonance","url":"https://www.academia.edu/Documents/in/Nuclear_Magnetic_Resonance"},{"id":17733,"name":"Nanotechnology","url":"https://www.academia.edu/Documents/in/Nanotechnology"},{"id":26327,"name":"Medicine","url":"https://www.academia.edu/Documents/in/Medicine"},{"id":27303,"name":"Fuel Cell","url":"https://www.academia.edu/Documents/in/Fuel_Cell"},{"id":83315,"name":"Diffusion","url":"https://www.academia.edu/Documents/in/Diffusion"},{"id":171569,"name":"Polymer Electrolyte","url":"https://www.academia.edu/Documents/in/Polymer_Electrolyte"},{"id":205994,"name":"Nafion","url":"https://www.academia.edu/Documents/in/Nafion"},{"id":234860,"name":"Steady state","url":"https://www.academia.edu/Documents/in/Steady_state"},{"id":893307,"name":"Water Transport","url":"https://www.academia.edu/Documents/in/Water_Transport"},{"id":1276642,"name":"Electrolyte","url":"https://www.academia.edu/Documents/in/Electrolyte"}],"urls":[{"id":30851798,"url":"http://stacks.iop.org/0953-8984/23/i=23/a=234108/pdf"}]}, dispatcherData: dispatcherData }); 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As a consequence, the design of a fuel cell without gas diffusion layers must take into account these limitations visualized by neutron radiography.","publication_date":{"day":null,"month":null,"year":2010,"errors":{}},"publication_name":"Electrochimica 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data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/100630989/A_novel_simplified_micro_PEFC_concept_employing_glassy_carbon_micro_structures"><img alt="Research paper thumbnail of A novel, simplified micro-PEFC concept employing glassy carbon micro-structures" class="work-thumbnail" src="https://attachments.academia-assets.com/101399071/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/100630989/A_novel_simplified_micro_PEFC_concept_employing_glassy_carbon_micro_structures">A novel, simplified micro-PEFC concept employing glassy carbon micro-structures</a></div><div class="wp-workCard_item"><span>Electrochemistry Communications</span><span>, 2007</span></div><div class="wp-workCard_item wp-workCard--actions"><span 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It consists only of three elements; two glassy carbon sheets with micro-structured flow fields and a catalyst-coated membrane. The micro-structures are prepared in a sequence of three processing steps, i.e. sputtering, laser ablation, and reactive ion etching. 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By the current state of scientific knowledge, universal modeling without high computing power of these complex apparatuses is not possible to a satisfactory degree. In this article, a one-dimensional model to describe the mass transfer during a physical extraction process in an ACC is presented. The model is based on solely geometrical data and operating conditions of the ACC, as well as physical properties of the components. Regarding the selection of physical properties, only physical properties that are easily accessible were used. With this model, mass transfer calculations are possible and therefore, the output concentrations can be predicted. Simulations of an ACC based on the model were done by creating and running a python code. 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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="100631008"><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/100631008/Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers"><img alt="Research paper thumbnail of Continuous Nanoprecipitation of Polycaprolactone in Additively Manufactured Micromixers" class="work-thumbnail" src="https://attachments.academia-assets.com/101399021/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/100631008/Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers">Continuous Nanoprecipitation of Polycaprolactone in Additively Manufactured Micromixers</a></div><div class="wp-workCard_item"><span>Polymers</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">The polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with b...</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 polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with biologically degradable polymers. Usually, a discontinuous or semi-continuous process is employed due to its low technical effort and the fact that the amount of dispersions needed in a laboratory is relatively small. However, the number of particles produced in this method is not enough to make this process economically feasible. Therefore, it is necessary to improve the productivity of the process and create a controllable and robust continuous process with the potential to control parameters, such as the particle size or surface properties. In this study, nanoparticles were formulated from polycaprolactone (PCL) in a continuous process using additively manufactured micromixers. The main goal was to be able to exert control on the particle parameters in terms of size and zeta potential. The results showed that particle size could be adjusted in the range of 130 to 465 nm by using differ...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="65acfb3e439e40413a323cc63b98c73f" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399021,"asset_id":100631008,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399021/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100631008"><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="100631008"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100631008; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100631008]").text(description); $(".js-view-count[data-work-id=100631008]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100631008; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100631008']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100631008, 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: "65acfb3e439e40413a323cc63b98c73f" } } $('.js-work-strip[data-work-id=100631008]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100631008,"title":"Continuous Nanoprecipitation of Polycaprolactone in Additively Manufactured Micromixers","translated_title":"","metadata":{"abstract":"The polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with biologically degradable polymers. 