Kinetics study of pyridine biodegradation by a novel bacterial strain,Rhizobium sp. NJUST18

Biodegradation of pyridine by a novel bacterial strain, Rhizobium sp. NJUST18, was studied in batch experiments over a wide concentration range (from 100 to 1,000 mg l^?1). Pyridine inhibited both growth of Rhizobium sp. NJUST18 and biodegradation of pyridine. The Haldane model could be fitted to the growth kinetics data well with the kinetic constants μ* = 0.1473 h^?1, K _s = 793.97 mg l^?1, K _i = 268.60 mg l^?1 and S _m = 461.80 mg l^?1. The true μ _max, calculated from μ*, was found to be 0.0332 h^?1. Yield coefficient Y _X/S depended on S _i and reached a maximum of 0.51 g g^?1 at S _i of 600 mg l^?1. V _max was calculated by fitting the pyridine consumption data with the Gompertz model. V _max increased with initial pyridine concentration up to 14.809 mg l^?1 h^?1. The q _S values, calculated from $V_{ \hbox{max} }$ , were fitted with the Haldane equation, yielding q _Smax = 0.1212 g g^?1 h^?1 and q* = 0.3874 g g^?1 h^?1 at S _m′ = 507.83 mg l^?1, K _s′ = 558.03 mg l^?1, and K _i′ = 462.15 mg l^?1. Inhibition constants for growth and degradation rate value were in the same range. Compared with other pyridine degraders, μ _max and S _m obtained for Rhizobium sp. NJUST18 were relatively high. High K _i and K _i′ values and extremely high K _s and K _s′ values indicated that NJUST18 was able to grow on pyridine within a wide concentration range, especially at relatively high concentrations.     

Effect of controlled oxygen limitation on Candida shehatae physiology for ethanol production from xylose and glucose

Carbon distribution and kinetics of Candida shehatae were studied in fed-batch fermentation with xylose or glucose (separately) as the carbon source in mineral medium. The fermentations were carried out in two phases, an aerobic phase dedicated to growth followed by an oxygen limitation phase dedicated to ethanol production. Oxygen limitation was quantified with an average specific oxygen uptake rate (OUR) varying between 0.30 and 2.48 mmolO₂ g dry cell weight (DCW)^?1 h^?1, the maximum value before the aerobic shift. The relations among respiration, growth, ethanol production and polyol production were investigated. It appeared that ethanol was produced to provide energy, and polyols (arabitol, ribitol, glycerol and xylitol) were produced to reoxidize NADH from assimilatory reactions and from the co-factor imbalance of the two-first enzymatic steps of xylose uptake. Hence, to manage carbon flux to ethanol production, oxygen limitation was a major controlled parameter; an oxygen limitation corresponding to an average specific OUR of 1.19 mmolO₂ g DCW^?1 h^?1 allowed maximization of the ethanol yield over xylose (0.327 g g^?1), the average productivity (2.2 g l^?1 h^?1) and the ethanol final titer (48.81 g l^?1). For glucose fermentation, the ethanol yield over glucose was the highest (0.411 g g^?1) when the specific OUR was low, corresponding to an average specific OUR of 0.30 mmolO₂ g DCW^?1 h^?1, whereas the average ethanol productivity and ethanol final titer reached the maximum values of 1.81 g l^?1 h^?1 and 54.19 g l^?1 when the specific OUR was the highest.     

Evaluation of ethanol production by a new isolate of yeast during fermentation in synthetic medium and sugarcane bagasse hemicellulosic hydrolysate

A new xylose fermenting yeast was isolated from over-ripe banana by enrichment in xylose-containing medium. The phylogenetic analysis of ITS1-5.8S-ITS2 region sequences of ribosomal RNA of isolate BY2 revealed that it shows affiliation to genus Pichia and clades with Pichia caribbica. In batch fermentation, Pichia strain BY2 fermented xylose, producing 15 g l^?1 ethanol from 30 g l^?1 xylose under shaking conditions at 28°C, with ethanol yield of 0.5 g g^?1 and volumetric productivity of 0.31 g l^?1 h^?1. The optimum pH range for ethanol production from xylose by Pichia strain BY2 was 5–7. Pichia strain BY2 also produced 6.08 g l^?1 ethanol from 30 g l^?1 arabinose. Pichia strain BY2 can utilize sugarcane bagasse hemicellulose acid hydrolysate for alcohol production, efficiency of fermentation was improved by neutralization, and sequential use of activated charcoal adsorption method. Percent total sugar utilized and ethanol yield for the untreated hydrolysate was 17.14% w/v and 0.33 g g^?1, respectively, compared with 66.79% w/v and 0.45 g g^?1, respectively, for treated hemicellulose acid hydrolysate. This new yeast isolate showed ethanol yield of 0.45 g g^?1 and volumetric productivity of 0.33 g l^?1 h^?1 from sugarcane bagasse hemicellulose hydrolysate detoxified by neutralization and activated charcoal treatment, and has potential application in practical process of ethanol production from lignocellulosic hydrolysate.     

