Mathematical analysis of two-phase mass transfer in a batch reactor for the chemical transformation of a steroid
A reactor is described for the conversion of the slightly water‐soluble steroid testosterone (T) to 4‐androstene‐3, 17‐dione (4‐AD) by enzyme in the presence of excess cofactor. Since the enzyme is subject to substrate inhibition, reaction rates are strong functions of aqueous substrate concentratio...
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Veröffentlicht in: | Biotechnology and bioengineering 1987-09, Vol.30 (4), p.505-513 |
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creator | Pereira, Vincent Tigli, Husevin Gryte, Carl C. |
description | A reactor is described for the conversion of the slightly water‐soluble steroid testosterone (T) to 4‐androstene‐3, 17‐dione (4‐AD) by enzyme in the presence of excess cofactor. Since the enzyme is subject to substrate inhibition, reaction rates are strong functions of aqueous substrate concentration. High concentrations of the substrate, testosterone, per unit reactor volume are maintained within poly(dimethylsiloxane) beads that are suspended in the aqueous enzyme solution. Mass transfer (controlled by bead size, polymer to water volume ratio, enzyme loading) is used to control the degree and rate of conversion. The reactor dynamics are predicted over a wide range of reaction conditions. The product steroid is recovered in the polymeric beads from the enzyme solution. |
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Since the enzyme is subject to substrate inhibition, reaction rates are strong functions of aqueous substrate concentration. High concentrations of the substrate, testosterone, per unit reactor volume are maintained within poly(dimethylsiloxane) beads that are suspended in the aqueous enzyme solution. Mass transfer (controlled by bead size, polymer to water volume ratio, enzyme loading) is used to control the degree and rate of conversion. The reactor dynamics are predicted over a wide range of reaction conditions. The product steroid is recovered in the polymeric beads from the enzyme solution.</description><identifier>ISSN: 0006-3592</identifier><identifier>EISSN: 1097-0290</identifier><identifier>DOI: 10.1002/bit.260300407</identifier><identifier>PMID: 18581428</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc., A Wiley Company</publisher><subject>4-androstene-3,17-dione ; bioreactors ; mass transfer ; mathematical models ; testosterone</subject><ispartof>Biotechnology and bioengineering, 1987-09, Vol.30 (4), p.505-513</ispartof><rights>Copyright © 1987 John Wiley & Sons, Inc.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3587-240214175819ca1c27d97503b312189d849662fc01d77299b4e53f19b7e7cbd63</citedby><cites>FETCH-LOGICAL-c3587-240214175819ca1c27d97503b312189d849662fc01d77299b4e53f19b7e7cbd63</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fbit.260300407$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fbit.260300407$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,776,780,1411,27901,27902,45550,45551</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/18581428$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Pereira, Vincent</creatorcontrib><creatorcontrib>Tigli, Husevin</creatorcontrib><creatorcontrib>Gryte, Carl C.</creatorcontrib><title>Mathematical analysis of two-phase mass transfer in a batch reactor for the chemical transformation of a steroid</title><title>Biotechnology and bioengineering</title><addtitle>Biotechnol. Bioeng</addtitle><description>A reactor is described for the conversion of the slightly water‐soluble steroid testosterone (T) to 4‐androstene‐3, 17‐dione (4‐AD) by enzyme in the presence of excess cofactor. Since the enzyme is subject to substrate inhibition, reaction rates are strong functions of aqueous substrate concentration. High concentrations of the substrate, testosterone, per unit reactor volume are maintained within poly(dimethylsiloxane) beads that are suspended in the aqueous enzyme solution. Mass transfer (controlled by bead size, polymer to water volume ratio, enzyme loading) is used to control the degree and rate of conversion. The reactor dynamics are predicted over a wide range of reaction conditions. The product steroid is recovered in the polymeric beads from the enzyme solution.