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The results showed that particle size could be adjusted in the range of 130 to 465 nm by using differ...","publisher":"MDPI AG","publication_name":"Polymers"},"translated_abstract":"The polymeric ouzo effect is an energy-efficient and robust method to create nanoparticles with biologically degradable polymers. Usually, a discontinuous or semi-continuous process is employed due to its low technical effort and the fact that the amount of dispersions needed in a laboratory is relatively small. However, the number of particles produced in this method is not enough to make this process economically feasible. Therefore, it is necessary to improve the productivity of the process and create a controllable and robust continuous process with the potential to control parameters, such as the particle size or surface properties. In this study, nanoparticles were formulated from polycaprolactone (PCL) in a continuous process using additively manufactured micromixers. The main goal was to be able to exert control on the particle parameters in terms of size and zeta potential. The results showed that particle size could be adjusted in the range of 130 to 465 nm by using differ...","internal_url":"https://www.academia.edu/100631008/Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers","translated_internal_url":"","created_at":"2023-04-23T08:35:46.381-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":101399021,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/101399021/thumbnails/1.jpg","file_name":"pdf.pdf","download_url":"https://www.academia.edu/attachments/101399021/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Continuous_Nanoprecipitation_of_Polycapr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/101399021/pdf-libre.pdf?1682280002=\u0026response-content-disposition=attachment%3B+filename%3DContinuous_Nanoprecipitation_of_Polycapr.pdf\u0026Expires=1732466740\u0026Signature=WFTf9FD6M8RgMp4s5E7Rxwr9ZUdV3BJnrSAyf7IHiKdr~3NSkMXwsl79zLKR6CP9fgWw1h66ofzSXYnfGGjCBRzkFJxxkYnBnR6jslgMqUQn6wh0-Gy9Z4fYBSHNQTKaEQh1PS179ypAE6UgTvfoKdv8rCqyLgxROrA59X~LyJBEH3b8p1QN3g~JrReXCEV2P2YXZ5BfxSRKrqvsVS9y6GHNkhWMtE65Zw0zG9Dj7EkBgn-72y6KJ0NYjRe-rMQzOprbcaMuT4~NPrRVfOO9unXKG2ztr9B53fGKrhnKWjuWWcu07H-78P8q9B3BGqmMSYjRlORppjqy0yDcbv5lEw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Continuous_Nanoprecipitation_of_Polycaprolactone_in_Additively_Manufactured_Micromixers","translated_slug":"","page_count":14,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[{"id":101399021,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/101399021/thumbnails/1.jpg","file_name":"pdf.pdf","download_url":"https://www.academia.edu/attachments/101399021/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Continuous_Nanoprecipitation_of_Polycapr.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/101399021/pdf-libre.pdf?1682280002=\u0026response-content-disposition=attachment%3B+filename%3DContinuous_Nanoprecipitation_of_Polycapr.pdf\u0026Expires=1732466740\u0026Signature=WFTf9FD6M8RgMp4s5E7Rxwr9ZUdV3BJnrSAyf7IHiKdr~3NSkMXwsl79zLKR6CP9fgWw1h66ofzSXYnfGGjCBRzkFJxxkYnBnR6jslgMqUQn6wh0-Gy9Z4fYBSHNQTKaEQh1PS179ypAE6UgTvfoKdv8rCqyLgxROrA59X~LyJBEH3b8p1QN3g~JrReXCEV2P2YXZ5BfxSRKrqvsVS9y6GHNkhWMtE65Zw0zG9Dj7EkBgn-72y6KJ0NYjRe-rMQzOprbcaMuT4~NPrRVfOO9unXKG2ztr9B53fGKrhnKWjuWWcu07H-78P8q9B3BGqmMSYjRlORppjqy0yDcbv5lEw__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":8950,"name":"Nanoparticle","url":"https://www.academia.edu/Documents/in/Nanoparticle"},{"id":21466,"name":"Polymers","url":"https://www.academia.edu/Documents/in/Polymers"},{"id":26327,"name":"Medicine","url":"https://www.academia.edu/Documents/in/Medicine"},{"id":177878,"name":"Polycaprolactone","url":"https://www.academia.edu/Documents/in/Polycaprolactone"},{"id":390245,"name":"Particle Size","url":"https://www.academia.edu/Documents/in/Particle_Size"},{"id":983062,"name":"Zeta Potential","url":"https://www.academia.edu/Documents/in/Zeta_Potential"}],"urls":[{"id":30851811,"url":"https://www.mdpi.com/2073-4360/14/8/1509/pdf"}]}, 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="100631007"><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/100631007/Prediction_of_Excess_Enthalpy_Using_Volume_Translated_Peng_Robinson_Equation_of_State"><img alt="Research paper thumbnail of Prediction of Excess Enthalpy Using Volume-Translated Peng–Robinson Equation of State" class="work-thumbnail" src="https://attachments.academia-assets.com/101399060/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/100631007/Prediction_of_Excess_Enthalpy_Using_Volume_Translated_Peng_Robinson_Equation_of_State">Prediction of Excess Enthalpy Using Volume-Translated Peng–Robinson Equation of State</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In this work volume-translated Peng–Robinson group contribution equation of state was used to cal...</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 work volume-translated Peng–Robinson group contribution equation of state was used to calculate excess enthalpies. Four model systems were selected with the purpose to compare experimental and predicted enthalpy values at different temperatures. After the calculations were performed in Matlab software, results were verified with free software tool of Dortmunder Datenbank (DDB). In a next step, the mixing process and interaction forces were described on the basis of the sign and course of enthalpy values. The endothermic behavior of three systems could be well predicted, while for the most polar system, predictions were less precise. Furthermore, the discrepancy between experimental data from the literature and predicted values was discussed to evaluate the accuracy of the selected model. Lowest mean deviations (&lt;75 J/mol and &lt;15% at all temperatures) could be stated for alkane/benzene mixtures, while highest deviations could be again observed for the most polar mixture...