Analysis of Protein Adsorption to Ion Exchangers in a Finite Bath
Bovine serum albumin was used as a model for the study of protein adsorption. The effect of initial protein concentration on the nature of adsorption was examined by both finite bath experiments and computer simulations using 4 different rate models. Some equilibrium models were found to underestima...
Gespeichert in:
Veröffentlicht in: | Journal of chemical technology and biotechnology (1986) 1997-08, Vol.69 (4), p.405-414 |
---|---|
Hauptverfasser: | , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 414 |
---|---|
container_issue | 4 |
container_start_page | 405 |
container_title | Journal of chemical technology and biotechnology (1986) |
container_volume | 69 |
creator | Habbaba, Maamoun M. Ülgen, Kutlu Ö. |
description | Bovine serum albumin was used as a model for the study of protein adsorption. The effect of initial protein concentration on the nature of adsorption was examined by both finite bath experiments and computer simulations using 4 different rate models. Some equilibrium models were found to underestimate the adsorption parameters, the reaction rate constant and the effective pore diffusivity, as these models assumed that a single mechanism was governing the overall rate of adsorption. The adsorption process should be considered as a series of steps. In terms of interpretation of the experimental data, the most useful model is that which incorporates the mass transfer resistance, the diffusional restrictions of the protein into the interior of the adsorbent particles, and the interaction rate constant, into the overall adsorption mechanism. |
doi_str_mv | 10.1002/(SICI)1097-4660(199708)69:4<405::AID-JCTB729>3.0.CO;2-G |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_27244559</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>27244559</sourcerecordid><originalsourceid>FETCH-LOGICAL-c283t-b56b85286f0cb1a9a571a31874b6f0b3b67ba45af7bd25c7f036af5e8541634b3</originalsourceid><addsrcrecordid>eNo9kF1r1EAUhgdRcK3-h1yItBfZzvdMVlGyabtGqluwUvDmcCad2Klpss6k0P57s-yyVy-c85yXw0PIF0bnjFJ-evyzruoTRguTS63pMSsKQ-2JLhbyk6RqsSjrs_xbdb00vPgs5nRerT_yfPWCzA43L8mMcm1zrox6Td6kdE8p1ZbrGSnLHrvnFFI2tNlVHEYf-qy8TUPcjGHos3HI6inOn5o77P_4mLJpj9lF6MPosyWOd2_Jqxa75N_t84j8uji_rr7ml-tVXZWXecOtGHOntLOKW93SxjEsUBmGglkj3TRywmnjUCpsjbvlqjEtFRpb5a2STAvpxBH5sOvdxOHfo08jPITU-K7D3g-PCbjhUipVTODNDmzikFL0LWxieMD4DIzCVinAVils9cBWD-yUgi5AwqQUYFIKe6UggEK1Bg6rqfn9_gVMDXZtxL4J6VDPjWWcswnLd1hIo386rDH-BW2EUXDzYwVX339rS7WCpfgPPv2KrA</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>27244559</pqid></control><display><type>article</type><title>Analysis of Protein Adsorption to Ion Exchangers in a Finite Bath</title><source>Access via Wiley Online Library</source><creator>Habbaba, Maamoun M. ; Ülgen, Kutlu Ö.</creator><creatorcontrib>Habbaba, Maamoun M. ; Ülgen, Kutlu Ö.</creatorcontrib><description>Bovine serum albumin was used as a model for the study of protein adsorption. The effect of initial protein concentration on the nature of adsorption was examined by both finite bath experiments and computer simulations using 4 different rate models. Some equilibrium models were found to underestimate the adsorption parameters, the reaction rate constant and the effective pore diffusivity, as these models assumed that a single mechanism was governing the overall rate of adsorption. The adsorption process should be considered as a series of steps. In terms of interpretation of the experimental data, the most useful model is that which incorporates the mass transfer resistance, the diffusional restrictions of the protein into the interior of the adsorbent particles, and the interaction rate constant, into the overall adsorption mechanism.</description><identifier>ISSN: 0268-2575</identifier><identifier>EISSN: 1097-4660</identifier><identifier>DOI: 10.1002/(SICI)1097-4660(199708)69:4<405::AID-JCTB729>3.0.CO;2-G</identifier><identifier>CODEN: JCTBDC</identifier><language>eng</language><publisher>Chichester, UK: John Wiley & Sons, Ltd</publisher><subject>Biological and medical sciences ; Biotechnology ; computer simulation ; Fundamental and applied biological sciences. Psychology ; ion-exchange chromatography ; Methods. Procedures. Technologies ; Others ; process design ; protein purification ; Various methods and equipments</subject><ispartof>Journal of chemical technology and biotechnology (1986), 1997-08, Vol.69 (4), p.405-414</ispartof><rights>1997 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>315,781,785,27929,27930</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=2781221$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Habbaba, Maamoun M.</creatorcontrib><creatorcontrib>Ülgen, Kutlu Ö.</creatorcontrib><title>Analysis of Protein Adsorption to Ion Exchangers in a Finite Bath</title><title>Journal of chemical technology and biotechnology (1986)</title><addtitle>J. Chem. Technol. Biotechnol</addtitle><description>Bovine serum albumin was used as a model for the study of protein adsorption. The effect of initial protein concentration on the nature of adsorption was examined by both finite bath experiments and computer simulations using 4 different rate models. Some equilibrium models were found to underestimate the adsorption parameters, the reaction rate constant and the effective pore diffusivity, as these models assumed that a single mechanism was governing the overall rate of adsorption. The adsorption process should be considered as a series of steps. In terms of interpretation of the experimental data, the most useful model is that which incorporates the mass transfer resistance, the diffusional restrictions of the protein into the interior of the adsorbent particles, and the interaction rate constant, into the overall adsorption mechanism.