</description><subject>4-androstene-3,17-dione</subject><subject>bioreactors</subject><subject>mass transfer</subject><subject>mathematical models</subject><subject>testosterone</subject><issn>0006-3592</issn><issn>1097-0290</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1987</creationdate><recordtype>article</recordtype><recordid>eNp9kT1PHDEQhq0IFA6SMm3kilQLY3vXHyWghG8oQpTS8nq9Oofd9cX2Ce7fx5c7ARXFaDTSM49G8yL0hcARAaDHrc9HlAMDqEF8QDMCSlRAFeygGQDwijWK7qH9lP6UUUjOP6I9IhtJaipnaHFr8tyNJntrBmwmM6ySTzj0OD-FajE3yeHRpIRzNFPqXcR-wga3Jts5js7YHCLuSxULtsX037OBQ1x7w7S2GZyyi8F3n9Bub4bkPm_7Afr14_vD2UV1c39-eXZyU1nWSFHRGiipiSh3KmuIpaJTogHWMkKJVJ2sFee0t0A6IahSbe0a1hPVCids23F2gL5tvIsY_i5dynr0ybphMJMLy6QFY5woUbNCHr5LkloCJyALWG1AG0NK0fV6Ef1o4koT0OswdAlDv4RR-K9b8bIdXfdKb79fALEBnvzgVu_b9Onlw1v19hRf3vr8smnio-aCiUb_vjvXzdXV9cWpZPon-wcTxqPC</recordid><startdate>198709</startdate><enddate>198709</enddate><creator>Pereira, Vincent</creator><creator>Tigli, Husevin</creator><creator>Gryte, Carl C.</creator><general>Wiley Subscription Services, Inc., A Wiley Company</general><scope>BSCLL</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QO</scope><scope>8FD</scope><scope>FR3</scope><scope>P64</scope><scope>7X8</scope></search><sort><creationdate>198709</creationdate><title>Mathematical analysis of two-phase mass transfer in a batch reactor for the chemical transformation of a steroid</title><author>Pereira, Vincent ; Tigli, Husevin ; Gryte, Carl C.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3587-240214175819ca1c27d97503b312189d849662fc01d77299b4e53f19b7e7cbd63</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1987</creationdate><topic>4-androstene-3,17-dione</topic><topic>bioreactors</topic><topic>mass transfer</topic><topic>mathematical models</topic><topic>testosterone</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Pereira, Vincent</creatorcontrib><creatorcontrib>Tigli, Husevin</creatorcontrib><creatorcontrib>Gryte, Carl C.</creatorcontrib><collection>Istex</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Biotechnology Research Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>MEDLINE - Academic</collection><jtitle>Biotechnology and bioengineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Pereira, Vincent</au><au>Tigli, Husevin</au><au>Gryte, Carl C.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Mathematical analysis of two-phase mass transfer in a batch reactor for the chemical transformation of a steroid</atitle><jtitle>Biotechnology and bioengineering</jtitle><addtitle>Biotechnol. Bioeng</addtitle><date>1987-09</date><risdate>1987</risdate><volume>30</volume><issue>4</issue><spage>505</spage><epage>513</epage><pages>505-513</pages><issn>0006-3592</issn><eissn>1097-0290</eissn><abstract>A reactor is described for the conversion of the slightly water‐soluble steroid testosterone (T) to 4‐androstene‐3, 17‐dione (4‐AD) by enzyme in the presence of excess cofactor. Since the enzyme is subject to substrate inhibition, reaction rates are strong functions of aqueous substrate concentration. High concentrations of the substrate, testosterone, per unit reactor volume are maintained within poly(dimethylsiloxane) beads that are suspended in the aqueous enzyme solution. Mass transfer (controlled by bead size, polymer to water volume ratio, enzyme loading) is used to control the degree and rate of conversion. The reactor dynamics are predicted over a wide range of reaction conditions. 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subjects | 4-androstene-3,17-dione bioreactors mass transfer mathematical models testosterone |
title | Mathematical analysis of two-phase mass transfer in a batch reactor for the chemical transformation of a steroid |
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