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="be20ae17d21c8d7caac92a94eff80d5c" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399060,"asset_id":100631007,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399060/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100631007"><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="100631007"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100631007; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100631007]").text(description); $(".js-view-count[data-work-id=100631007]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100631007; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100631007']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100631007, 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: "be20ae17d21c8d7caac92a94eff80d5c" } } $('.js-work-strip[data-work-id=100631007]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100631007,"title":"Prediction of Excess Enthalpy Using Volume-Translated Peng–Robinson Equation of State","translated_title":"","metadata":{"abstract":"In this work volume-translated Peng–Robinson group contribution equation of state was used to calculate excess enthalpies. Four model systems were selected with the purpose to compare experimental and predicted enthalpy values at different temperatures. After the calculations were performed in Matlab software, results were verified with free software tool of Dortmunder Datenbank (DDB). In a next step, the mixing process and interaction forces were described on the basis of the sign and course of enthalpy values. The endothermic behavior of three systems could be well predicted, while for the most polar system, predictions were less precise. Furthermore, the discrepancy between experimental data from the literature and predicted values was discussed to evaluate the accuracy of the selected model. Lowest mean deviations (\u0026lt;75 J/mol and \u0026lt;15% at all temperatures) could be stated for alkane/benzene mixtures, while highest deviations could be again observed for the most polar mixture...","publication_date":{"day":null,"month":null,"year":2021,"errors":{}}},"translated_abstract":"In this work volume-translated Peng–Robinson group contribution equation of state was used to calculate excess enthalpies. Four model systems were selected with the purpose to compare experimental and predicted enthalpy values at different temperatures. After the calculations were performed in Matlab software, results were verified with free software tool of Dortmunder Datenbank (DDB). In a next step, the mixing process and interaction forces were described on the basis of the sign and course of enthalpy values. The endothermic behavior of three systems could be well predicted, while for the most polar system, predictions were less precise. Furthermore, the discrepancy between experimental data from the literature and predicted values was discussed to evaluate the accuracy of the selected model. Lowest mean deviations (\u0026lt;75 J/mol and \u0026lt;15% at all temperatures) could be stated for alkane/benzene mixtures, while highest deviations could be again observed for the most polar mixture...","internal_url":"https://www.academia.edu/100631007/Prediction_of_Excess_Enthalpy_Using_Volume_Translated_Peng_Robinson_Equation_of_State","translated_internal_url":"","created_at":"2023-04-23T08:35:46.290-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":101399060,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/101399060/thumbnails/1.jpg","file_name":"ChemEngineering-05-00008.pdf","download_url":"https://www.academia.edu/attachments/101399060/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Prediction_of_Excess_Enthalpy_Using_Volu.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/101399060/ChemEngineering-05-00008-libre.pdf?1682280009=\u0026response-content-disposition=attachment%3B+filename%3DPrediction_of_Excess_Enthalpy_Using_Volu.pdf\u0026Expires=1732466740\u0026Signature=f3kwDJqNLGEej-8r2V9ObGdb95nnUO-WkRfXBHoHP2taVB9-9~XRZinZOT9m1nPjz~TscZZ~uMp6yoyrOTDQIoludyaLlIvLisni8QSgEo7BMAjzERm3k0UqajWbhZV013rYP25bAlvFHj3o-h5jz7fZPlzvfiXwPRfed6X9vRWYnM6FmU4moCJ81eaXzNE9MnzkWTy-Tjz7ZLFl32RTAHZ8yAKZw-xteuAQbp-2urLyfmCNrZ-hBQTY7dVEm3ycAC8Bq5GxD5fbytu7gfAk2iZyEYIKenlEnnCwfwbR~qDSvtHNF4kQoUP9shcxVkRunMRqShfMeUrkA9qjXXUbZQ__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Prediction_of_Excess_Enthalpy_Using_Volume_Translated_Peng_Robinson_Equation_of_State","translated_slug":"","page_count":14,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[{"id":101399060,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/101399060/thumbnails/1.jpg","file_name":"ChemEngineering-05-00008.pdf","download_url":"https://www.academia.edu/attachments/101399060/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Prediction_of_Excess_Enthalpy_Using_Volu.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/101399060/ChemEngineering-05-00008-libre.pdf?1682280009=\u0026response-content-disposition=attachment%3B+filename%3DPrediction_of_Excess_Enthalpy_Using_Volu.pdf\u0026Expires=1732466740\u0026Signature=f3kwDJqNLGEej-8r2V9ObGdb95nnUO-WkRfXBHoHP2taVB9-9~XRZinZOT9m1nPjz~TscZZ~uMp6yoyrOTDQIoludyaLlIvLisni8QSgEo7BMAjzERm3k0UqajWbhZV013rYP25bAlvFHj3o-h5jz7fZPlzvfiXwPRfed6X9vRWYnM6FmU4moCJ81eaXzNE9MnzkWTy-Tjz7ZLFl32RTAHZ8yAKZw-xteuAQbp-2urLyfmCNrZ-hBQTY7dVEm3ycAC8Bq5GxD5fbytu7gfAk2iZyEYIKenlEnnCwfwbR~qDSvtHNF4kQoUP9shcxVkRunMRqShfMeUrkA9qjXXUbZQ__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":300,"name":"Mathematics","url":"https://www.academia.edu/Documents/in/Mathematics"},{"id":522,"name":"Thermodynamics","url":"https://www.academia.edu/Documents/in/Thermodynamics"},{"id":114712,"name":"Enthalpy","url":"https://www.academia.edu/Documents/in/Enthalpy"},{"id":1320599,"name":"Equation of State","url":"https://www.academia.edu/Documents/in/Equation_of_State"}],"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="100631005"><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/100631005/A_method_of_operating_a_fuel_cell_system_and_fuel_cell_system"><img alt="Research paper thumbnail of A method of operating a fuel cell system and fuel cell system" 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/100631005/A_method_of_operating_a_fuel_cell_system_and_fuel_cell_system">A method of operating a fuel cell system and fuel cell system</a></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In a method for operating a fuel cell system with at least one fuel cell (12), a reformer (20) 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 a method for operating a fuel cell system with at least one fuel cell (12), a reformer (20) for generating hydrogen-containing gas and the fuel cell (12) downstream of the burner (26) in a deviating from the normal operating state, the fuel cell (12 ) purged with a substantially inert gases consisting of gas flow. 