Growth-rate-independent production of recombinant glucoamylase by Fusarium venenatum JeRS 325
Most recombinant proteins generated in filamentous fungi are produced in fed‐batch cultures, in which specific growth rate normally decreases progressively with time. Because of this, such cultures are more suited to the production of products that are produced efficiently at low‐growth rates (e.g.,...
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description | Most recombinant proteins generated in filamentous fungi are produced in fed‐batch cultures, in which specific growth rate normally decreases progressively with time. Because of this, such cultures are more suited to the production of products that are produced efficiently at low‐growth rates (e.g., penicillin) than to products which are produced more efficiently at high‐growth rates (e.g., glucoamylase). Fusarium venenatum A3/5 has been transformed (JeRS 325) to produce Aspergillus niger glucoamylase (GAM) under the control of the Fusarium oxysporum trypsin‐like protease promoter. No glucoamylase was detected in the culture supernatant during exponential growth of F. venenatum JeRS 325 in batch culture. In glucose‐limited chemostat cultures, GAM concentration increased with decrease in dilution rate, but the specific production rate of GAM (g GAM [g biomass]−1 h−1) remained approximately constant over the dilution‐rate range 0.05 h to 0.19 h−1, i.e., the recombinant protein was produced in a growth‐rate‐independent manner. The specific production rate decreased at dilution rates of 0.04 h−1 and below. Specific production rates of 5.8 mg and 4.0 mg GAM [g biomass]−1 h−1 were observed in glucose‐limited chemostat cultures in the presence and absence of 1 g mycological peptone L−1. Compared to production in batch culture, and for the same final volume of medium, there was no increase in glucoamylase production when cultures were grown in fed‐batch culture. The results suggested that a chemostat operated at a slow dilution rate would be the most productive culture system for enzyme production under this trypsin‐like promoter. © 2000 John Wiley & Sons, Inc. Biotechnol Bioeng 68: 245–251, 2000. |
doi_str_mv | 10.1002/(SICI)1097-0290(20000505)68:3<245::AID-BIT2>3.0.CO;2-F |
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Because of this, such cultures are more suited to the production of products that are produced efficiently at low‐growth rates (e.g., penicillin) than to products which are produced more efficiently at high‐growth rates (e.g., glucoamylase). Fusarium venenatum A3/5 has been transformed (JeRS 325) to produce Aspergillus niger glucoamylase (GAM) under the control of the Fusarium oxysporum trypsin‐like protease promoter. No glucoamylase was detected in the culture supernatant during exponential growth of F. venenatum JeRS 325 in batch culture. In glucose‐limited chemostat cultures, GAM concentration increased with decrease in dilution rate, but the specific production rate of GAM (g GAM [g biomass]−1 h−1) remained approximately constant over the dilution‐rate range 0.05 h to 0.19 h−1, i.e., the recombinant protein was produced in a growth‐rate‐independent manner. The specific production rate decreased at dilution rates of 0.04 h−1 and below. Specific production rates of 5.8 mg and 4.0 mg GAM [g biomass]−1 h−1 were observed in glucose‐limited chemostat cultures in the presence and absence of 1 g mycological peptone L−1. Compared to production in batch culture, and for the same final volume of medium, there was no increase in glucoamylase production when cultures were grown in fed‐batch culture. The results suggested that a chemostat operated at a slow dilution rate would be the most productive culture system for enzyme production under this trypsin‐like promoter. © 2000 John Wiley & Sons, Inc. Biotechnol Bioeng 68: 245–251, 2000.</description><identifier>ISSN: 0006-3592</identifier><identifier>EISSN: 1097-0290</identifier><identifier>DOI: 10.1002/(SICI)1097-0290(20000505)68:3<245::AID-BIT2>3.0.CO;2-F</identifier><identifier>PMID: 10745192</identifier><identifier>CODEN: BIBIAU</identifier><language>eng</language><publisher>New York: John Wiley & Sons, Inc</publisher><subject>Batch cell culture ; Bioconversion ; Biological and medical sciences ; Biosynthesis ; Biotechnology ; Biotechnology - instrumentation ; Biotechnology - methods ; chemostat culture ; Enzyme engineering ; Enzyme kinetics ; Fermentation ; Fundamental and applied biological sciences. Psychology ; Fungi ; Fusarium - enzymology ; Fusarium - genetics ; Fusarium - growth & development ; Fusarium venenatum ; Genetic engineering ; Genetic technics ; Glucan 1,4-alpha-Glucosidase - genetics ; Glucan 1,4-alpha-Glucosidase - metabolism ; glucoamylase ; Growth kinetics ; growth-rate-independent production ; Methods. 