</description><subject>Biological and medical sciences</subject><subject>Biotechnology</subject><subject>computer simulation</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>ion-exchange chromatography</subject><subject>Methods. Procedures. Technologies</subject><subject>Others</subject><subject>process design</subject><subject>protein purification</subject><subject>Various methods and equipments</subject><issn>0268-2575</issn><issn>1097-4660</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1997</creationdate><recordtype>article</recordtype><recordid>eNo9kF1r1EAUhgdRcK3-h1yItBfZzvdMVlGyabtGqluwUvDmcCad2Klpss6k0P57s-yyVy-c85yXw0PIF0bnjFJ-evyzruoTRguTS63pMSsKQ-2JLhbyk6RqsSjrs_xbdb00vPgs5nRerT_yfPWCzA43L8mMcm1zrox6Td6kdE8p1ZbrGSnLHrvnFFI2tNlVHEYf-qy8TUPcjGHos3HI6inOn5o77P_4mLJpj9lF6MPosyWOd2_Jqxa75N_t84j8uji_rr7ml-tVXZWXecOtGHOntLOKW93SxjEsUBmGglkj3TRywmnjUCpsjbvlqjEtFRpb5a2STAvpxBH5sOvdxOHfo08jPITU-K7D3g-PCbjhUipVTODNDmzikFL0LWxieMD4DIzCVinAVils9cBWD-yUgi5AwqQUYFIKe6UggEK1Bg6rqfn9_gVMDXZtxL4J6VDPjWWcswnLd1hIo386rDH-BW2EUXDzYwVX339rS7WCpfgPPv2KrA</recordid><startdate>199708</startdate><enddate>199708</enddate><creator>Habbaba, Maamoun M.</creator><creator>Ülgen, Kutlu Ö.</creator><general>John Wiley & Sons, Ltd</general><general>Wiley</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope></search><sort><creationdate>199708</creationdate><title>Analysis of Protein Adsorption to Ion Exchangers in a Finite Bath</title><author>Habbaba, Maamoun M. ; Ülgen, Kutlu Ö.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c283t-b56b85286f0cb1a9a571a31874b6f0b3b67ba45af7bd25c7f036af5e8541634b3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1997</creationdate><topic>Biological and medical sciences</topic><topic>Biotechnology</topic><topic>computer simulation</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>ion-exchange chromatography</topic><topic>Methods. Procedures. Technologies</topic><topic>Others</topic><topic>process design</topic><topic>protein purification</topic><topic>Various methods and equipments</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Habbaba, Maamoun M.</creatorcontrib><creatorcontrib>Ülgen, Kutlu Ö.</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><jtitle>Journal of chemical technology and biotechnology (1986)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Habbaba, Maamoun M.</au><au>Ülgen, Kutlu Ö.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Analysis of Protein Adsorption to Ion Exchangers in a Finite Bath</atitle><jtitle>Journal of chemical technology and biotechnology (1986)</jtitle><addtitle>J. Chem. Technol. Biotechnol</addtitle><date>1997-08</date><risdate>1997</risdate><volume>69</volume><issue>4</issue><spage>405</spage><epage>414</epage><pages>405-414</pages><issn>0268-2575</issn><eissn>1097-4660</eissn><coden>JCTBDC</coden><abstract>Bovine serum albumin was used as a model for the study of protein adsorption. The effect of initial protein concentration on the nature of adsorption was examined by both finite bath experiments and computer simulations using 4 different rate models. Some equilibrium models were found to underestimate the adsorption parameters, the reaction rate constant and the effective pore diffusivity, as these models assumed that a single mechanism was governing the overall rate of adsorption. The adsorption process should be considered as a series of steps. In terms of interpretation of the experimental data, the most useful model is that which incorporates the mass transfer resistance, the diffusional restrictions of the protein into the interior of the adsorbent particles, and the interaction rate constant, into the overall adsorption mechanism.</abstract><cop>Chichester, UK</cop><pub>John Wiley & Sons, Ltd</pub><doi>10.1002/(SICI)1097-4660(199708)69:4<405::AID-JCTB729>3.0.CO;2-G</doi><tpages>10</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0268-2575 |
ispartof | Journal of chemical technology and biotechnology (1986), 1997-08, Vol.69 (4), p.405-414 |
issn | 0268-2575 1097-4660 |
language | eng |
recordid | cdi_proquest_miscellaneous_27244559 |
source | Access via Wiley Online Library |
subjects | Biological and medical sciences Biotechnology computer simulation Fundamental and applied biological sciences. Psychology ion-exchange chromatography Methods. Procedures. Technologies Others process design protein purification Various methods and equipments |
title | Analysis of Protein Adsorption to Ion Exchangers in a Finite Bath |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-11T22%3A03%3A02IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Analysis%20of%20Protein%20Adsorption%20to%20Ion%20Exchangers%20in%20a%20Finite%20Bath&rft.jtitle=Journal%20of%20chemical%20technology%20and%20biotechnology%20(1986)&rft.au=Habbaba,%20Maamoun%20M.&rft.date=1997-08&rft.volume=69&rft.issue=4&rft.spage=405&rft.epage=414&rft.pages=405-414&rft.issn=0268-2575&rft.eissn=1097-4660&rft.coden=JCTBDC&rft_id=info:doi/10.1002/(SICI)1097-4660(199708)69:4%3C405::AID-JCTB729%3E3.0.CO;2-G&rft_dat=%3Cproquest_cross%3E27244559%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=27244559&rft_id=info:pmid/&rfr_iscdi=true |