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The exhaust gas of the fuel cell (12) is reacted in the burner (26) substantially in inert gases, and that from the burner (26) exit gas stream is passed through an exhaust gas recirculation for flushing by the fuel cell (12).","internal_url":"https://www.academia.edu/100631005/A_method_of_operating_a_fuel_cell_system_and_fuel_cell_system","translated_internal_url":"","created_at":"2023-04-23T08:35:46.214-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"A_method_of_operating_a_fuel_cell_system_and_fuel_cell_system","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[],"research_interests":[{"id":402,"name":"Environmental Science","url":"https://www.academia.edu/Documents/in/Environmental_Science"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="100631003"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/100631003/PlantDesign_Prototypical_implementation_of_an_integrated_engineering_tool"><img alt="Research paper thumbnail of PlantDesign - Prototypical implementation of an integrated engineering tool" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/100631003/PlantDesign_Prototypical_implementation_of_an_integrated_engineering_tool">PlantDesign - Prototypical implementation of an integrated engineering tool</a></div><div class="wp-workCard_item"><span>Computers &amp; Chemical Engineering</span><span>, 2021</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="100631003"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="100631003"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100631003; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100631003]").text(description); 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$(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="100631000"><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/100631000/Investigation_of_Contact_Angles_and_Surface_Morphology_of_3D_Printed_Materials"><img alt="Research paper thumbnail of Investigation of Contact Angles and Surface Morphology of 3D-Printed Materials" class="work-thumbnail" src="https://attachments.academia-assets.com/101399059/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/100631000/Investigation_of_Contact_Angles_and_Surface_Morphology_of_3D_Printed_Materials">Investigation of Contact Angles and Surface Morphology of 3D-Printed Materials</a></div><div class="wp-workCard_item"><span>Industrial &amp; Engineering Chemistry Research</span><span>, 2020</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="5f24d585f5d8d3c076da1643860d5ffa" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399059,"asset_id":100631000,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399059/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100631000"><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="100631000"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100631000; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100631000]").text(description); $(".js-view-count[data-work-id=100631000]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100631000; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100631000']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100631000, 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="100630997"><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/100630997/Extraction_Centrifuges_Intensified_Equipment_Facilitating_Modular_and_Flexible_Plant_Concepts"><img alt="Research paper thumbnail of Extraction Centrifuges—Intensified Equipment Facilitating Modular and Flexible Plant Concepts" class="work-thumbnail" src="https://attachments.academia-assets.com/101399020/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/100630997/Extraction_Centrifuges_Intensified_Equipment_Facilitating_Modular_and_Flexible_Plant_Concepts">Extraction Centrifuges—Intensified Equipment Facilitating Modular and Flexible Plant Concepts</a></div><div class="wp-workCard_item"><span>ChemEngineering</span><span>, 2019</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">In recent years, modularization of chemical production plants has become a widely discussed trend...</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, modularization of chemical production plants has become a widely discussed trend to overcome some of key issues the chemical industry struggles with. High volatility in raw material and customer markets, shorter product life cycles, cost pressure and increasing competition are just a few of them. Modularization of chemical production offers the opportunity to deal with these issues. The unit operations, which are capable to be applied in modular plant concepts, are subject of on-going research. On the reaction side, tubular continuous flow reactors are typical assets and methods for design and operation are available on a high technical level. Separation units on the downstream side are not yet developed to technical maturity. This paper focuses on extraction centrifuges, which are promising devices due to their large range of application, small volumes, high separation efficiency and excellent scalability. Industrial examples show the performance of extraction cent...</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="b45259eec1c22e1fa5ae644c72754602" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399020,"asset_id":100630997,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399020/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100630997"><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="100630997"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630997; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630997]").text(description); $(".js-view-count[data-work-id=100630997]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630997; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630997']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630997, 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: "b45259eec1c22e1fa5ae644c72754602" } } $('.js-work-strip[data-work-id=100630997]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630997,"title":"Extraction Centrifuges—Intensified Equipment Facilitating Modular and Flexible Plant Concepts","translated_title":"","metadata":{"abstract":"In recent years, modularization of chemical production plants has become a widely discussed trend to overcome some of key issues the chemical industry struggles with. High volatility in raw material and customer markets, shorter product life cycles, cost pressure and increasing competition are just a few of them. Modularization of chemical production offers the opportunity to deal with these issues. The unit operations, which are capable to be