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Bioeng</addtitle><description>Most recombinant proteins generated in filamentous fungi are produced in fed‐batch cultures, in which specific growth rate normally decreases progressively with time. Because of this, such cultures are more suited to the production of products that are produced efficiently at low‐growth rates (e.g., penicillin) than to products which are produced more efficiently at high‐growth rates (e.g., glucoamylase). Fusarium venenatum A3/5 has been transformed (JeRS 325) to produce Aspergillus niger glucoamylase (GAM) under the control of the Fusarium oxysporum trypsin‐like protease promoter. No glucoamylase was detected in the culture supernatant during exponential growth of F. venenatum JeRS 325 in batch culture. In glucose‐limited chemostat cultures, GAM concentration increased with decrease in dilution rate, but the specific production rate of GAM (g GAM [g biomass]−1 h−1) remained approximately constant over the dilution‐rate range 0.05 h to 0.19 h−1, i.e., the recombinant protein was produced in a growth‐rate‐independent manner. The specific production rate decreased at dilution rates of 0.04 h−1 and below. Specific production rates of 5.8 mg and 4.0 mg GAM [g biomass]−1 h−1 were observed in glucose‐limited chemostat cultures in the presence and absence of 1 g mycological peptone L−1. Compared to production in batch culture, and for the same final volume of medium, there was no increase in glucoamylase production when cultures were grown in fed‐batch culture. The results suggested that a chemostat operated at a slow dilution rate would be the most productive culture system for enzyme production under this trypsin‐like promoter. © 2000 John Wiley & Sons, Inc. Biotechnol Bioeng 68: 245–251, 2000.</description><subject>Batch cell culture</subject><subject>Bioconversion</subject><subject>Biological and medical sciences</subject><subject>Biosynthesis</subject><subject>Biotechnology</subject><subject>Biotechnology - instrumentation</subject><subject>Biotechnology - methods</subject><subject>chemostat culture</subject><subject>Enzyme engineering</subject><subject>Enzyme kinetics</subject><subject>Fermentation</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Fungi</subject><subject>Fusarium - enzymology</subject><subject>Fusarium - genetics</subject><subject>Fusarium - growth & development</subject><subject>Fusarium venenatum</subject><subject>Genetic engineering</subject><subject>Genetic technics</subject><subject>Glucan 1,4-alpha-Glucosidase - genetics</subject><subject>Glucan 1,4-alpha-Glucosidase - metabolism</subject><subject>glucoamylase</subject><subject>Growth kinetics</subject><subject>growth-rate-independent production</subject><subject>Methods. Procedures. Technologies</subject><subject>Modification of gene expression level</subject><subject>Plant cell culture</subject><subject>Production of selected enzymes</subject><subject>Promoter Regions, Genetic</subject><subject>recombinant protein</subject><subject>Recombinant Proteins - genetics</subject><subject>Recombinant Proteins - metabolism</subject><subject>specific production rate</subject><issn>0006-3592</issn><issn>1097-0290</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2000</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkl1v0zAUhiMEYmXwF1AuENouUvztuKBJI9AuqKLSNj5ukOW4x1sgHyVOGP33OLQb3M0Xto_8nFfH57xRdILRFCNEXh1d5Fl-jJGSCSIKHREUFkf8WKQz-oYwPpud5u-St_klOaFTNM1Wr0kyfxBN7lIeRpOQIhLKFTmInnj_PYQyFeJxdICRZBwrMom-Lbr2pr9OOtNDUjZr2EDYmj7edO16sH3ZNnHr4g5sWxdlY8LLVTXY1tTbyniIi208H7zpyqGOf0EDjenD7QOcX8SU8KfRI2cqD8_252H0af7-MjtLlqtFnp0ukyvGKUmsko6BcoQpxYQNP0jdWjqLU-4sQ8wZZIEI4qBQoFIgmDg0dqRAAGvn6GH0cqcbqv45gO91XXoLVWUaaAevJUaYphjfCxLMmBRE3AtiKRiVjAbw-R4cihrWetOVtem2-rbFAXixB4y3pnKdaWzp_3E0MBwF7PMOuykr2P4no0c_6NEOepytHmerb-2gRaqpDnbQwQ16dEMIkc5Wmuj53zgIJzvh0vfw-07YdD-0kFRy_eXjQn8l5zI9W8pQzh909bsa</recordid><startdate>20000505</startdate><enddate>20000505</enddate><creator>Wiebe, Marilyn G.</creator><creator>Robson, Geoffrey D.</creator><creator>Shuster, Jeff</creator><creator>Trinci, Anthony P.J.</creator><general>John Wiley & Sons, Inc</general><general>Wiley</general><scope>BSCLL</scope><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>7QO</scope><scope>8FD</scope><scope>FR3</scope><scope>P64</scope><scope>7X8</scope></search><sort><creationdate>20000505</creationdate><title>Growth-rate-independent production of recombinant glucoamylase by Fusarium venenatum JeRS 325</title><author>Wiebe, Marilyn G. ; Robson, Geoffrey D. ; Shuster, Jeff ; Trinci, Anthony P.J.