Continuous high-ethanol fermentation from cane molasses by a flocculating yeast

Repeated-batch fermentation by a flocculating fusant, Saccharomyces cerevisiae HA 2, was done in a molasses medium that contained 20% (w/v) total sugar, at 30°C in an automatically controlled fermentor, and the effects of ethanol concentration on the specific growth rate and the specific production rate of ethanol were studied. Both the specific growth rate and the specific production rate of ethanol fell with increase of ethanol concentration, and there was a linear correlation between each rate and the concentration of thanol. The maximum specific growth rate (μ_max) and the maximum specific production rate of ethanol (q_max) were 0.12 h⁻¹ and 0.1 g ethanol/10⁹ cells·h, respectively. The specific growth rate and the specific production rate of ethanol fell to zero at ethanol concentration of 89 g/l and 95 g/l, respectively. The number of viable cells, calculated from the linear inhibition equation, was 1.3 × 10⁹ cells/ml for production of 85 g/l ethanol at a dilution rate (D₁) of 0.2 h⁻¹. Based on this estimation, a laboratory-scale continuous fermentation, using two fermentors in series, was done. In the second fermentor, 85 g/l ethanol was produced at a dilution rate (D₁) of 0.2 h⁻¹ by the active feedig of the fermented mash from the first fermentor into the second fermentor by pumping (hereafter called active feeding). To maintain the number of viable cells above 10⁹ cells/ml in the second fermentor, a active feeding ratio of more than 23% was required. Under these conditions, 81 g/l ethanol was produced in the second fermentor at a dilution rate (D_t) of 0.25 h⁻¹, and the high ethanol productivity of 20.3 g/l·h could be achieved. A bench-scale continuous fermentation, using two fermentors in series, with a active feeding ratio of 25% was done. An ethanol concentration of 84 g/l in the second fermentor at a dilution rate (D_t) of 0.25 h⁻¹ was achieved, just as it was in the laboratory-scale fermentation test.     

Effect of tannins on growth and amylase production by Calvatia gigantea

The effect of tannins was investigated on growth and α-amylase (α-1,4-glucan 4-glucanohydrolase, EC 3.2.1.1) production by the edible fungal species Calvatia gigantea, grown in a laboratory-scale fermenter on acorn starch media containing up to 2 g tannins l⁻¹. No inhibition of both growth and amylase excretion was observed when the fungus was cultivated on media containing 40 to 100 times higher tannin concentration than that reported to inhibit microbial growth. Amylase excretion was enhanced when starch was dry sterilized but specific growth rate was higher when starch was wet sterilized. Biomass and amylase production increased with increasing substrate concentration and specific growth rate reached its maximum value at 20 g l⁻¹ starch concentration. The optimum pH of biomass and amylase productionwas 5.0–5.5 and 6.0−6.5 respectively and that of temperature was 29–32 and 29–30°C respectively. Maximum yields of 68 250 U amylase and 0.58–0.60 g biomass g⁻¹ acorn were obtained at optimum growth conditions. A plot of reciprocal growth rate vs. reciprocal starch concentration made it possible to calculate K_s = 0.84 g acorn starch l⁻¹ and μ_max = 0.249 h⁻¹.     

Ethanol fermentation by an efficient strain,NRRL B-4286, of Zymomonas mobilis

We studied the effect of the initial substrate concentration over the range of 100–250 g·l⁻¹ on the fermentation kinetics in batch cultures of Zymomonas mobilis NRRL B-4286 on glucose, fructose, and sucrose, using an adapted initial inoculum. With increasing concentrations of substrate, parameters related to growth were more rapidly and strongly affected than those related to ethanol production. This strain produced 94.0 g·l⁻¹, 76.9 g·l⁻¹, and 66.5 g·l⁻¹ of ethanol at glucose, fructose, and sucrose concentrations of 200 g·l⁻¹, respectively, more than the amount produced by the efficient strain ZM4 (NRRL B-14023).     

