2001
DOI: 10.1021/bp000164j
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Human Chymotrypsinogen B Production with Pichiapastoris by Integrated Development of Fermentation and Downstream Processing. Part 1. Fermentation

Abstract: Based on an integrated approach of genetic engineering, fermentation process development, and downstream processing, a fermentative chymotrypsinogen B production process using recombinant Pichia pastoris is presented. Making use of the P. pastoris AOX1-promotor, the demand for methanol as the single carbon source as well as an inducer of protein secretion enforced the use of an optimized feeding strategy by help of on-line analysis and an advanced controller algorithm. By using an experimental system of six pa… Show more

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Cited by 78 publications
(64 citation statements)
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“…Thus, the common concept of a toxicity threshold for extracellular methanol concentration may be questioned. However, production strategies under AOX1 promoter control of Mut ϩ strains usually require control of methanol addition to achieve residual (extracellular) concentrations ranging from 1 to 5 g liter Ϫ1 (10,11,19,21,57,60). Concentrations of more than 3.5 g liter Ϫ1 are reported to inhibit biomass growth (60), while concentrations of more than 8 g liter Ϫ1 cause a decrease in productivity (57).…”
Section: Discussionmentioning
confidence: 99%
“…Thus, the common concept of a toxicity threshold for extracellular methanol concentration may be questioned. However, production strategies under AOX1 promoter control of Mut ϩ strains usually require control of methanol addition to achieve residual (extracellular) concentrations ranging from 1 to 5 g liter Ϫ1 (10,11,19,21,57,60). Concentrations of more than 3.5 g liter Ϫ1 are reported to inhibit biomass growth (60), while concentrations of more than 8 g liter Ϫ1 cause a decrease in productivity (57).…”
Section: Discussionmentioning
confidence: 99%
“…Chung (2000) estimated that 0.64 mol of oxygen is required per mol of methanol consumed based on methanol metabolism stoichiometry and a correlation between specific oxygen and methanol uptake rates obtained from steady state fed-batch cultivation conditions. Curvers et al (2001) used the measured yield of biomass from methanol (0.32 g DCW/g CH 3 OH) combined with an elemental analysis of biomass (CH 1.68 O 0.61 N 0.12 ) grown on methanol to calculate that 1.08 mol of O 2 is required per mole of methanol consumed. Cunha et al (2004) as well as Jahic et al (2003) measured the oxygen consumption rate as a function of the methanol uptake rate in fed-batch cultivations to be 0.8-1.1 mol O 2 /mol methanol consumed.…”
Section: Introductionmentioning
confidence: 99%
“…Continuous bioprocess using methanol was performed via online methanol measurement and control using a minimal-variance-controller and a semi-continuous Kalman-Filter (Curvers et al, 2001).…”
Section: Introductionmentioning
confidence: 99%