applied in modular plant concepts, are subject of on-going research. On the reaction side, tubular continuous flow reactors are typical assets and methods for design and operation are available on a high technical level. Separation units on the downstream side are not yet developed to technical maturity. This paper focuses on extraction centrifuges, which are promising devices due to their large range of application, small volumes, high separation efficiency and excellent scalability. Industrial examples show the performance of extraction cent...","publisher":"MDPI AG","publication_date":{"day":null,"month":null,"year":2019,"errors":{}},"publication_name":"ChemEngineering"},"translated_abstract":"In recent years, modularization of chemical production plants has become a widely discussed trend to overcome some of key issues the chemical industry struggles with. High volatility in raw material and customer markets, shorter product life cycles, cost pressure and increasing competition are just a few of them. Modularization of chemical production offers the opportunity to deal with these issues. The unit operations, which are capable to be applied in modular plant concepts, are subject of on-going research. On the reaction side, tubular continuous flow reactors are typical assets and methods for design and operation are available on a high technical level. Separation units on the downstream side are not yet developed to technical maturity. This paper focuses on extraction centrifuges, which are promising devices due to their large range of application, small volumes, high separation efficiency and excellent scalability. 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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="100630995"><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/100630995/Reducing_Time_to_Market_by_Innovative_Development_and_Production_Strategies"><img alt="Research paper thumbnail of Reducing Time to Market by Innovative Development and Production Strategies" class="work-thumbnail" src="https://attachments.academia-assets.com/101399079/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/100630995/Reducing_Time_to_Market_by_Innovative_Development_and_Production_Strategies">Reducing Time to Market by Innovative Development and Production Strategies</a></div><div class="wp-workCard_item"><span>Chemical Engineering &amp; Technology</span><span>, 2016</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="8bc50e86fa9380da3f095f902e5165f8" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399079,"asset_id":100630995,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399079/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100630995"><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="100630995"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630995; 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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="100630992"><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/100630992/2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures"><img alt="Research paper thumbnail of 2+1D modelling of a polymer electrolyte fuel cell with glassy-carbon microstructures" 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/100630992/2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures">2+1D modelling of a polymer electrolyte fuel cell with glassy-carbon microstructures</a></div><div class="wp-workCard_item"><span>Mathematical and Computer Modelling of Dynamical Systems</span><span>, 2012</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">ABSTRACT A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented...</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 A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented, based on a 2+1D FEM modelling approach. This approach is suitable to take the high aspect ratio between the in-plane and the through-plane dimensions of fuel cells into account, and to avoid expensive 3D calculations. The anode and cathode are described by 2D transport models. The coupling between the anode and cathode side is established by a nonlinear point-to-point 1D model representing the membrane electrode assembly (MEA). This 1D boundary value problem is formulated using the computer algebra software Mathematica. The approach is based on the symbolic weak form expressions of a nonlinear system of PDEs. The integrands of the tangential element stiffness matrix and the element residual vector of the coupled FEM problem are computed analytically. These integrands are converted to C code automatically. The model is applied to simulate a micro PEFC without gas diffusion layers (GDLs). The simulations reveal an inhomogeneous in-plane electric current density. Further, neutron radiography data obtained with the micro fuel cell is compared to the calculated water flux between the 1D MEA model and the 2D domains. The model is used to explain the locations where water condensation is found.</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="100630992"><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="100630992"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630992; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630992]").text(description); $(".js-view-count[data-work-id=100630992]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630992; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630992']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630992, 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" } } $('.js-work-strip[data-work-id=100630992]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630992,"title":"2+1D modelling of a polymer electrolyte fuel cell with glassy-carbon microstructures","translated_title":"","metadata":{"abstract":"ABSTRACT A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented, based on a 2+1D FEM modelling approach. 