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-g4532-c97f4e9f249946c0978fd7fc185fc404fa0ce262feb9e98e212f02000b0eedff3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2000</creationdate><topic>Batch cell culture</topic><topic>Bioconversion</topic><topic>Biological and medical sciences</topic><topic>Biosynthesis</topic><topic>Biotechnology</topic><topic>Biotechnology - instrumentation</topic><topic>Biotechnology - methods</topic><topic>chemostat culture</topic><topic>Enzyme engineering</topic><topic>Enzyme kinetics</topic><topic>Fermentation</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Fungi</topic><topic>Fusarium - enzymology</topic><topic>Fusarium - genetics</topic><topic>Fusarium - growth & development</topic><topic>Fusarium venenatum</topic><topic>Genetic engineering</topic><topic>Genetic technics</topic><topic>Glucan 1,4-alpha-Glucosidase - genetics</topic><topic>Glucan 1,4-alpha-Glucosidase - metabolism</topic><topic>glucoamylase</topic><topic>Growth kinetics</topic><topic>growth-rate-independent production</topic><topic>Methods. Procedures. Technologies</topic><topic>Modification of gene expression level</topic><topic>Plant cell culture</topic><topic>Production of selected enzymes</topic><topic>Promoter Regions, Genetic</topic><topic>recombinant protein</topic><topic>Recombinant Proteins - genetics</topic><topic>Recombinant Proteins - metabolism</topic><topic>specific production rate</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Wiebe, Marilyn G.</creatorcontrib><creatorcontrib>Robson, Geoffrey D.</creatorcontrib><creatorcontrib>Shuster, Jeff</creatorcontrib><creatorcontrib>Trinci, Anthony P.J.</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</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>Wiebe, Marilyn G.</au><au>Robson, Geoffrey D.</au><au>Shuster, Jeff</au><au>Trinci, Anthony P.J.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Growth-rate-independent production of recombinant glucoamylase by Fusarium venenatum JeRS 325</atitle><jtitle>Biotechnology and bioengineering</jtitle><addtitle>Biotechnol. Bioeng</addtitle><date>2000-05-05</date><risdate>2000</risdate><volume>68</volume><issue>3</issue><spage>245</spage><epage>251</epage><pages>245-251</pages><issn>0006-3592</issn><eissn>1097-0290</eissn><coden>BIBIAU</coden><abstract>Most recombinant proteins generated in filamentous fungi are produced in fed‐batch cultures, in which specific growth rate normally decreases progressively with time. Because of this, such cultures are more suited to the production of products that are produced efficiently at low‐growth rates (e.g., penicillin) than to products which are produced more efficiently at high‐growth rates (e.g., glucoamylase). Fusarium venenatum A3/5 has been transformed (JeRS 325) to produce Aspergillus niger glucoamylase (GAM) under the control of the Fusarium oxysporum trypsin‐like protease promoter. No glucoamylase was detected in the culture supernatant during exponential growth of F. venenatum JeRS 325 in batch culture. In glucose‐limited chemostat cultures, GAM concentration increased with decrease in dilution rate, but the specific production rate of GAM (g GAM [g biomass]−1 h−1) remained approximately constant over the dilution‐rate range 0.05 h to 0.19 h−1, i.e., the recombinant protein was produced in a growth‐rate‐independent manner. The specific production rate decreased at dilution rates of 0.04 h−1 and below. Specific production rates of 5.8 mg and 4.0 mg GAM [g biomass]−1 h−1 were observed in glucose‐limited chemostat cultures in the presence and absence of 1 g mycological peptone L−1. Compared to production in batch culture, and for the same final volume of medium, there was no increase in glucoamylase production when cultures were grown in fed‐batch culture. The results suggested that a chemostat operated at a slow dilution rate would be the most productive culture system for enzyme production under this trypsin‐like promoter. © 2000 John Wiley & Sons, Inc. Biotechnol Bioeng 68: 245–251, 2000.</abstract><cop>New York</cop><pub>John Wiley & Sons, Inc</pub><pmid>10745192</pmid><doi>10.1002/(SICI)1097-0290(20000505)68:3<245::AID-BIT2>3.0.CO;2-F</doi><tpages>7</tpages></addata></record> |
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subjects | Batch cell culture Bioconversion Biological and medical sciences Biosynthesis Biotechnology Biotechnology - instrumentation Biotechnology - methods chemostat culture Enzyme engineering Enzyme kinetics Fermentation Fundamental and applied biological sciences. Psychology Fungi Fusarium - enzymology Fusarium - genetics Fusarium - growth & development Fusarium venenatum Genetic engineering Genetic technics Glucan 1,4-alpha-Glucosidase - genetics Glucan 1,4-alpha-Glucosidase - metabolism glucoamylase Growth kinetics growth-rate-independent production Methods. Procedures. Technologies Modification of gene expression level Plant cell culture Production of selected enzymes Promoter Regions, Genetic recombinant protein Recombinant Proteins - genetics Recombinant Proteins - metabolism specific production rate |
title | Growth-rate-independent production of recombinant glucoamylase by Fusarium venenatum JeRS 325 |
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