001     34117
005     20180210141456.0
024 7 _ |2 DOI
|a 10.1002/1522-2640(200112)73:12<1615::AID-CITE1615>3.0.CO;2-6
024 7 _ |2 WOS
|a WOS:000173288200018
037 _ _ |a PreJuSER-34117
041 _ _ |a eng
082 _ _ |a 540
084 _ _ |2 WoS
|a Engineering, Chemical
100 1 _ |a Curves, S.
|0 P:(DE-Juel1)VDB4399
|b 0
|u FZJ
245 _ _ |a Recombinant protein production with pichia pastoris in continuous fermentation - kinetic analysis of growth and production formation
260 _ _ |a Weinheim
|b Wiley-VCH Verl.
|c 2001
300 _ _ |a 1615 - 1621
336 7 _ |a Journal Article
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336 7 _ |a Output Types/Journal article
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336 7 _ |a Journal Article
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336 7 _ |a ARTICLE
|2 BibTeX
336 7 _ |a JOURNAL_ARTICLE
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336 7 _ |a article
|2 DRIVER
440 _ 0 |a Chemie Ingenieur Technik
|x 0009-286X
|0 1215
|y 12
|v 73
500 _ _ |a Record converted from VDB: 12.11.2012
520 _ _ |a Continuous fermentation was applied to the production of recombinant human chymotrypsinogen B (hCTRB) by the methylotrophic yeast Pichia pastoris as a tool for the kinetic analysis of growth and product formation. Using methanol as the sole source of carbon, energy, and induction, cell growth could be described by a non-competitive M ON approach. The maximum growth rate p a,, was determined to be 0.084 h(-1) and the K-M-value for methanol to 0.22 g L-1, respectively. With respect to product formation a similar model was established exhibiting a methanol concentration of 0.13 g L-1 as the K-M-value and a maximum biomass-specific product-formation rate Of pi(max) = 0.23 mg g(-1) h(-1). The production of hCTRB was strictly growth-coupled.The data provided covers the range of methanol concentrations between 0 and 4 g L-1. Substrate concentrations exceeding this upper value led to a complete collapse of product formation. This change in phenotype turned out to be irreversible indicating a genetic instability of transformed Pichia pastoris caused by excess methanol.
536 _ _ |a Verfahrenstechnik zur mikrobiellen Gewinnung von Primärmetaboliten
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588 _ _ |a Dataset connected to Web of Science
650 _ 7 |a J
|2 WoSType
700 1 _ |a Linnemann, J.
|0 P:(DE-HGF)0
|b 1
700 1 _ |a Klauser, T.
|0 P:(DE-HGF)0
|b 2
700 1 _ |a Wandrey, C.
|0 P:(DE-Juel1)129071
|b 3
|u FZJ
700 1 _ |a Takors, R.
|0 P:(DE-Juel1)VDB1625
|b 4
|u FZJ
773 _ _ |a 10.1002/1522-2640(200112)73:12<1615::AID-CITE1615>3.0.CO;2-6
|g Vol. 73, p. 1615 - 1621
|p 1615 - 1621
|q 73<1615 - 1621
|0 PERI:(DE-600)2035041-7
|t Chemie - Ingenieur - Technik
|v 73
|y 2001
|x 0009-286X
909 C O |o oai:juser.fz-juelich.de:34117
|p VDB
913 1 _ |k 41.40.0
|v Verfahrenstechnik zur mikrobiellen Gewinnung von Primärmetaboliten
|l Biotechnologie
|b Lebenswissenschaften
|0 G:(DE-Juel1)FUEK93
|x 0
914 1 _ |y 2001
915 _ _ |0 StatID:(DE-HGF)0010
|a JCR/ISI refereed
920 1 _ |k IBT-2
|l Biotechnologie 2
|g IBT
|z ab 31.10.10 weitergeführt IBG-1
|0 I:(DE-Juel1)VDB56
|x 0
970 _ _ |a VDB:(DE-Juel1)3994
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980 _ _ |a journal
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980 _ _ |a UNRESTRICTED
981 _ _ |a I:(DE-Juel1)IBG-1-20101118


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