Refolding of proteins in a CSTR
A model to predict refolding of proteins in a continuous stirred tank reactor (CSTR) was developed and compared to a batch refolding process with simple dilution of the protein in a stirred tank reactor. For experimental verification of the model a continuous refolding of a model protein ( α -lactal...
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Veröffentlicht in: | Chemical engineering science 2005-11, Vol.60 (21), p.5770-5780 |
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creator | Schlegl, Robert Tscheliessnig, Anne Necina, Roman Wandl, Robert Jungbauer, Alois |
description | A model to predict refolding of proteins in a continuous stirred tank reactor (CSTR) was developed and compared to a batch refolding process with simple dilution of the protein in a stirred tank reactor. For experimental verification of the model a continuous refolding of a model protein (
α
-lactalbumin) was performed in a CSTR. The refolding process of denatured and fully reduced
α
-lactalbumin could be accurately predicted by a set of differential equations assuming a first order reaction rate for folding and a second order reaction rate for aggregation. The system composed of a CSTR with an additional diafiltration circuit for removal of denaturing agents from the feed solution and to maintain constant refolding conditions. Based on the folding kinetic the dynamic behavior of such a continuous refolding reactor was simulated under different operating conditions. It was shown that the refolding efficiency was higher compared to batch dilution under certain conditions, namely high residence times. The yield of refolded protein could further increased by recycling the outlet stream containing unfolded protein to the reactor entrance. |
doi_str_mv | 10.1016/j.ces.2005.04.086 |
format | Article |
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α
-lactalbumin) was performed in a CSTR. The refolding process of denatured and fully reduced
α
-lactalbumin could be accurately predicted by a set of differential equations assuming a first order reaction rate for folding and a second order reaction rate for aggregation. The system composed of a CSTR with an additional diafiltration circuit for removal of denaturing agents from the feed solution and to maintain constant refolding conditions. Based on the folding kinetic the dynamic behavior of such a continuous refolding reactor was simulated under different operating conditions. It was shown that the refolding efficiency was higher compared to batch dilution under certain conditions, namely high residence times. The yield of refolded protein could further increased by recycling the outlet stream containing unfolded protein to the reactor entrance.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/j.ces.2005.04.086</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Chemical engineering ; Continuous refolding ; CSTR ; Diafiltration ; Exact sciences and technology ; Membrane separation (reverse osmosis, dialysis...) ; Reactors ; Renaturation</subject><ispartof>Chemical engineering science, 2005-11, Vol.60 (21), p.5770-5780</ispartof><rights>2005 Elsevier Ltd</rights><rights>2005 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c358t-c8db58a8a681c3f6cdc81ec6b174acf8c366fcbe8c56d8dac6bf7d080c1780203</citedby><cites>FETCH-LOGICAL-c358t-c8db58a8a681c3f6cdc81ec6b174acf8c366fcbe8c56d8dac6bf7d080c1780203</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.ces.2005.04.086$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,777,781,3537,27905,27906,45976</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=16996173$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Schlegl, Robert</creatorcontrib><creatorcontrib>Tscheliessnig, Anne</creatorcontrib><creatorcontrib>Necina, Roman</creatorcontrib><creatorcontrib>Wandl, Robert</creatorcontrib><creatorcontrib>Jungbauer, Alois</creatorcontrib><title>Refolding of proteins in a CSTR</title><title>Chemical engineering science</title><description>A model to predict refolding of proteins in a continuous stirred tank reactor (CSTR) was developed and compared to a batch refolding process with simple dilution of the protein in a stirred tank reactor. For experimental verification of the model a continuous refolding of a model protein (
α
-lactalbumin) was performed in a CSTR. The refolding process of denatured and fully reduced
α