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Further, neutron radiography data obtained with the micro fuel cell is compared to the calculated water flux between the 1D MEA model and the 2D domains. The model is used to explain the locations where water condensation is found.","publisher":"Informa UK Limited","publication_date":{"day":null,"month":null,"year":2012,"errors":{}},"publication_name":"Mathematical and Computer Modelling of Dynamical Systems"},"translated_abstract":"ABSTRACT A computationally efficient model of a polymer electrolyte fuel cell (PEFC) is presented, based on a 2+1D FEM modelling approach. This approach is suitable to take the high aspect ratio between the in-plane and the through-plane dimensions of fuel cells into account, and to avoid expensive 3D calculations. The anode and cathode are described by 2D transport models. The coupling between the anode and cathode side is established by a nonlinear point-to-point 1D model representing the membrane electrode assembly (MEA). This 1D boundary value problem is formulated using the computer algebra software Mathematica. The approach is based on the symbolic weak form expressions of a nonlinear system of PDEs. The integrands of the tangential element stiffness matrix and the element residual vector of the coupled FEM problem are computed analytically. These integrands are converted to C code automatically. The model is applied to simulate a micro PEFC without gas diffusion layers (GDLs). The simulations reveal an inhomogeneous in-plane electric current density. Further, neutron radiography data obtained with the micro fuel cell is compared to the calculated water flux between the 1D MEA model and the 2D domains. The model is used to explain the locations where water condensation is found.","internal_url":"https://www.academia.edu/100630992/2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures","translated_internal_url":"","created_at":"2023-04-23T08:35:45.299-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"2_1D_modelling_of_a_polymer_electrolyte_fuel_cell_with_glassy_carbon_microstructures","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[],"research_interests":[{"id":237,"name":"Cognitive Science","url":"https://www.academia.edu/Documents/in/Cognitive_Science"},{"id":511,"name":"Materials Science","url":"https://www.academia.edu/Documents/in/Materials_Science"},{"id":2161,"name":"Microstructure","url":"https://www.academia.edu/Documents/in/Microstructure"},{"id":7477,"name":"Fuel Cells","url":"https://www.academia.edu/Documents/in/Fuel_Cells"},{"id":58527,"name":"Polymer","url":"https://www.academia.edu/Documents/in/Polymer"},{"id":173959,"name":"Current Density","url":"https://www.academia.edu/Documents/in/Current_Density"},{"id":201678,"name":"Computer Algebra","url":"https://www.academia.edu/Documents/in/Computer_Algebra"},{"id":352783,"name":"Glassy Carbon","url":"https://www.academia.edu/Documents/in/Glassy_Carbon"},{"id":473797,"name":"Microstructures","url":"https://www.academia.edu/Documents/in/Microstructures"},{"id":506858,"name":"Nonlinear system","url":"https://www.academia.edu/Documents/in/Nonlinear_system"},{"id":863497,"name":"Carbon Fibers","url":"https://www.academia.edu/Documents/in/Carbon_Fibers"},{"id":939537,"name":"Boundary Value Problem","url":"https://www.academia.edu/Documents/in/Boundary_Value_Problem"},{"id":1214993,"name":"Neutron Radiography","url":"https://www.academia.edu/Documents/in/Neutron_Radiography"},{"id":1276642,"name":"Electrolyte","url":"https://www.academia.edu/Documents/in/Electrolyte"},{"id":2742746,"name":"High aspect ratio","url":"https://www.academia.edu/Documents/in/High_aspect_ratio"}],"urls":[{"id":30851799,"url":"http://www.tandfonline.com/doi/pdf/10.1080/13873954.2011.642390"}]}, 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="100630991"><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/100630991/Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties"><img alt="Research paper thumbnail of Using2H labeling with neutron radiography for the study of solid polymer electrolyte water transport properties" 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/100630991/Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties">Using2H labeling with neutron radiography for the study of solid polymer electrolyte water transport properties</a></div><div class="wp-workCard_item"><span>Journal of Physics: Condensed Matter</span><span>, 2011</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neu...</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">A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neutron imaging for the analysis of transport parameters in the bulk and at the interfaces of Nafion polymer electrolyte membranes is proposed. The use of different isotope compositions in the steady state allows evaluation of the relation between bulk and interface transport parameters, but relies on literature data for evaluating absolute values. By using transients of isotope composition, absolute values of these parameters including the self-diffusion coefficient of H can be extracted, making this method an attractive alternative to self-diffusion measurements using nuclear magnetic resonance (NMR), allowing measurements in precisely controlled conditions in real fuel cell structures. First measurements were realized on samples with and without electrodes and we report values of the self-diffusion coefficient of the same order of magnitude as values measured using NMR, although with slightly higher numbers. In our particular case, lower interfacial exchange rates for water transport were observed for samples with an electrode.</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="100630991"><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="100630991"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630991; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630991]").text(description); $(".js-view-count[data-work-id=100630991]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630991; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630991']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630991, 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" } } $('.js-work-strip[data-work-id=100630991]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630991,"title":"Using2H labeling with neutron radiography for the study of solid polymer electrolyte water transport properties","translated_title":"","metadata":{"abstract":"A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neutron imaging for the analysis of transport parameters in the bulk and at the interfaces of Nafion polymer electrolyte membranes is proposed. The use of different isotope compositions in the steady state allows evaluation of the relation between bulk and interface transport parameters, but relies on literature data for evaluating absolute values. By using transients of isotope composition, absolute values of these parameters including the self-diffusion