-lactalbumin could be accurately predicted by a set of differential equations assuming a first order reaction rate for folding and a second order reaction rate for aggregation. The system composed of a CSTR with an additional diafiltration circuit for removal of denaturing agents from the feed solution and to maintain constant refolding conditions. Based on the folding kinetic the dynamic behavior of such a continuous refolding reactor was simulated under different operating conditions. It was shown that the refolding efficiency was higher compared to batch dilution under certain conditions, namely high residence times. The yield of refolded protein could further increased by recycling the outlet stream containing unfolded protein to the reactor entrance.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Continuous refolding</subject><subject>CSTR</subject><subject>Diafiltration</subject><subject>Exact sciences and technology</subject><subject>Membrane separation (reverse osmosis, dialysis...)</subject><subject>Reactors</subject><subject>Renaturation</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2005</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LAzEQhoMoWKs_wJN70duuk_1IZvEkxS8oCLWeQzpJJGW7W5NV8N-b0oI3T8Mw7_vOzMPYJYeCAxe364JsLEqApoC6ABRHbMJRVnldQ3PMJgDQ5mUD7Sk7i3GdWik5TNjVwrqhM77_yAaXbcMwWt_HzPeZzmZvy8U5O3G6i_biUKfs_fFhOXvO569PL7P7eU5Vg2NOaFYNatQCOVVOkCHklsSKy1qTQ6qEcLSySI0waHSaOGkAgbhEKKGaspt9bjrh88vGUW18JNt1urfDV1QlNhIliCTkeyGFIcZgndoGv9HhR3FQOxRqrRIKtUOhoFYJRfJcH8J1JN25oHvy8c8o2lZwWSXd3V5n06ff3gYVyduerPHB0qjM4P_Z8gu_tHI1</recordid><startdate>20051101</startdate><enddate>20051101</enddate><creator>Schlegl, Robert</creator><creator>Tscheliessnig, Anne</creator><creator>Necina, Roman</creator><creator>Wandl, Robert</creator><creator>Jungbauer, Alois</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope></search><sort><creationdate>20051101</creationdate><title>Refolding of proteins in a CSTR</title><author>Schlegl, Robert ; Tscheliessnig, Anne ; Necina, Roman ; Wandl, Robert ; Jungbauer, Alois</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c358t-c8db58a8a681c3f6cdc81ec6b174acf8c366fcbe8c56d8dac6bf7d080c1780203</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2005</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Continuous refolding</topic><topic>CSTR</topic><topic>Diafiltration</topic><topic>Exact sciences and technology</topic><topic>Membrane separation (reverse osmosis, dialysis...)</topic><topic>Reactors</topic><topic>Renaturation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Schlegl, Robert</creatorcontrib><creatorcontrib>Tscheliessnig, Anne</creatorcontrib><creatorcontrib>Necina, Roman</creatorcontrib><creatorcontrib>Wandl, Robert</creatorcontrib><creatorcontrib>Jungbauer, Alois</creatorcontrib><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>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Schlegl, Robert</au><au>Tscheliessnig, Anne</au><au>Necina, Roman</au><au>Wandl, Robert</au><au>Jungbauer, Alois</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Refolding of proteins in a CSTR</atitle><jtitle>Chemical engineering science</jtitle><date>2005-11-01</date><risdate>2005</risdate><volume>60</volume><issue>21</issue><spage>5770</spage><epage>5780</epage><pages>5770-5780</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>A model to predict refolding of proteins in a continuous stirred tank reactor (CSTR) was developed and compared to a batch refolding process with simple dilution of the protein in a stirred tank reactor. For experimental verification of the model a continuous refolding of a model protein (
α
-lactalbumin) was performed in a CSTR. The refolding process of denatured and fully reduced
α
-lactalbumin could be accurately predicted by a set of differential equations assuming a first order reaction rate for folding and a second order reaction rate for aggregation. The system composed of a CSTR with an additional diafiltration circuit for removal of denaturing agents from the feed solution and to maintain constant refolding conditions. Based on the folding kinetic the dynamic behavior of such a continuous refolding reactor was simulated under different operating conditions. It was shown that the refolding efficiency was higher compared to batch dilution under certain conditions, namely high residence times. The yield of refolded protein could further increased by recycling the outlet stream containing unfolded protein to the reactor entrance.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ces.2005.04.086</doi><tpages>11</tpages></addata></record> |
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subjects | Applied sciences Chemical engineering Continuous refolding CSTR Diafiltration Exact sciences and technology Membrane separation (reverse osmosis, dialysis...) Reactors Renaturation |
title | Refolding of proteins in a CSTR |
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