coefficient of H can be extracted, making this method an attractive alternative to self-diffusion measurements using nuclear magnetic resonance (NMR), allowing measurements in precisely controlled conditions in real fuel cell structures. First measurements were realized on samples with and without electrodes and we report values of the self-diffusion coefficient of the same order of magnitude as values measured using NMR, although with slightly higher numbers. In our particular case, lower interfacial exchange rates for water transport were observed for samples with an electrode.","publisher":"IOP Publishing","publication_date":{"day":null,"month":null,"year":2011,"errors":{}},"publication_name":"Journal of Physics: Condensed Matter"},"translated_abstract":"A method combining (2)H labeling of different sources of H atoms (hydrogen, water vapor) with neutron imaging for the analysis of transport parameters in the bulk and at the interfaces of Nafion polymer electrolyte membranes is proposed. The use of different isotope compositions in the steady state allows evaluation of the relation between bulk and interface transport parameters, but relies on literature data for evaluating absolute values. By using transients of isotope composition, absolute values of these parameters including the self-diffusion coefficient of H can be extracted, making this method an attractive alternative to self-diffusion measurements using nuclear magnetic resonance (NMR), allowing measurements in precisely controlled conditions in real fuel cell structures. First measurements were realized on samples with and without electrodes and we report values of the self-diffusion coefficient of the same order of magnitude as values measured using NMR, although with slightly higher numbers. In our particular case, lower interfacial exchange rates for water transport were observed for samples with an electrode.","internal_url":"https://www.academia.edu/100630991/Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties","translated_internal_url":"","created_at":"2023-04-23T08:35:45.146-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[],"slug":"Using2H_labeling_with_neutron_radiography_for_the_study_of_solid_polymer_electrolyte_water_transport_properties","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard Seyfang","url":"https://independent.academia.edu/BernhardSeyfang"},"attachments":[],"research_interests":[{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering"},{"id":505,"name":"Condensed Matter Physics","url":"https://www.academia.edu/Documents/in/Condensed_Matter_Physics"},{"id":523,"name":"Chemistry","url":"https://www.academia.edu/Documents/in/Chemistry"},{"id":7333,"name":"Nuclear Magnetic Resonance","url":"https://www.academia.edu/Documents/in/Nuclear_Magnetic_Resonance"},{"id":17733,"name":"Nanotechnology","url":"https://www.academia.edu/Documents/in/Nanotechnology"},{"id":26327,"name":"Medicine","url":"https://www.academia.edu/Documents/in/Medicine"},{"id":27303,"name":"Fuel Cell","url":"https://www.academia.edu/Documents/in/Fuel_Cell"},{"id":83315,"name":"Diffusion","url":"https://www.academia.edu/Documents/in/Diffusion"},{"id":171569,"name":"Polymer Electrolyte","url":"https://www.academia.edu/Documents/in/Polymer_Electrolyte"},{"id":205994,"name":"Nafion","url":"https://www.academia.edu/Documents/in/Nafion"},{"id":234860,"name":"Steady state","url":"https://www.academia.edu/Documents/in/Steady_state"},{"id":893307,"name":"Water Transport","url":"https://www.academia.edu/Documents/in/Water_Transport"},{"id":1276642,"name":"Electrolyte","url":"https://www.academia.edu/Documents/in/Electrolyte"}],"urls":[{"id":30851798,"url":"http://stacks.iop.org/0953-8984/23/i=23/a=234108/pdf"}]}, 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="100630990"><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/100630990/Identification_of_liquid_water_constraints_in_micro_polymer_electrolyte_fuel_cells_without_gas_diffusion_layers"><img alt="Research paper thumbnail of Identification of liquid water constraints in micro polymer electrolyte fuel cells without gas diffusion layers" class="work-thumbnail" src="https://attachments.academia-assets.com/101399070/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/100630990/Identification_of_liquid_water_constraints_in_micro_polymer_electrolyte_fuel_cells_without_gas_diffusion_layers">Identification of liquid water constraints in micro polymer electrolyte fuel cells without gas diffusion layers</a></div><div class="wp-workCard_item"><span>Electrochimica Acta</span><span>, 2010</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="73ee759c56581cf873d2fd1ce2c25c55" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":101399070,"asset_id":100630990,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/101399070/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&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="100630990"><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="100630990"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630990; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630990]").text(description); $(".js-view-count[data-work-id=100630990]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630990; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630990']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630990, 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: "73ee759c56581cf873d2fd1ce2c25c55" } } $('.js-work-strip[data-work-id=100630990]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630990,"title":"Identification of liquid water constraints in micro polymer electrolyte fuel cells without gas diffusion layers","translated_title":"","metadata":{"publisher":"Elsevier BV","grobid_abstract":"A simplified, miniaturized polymer electrolyte fuel cell without gas diffusion layers was investigated under operation by neutron radiography. By visualizing liquid water, it was possible to identify limiting effects, which are directly related to the simplified construction principle. Depending on the operation conditions, undesired water accumulation either in particular micro-channels or on the cathode catalyst layer as well as drying of the anode catalyst layer was observed. As a consequence, the design of a fuel cell without gas diffusion layers must take into account these limitations visualized by neutron radiography.","publication_date":{"day":null,"month":null,"year":2010,"errors":{}},"publication_name":"Electrochimica Acta","grobid_abstract_attachment_id":101399070},"translated_abstract":null,"internal_url":"https://www.academia.edu/100630990/Identification_of_liquid_water_constraints_in_micro_polymer_electrolyte_fuel_cells_without_gas_diffusion_layers","translated_internal_url":"","created_at":"2023-04-23T08:35:45.019-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":266870439,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[],"downloadable_attachments":[{"id":101399070,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/101399070/thumbnails/1.jpg","file_name":"j.electacta.2009.12.06120230423-1-w4lajt.pdf","download_url":"https://www.academia.edu/attachments/101399070/download_file?st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&st=MTczMjQ2MzE0MCw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"Identification_of_liquid_water_constrain.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/101399070/j.electacta.2009.12.06120230423-1-w4lajt-libre.pdf?1682279992=\u0026response-content-disposition=attachment%3B+filename%3DIdentification_of_liquid_water_constrain.pdf\u0026Expires=1732466740\u0026Signature=DyussVTsGfH3L1E7-QIkm6D06t5mehrLMTvfJyxEeW-pQzNGNPgoz79ygHy6EJXJR4b3HSt-HtHveV4Z1LRpQKRtt5ee~sXbkkIcWNBI7Y0O5RGFWkOJxXdXyaOmmLlQkYlx23JlFVep3tzzoqo7C9hSqC3NJuWrPfkl~7~EYk1ExAU3j7DgxBI2icXlwJccs02mtJkjBdBaI7d~qfvjiHQJkub9pkPHUPyt2Byl7pVYcawjXTqQFo2RglPTIC8BS84YuAZA7iRNtB1grNXc4SboRc6hLlpLCsDwW7P7QszKfwE2cGf-Yc2MU7tw91OovRTgGOGkPWUlkseTjsk~RQ__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"Identification_of_liquid_water_constraints_in_micro_polymer_electrolyte_fuel_cells_without_gas_diffusion_layers","translated_slug":"","page_count":7,"language":"en","content_type":"Work","owner":{"id":266870439,"first_name":"Bernhard","middle_initials":null,"last_name":"Seyfang","page_name":"BernhardSeyfang","domain_name":"independent","created_at":"2023-04-23T08:34:14.221-07:00","display_name":"Bernhard 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Cell","url":"https://www.academia.edu/Documents/in/Fuel_Cell"},{"id":58527,"name":"Polymer","url":"https://www.academia.edu/Documents/in/Polymer"},{"id":81605,"name":"Neutron Imaging","url":"https://www.academia.edu/Documents/in/Neutron_Imaging"},{"id":83315,"name":"Diffusion","url":"https://www.academia.edu/Documents/in/Diffusion"},{"id":118582,"name":"Physical sciences","url":"https://www.academia.edu/Documents/in/Physical_sciences"},{"id":173959,"name":"Current Density","url":"https://www.academia.edu/Documents/in/Current_Density"},{"id":260118,"name":"CHEMICAL SCIENCES","url":"https://www.academia.edu/Documents/in/CHEMICAL_SCIENCES"},{"id":352783,"name":"Glassy Carbon","url":"https://www.academia.edu/Documents/in/Glassy_Carbon"},{"id":477865,"name":"Operant 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data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/100630989/A_novel_simplified_micro_PEFC_concept_employing_glassy_carbon_micro_structures"><img alt="Research paper thumbnail of A novel, simplified micro-PEFC concept employing glassy carbon micro-structures" class="work-thumbnail" src="https://attachments.academia-assets.com/101399071/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/100630989/A_novel_simplified_micro_PEFC_concept_employing_glassy_carbon_micro_structures">A novel, simplified micro-PEFC concept employing glassy carbon micro-structures</a></div><div class="wp-workCard_item"><span>Electrochemistry Communications</span><span>, 2007</span></div><div class="wp-workCard_item wp-workCard--actions"><span 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href="https://www.academia.edu/100630988/In_situ_observation_of_the_water_distribution_across_a_PEFC_using_high_resolution_neutron_radiography">In situ observation of the water distribution across a PEFC using high resolution neutron radiography</a></div><div class="wp-workCard_item"><span>Electrochemistry Communications</span><span>, 2008</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">... The technical support from Christian-André Marmy and Marcel Hottiger as well as the financial...</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 technical support from Christian-André Marmy and Marcel Hottiger as well as the financial support from the Swiss Federal Office of Energy (BFE) are gratefully acknowledged. References. [1] AB Geiger, A. Tsukada, E. Lehmann, P. Vontobel, A. Wokaun and GG Scherer ...</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="100630988"><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="100630988"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 100630988; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=100630988]").text(description); $(".js-view-count[data-work-id=100630988]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 100630988; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='100630988']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 100630988, 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" } } $('.js-work-strip[data-work-id=100630988]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":100630988,"title":"In situ observation of the water distribution across a PEFC using high resolution neutron radiography","translated_title":"","metadata":{"abstract":"... The technical support from Christian-André Marmy and Marcel Hottiger as well as the financial support from the Swiss Federal Office of Energy (BFE) are gratefully acknowledged. References. [1] AB Geiger, A. Tsukada, E. Lehmann, P. Vontobel, A. Wokaun and GG Scherer ...","publisher":"Elsevier BV","publication_date":{"day":null,"month":null,"year":2008,"errors":{}},"publication_name":"Electrochemistry Communications"},"translated_abstract":"... The technical support from Christian-André Marmy and Marcel Hottiger as well as the financial support from the Swiss Federal Office of Energy (BFE) are gratefully acknowledged. References. [1] AB Geiger, A. Tsukada, E. Lehmann, P. Vontobel, A. 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If used as a positiv...</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 spinel LiMn2O4 is a promising candidate for future battery applications. If used as a positive electrode in a battery, the charging capacity of such a battery element is limited by the formation of a solid electrolyte interphase like layer between the electrolyte and the spinel. 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