Ethanol production by whole cell immobilization using lignocellulosic materials as solid matrix

Amongst four carriers used, rice-straw was found to be superior in terms of ethanol production. The maximum productivity (17.84 gl⁻¹ h⁻¹) corresponded to a dilution rate of 0.39 h⁻¹, the ethanol concentration being 45.80 gl⁻¹. A multistage rhomboidal bioreactor was found to partially overcome the disruption effect caused by the generation of a large volume of carbon dioxide in the column. Increases in productivity of about 12.55% and 3.6%, respectively, were achieved using rhomboidal and tapered bioreactors as compared to the cylindrical bioreactor. It was observed that the generation time of cells, in both the immobilized and free states, was around 2.5 h. The ethanol yield (Y_p/s) in the lower part of the reactor was less in comparison with other zones, where the substrate utilization efficiency was relatively higher.     

Ethanol production in simultaneous saccharification and fermentation of cellulose with temperature profiling

The effects of temperature on enzymatic saccharification of cellulose and simulataneous saccharification and fermentation (SSF) were investigated with 100 g·l⁻¹ Solka Floc, 5g·l⁻¹Trichoderma reesei cellulase, and Zymomonas mobilis ATCC 29191. The following results were obtained: 1) Ethanol fermentation under glucose dificient conditions can proceed for more than 100 h at 30°C but gradually ceases after 50 h of operation at 40°C. 2) Equivalent glucose yield based on cellulose for SSF operated at its optimum temperature (37°C) is higher than that for enzymatic saccharification of cellulose at the same temperature by 32%. However, the same equivalent glucose yields were obtained for both processes if they were operated at their respective optimum temperature. 3) SSF with temperature cycling increased the ethanol productivity but gave similar ethanol yield to SSF at 37°C. 4) SSF with temperature profiling gave an ethanol yield of 0.32 g·g⁻¹ and cellulose use of 0.86 g·g⁻¹ which were increased by 39% and 34% over SSF with temperature cycling and at 37°C.     

Protein production from whey usingPenicillium cyclopium; growth parameters and cellular composition

Summary The growth parameters ofPenicillium cyclopium have been evaluated in a continuous culture system for the production of fungal protein from whey. Dilution rates varied from 0.05 to 0.20 h^–1 under constant conditions of temperature (28°C) and pH (3.5). The saturation coefficients in the Monod equation were 0.74 g l^–1 for lactose and 0.14 mg l^–1 for oxygen, respectively. For a wide range of dilution rates, the yield was 0.68 g g^–1 biomass per lactose and the maintenance coefficient 0.005 g g^–1 h^–1 lactose per biomass, respectively. The maximum biomass productivity achieved was 2 g l^–1 h^–1 biomass at dilution rates of 0.16–0.17 h^–1 with a lactose concentration of 20 g l^–1 in the feed. The crude protein and total nucleic acid contents increased with a dilution rate, crude protein content varied from 43% to 54% and total nucleic acids from 6 to 9% in the range of dilution rates from 0.05 to 0.2 h^–1, while the Lowry protein content was almost constant at approximately 37.5% of dry matter.Nomenclature (mg l^–1) C_o initial concentration of dissolved oxygen - (h^–1) D dilution rate - (mg l^–1) K₀₂ saturation coefficient for oxygen - (g l^–1) K_s saturation coefficient for substrate - (g g^–1 h^–1) lactose per biomass) m maintenance energy coefficient - (mM g^–1 h^–1O₂ per biomass) Q₀₂ specific oxygen uptake rate - (g l^–1) S residual substrate concentration at steady state - (g l^–1) S_o initial substrate concentration in feed - (min) t_1/2 time when C_o is equal to C_o/2 - (g l^–1) X biomass concentration - (g l^–1) X biomass concentration at steady state - (g g^–1 biomass per lactose) Y_G yield coefficient for cell growth - (g g^–1 biomass per lactose) Y_x/s overall yield coefficient - (h^–1) specific growth rate     

Lipid and biomass production by the halotolerant microalga Nannochloropsis salina

The effect of environmental factors on cell-lipid content, on the growth rate and on the overall productivity of Nannochloropsis salina was tested in the laboratory and in outdoor cultures. Under optimum conditions in the laboratory, the maximum growth rate (μ_max) was 0·030 h⁻¹, which corresponds to a doubling time of 23 h. Cellular lipid content was affected by the phase of growth and the temperature, but not by nitrogen starvation, pH or the source of sea water. The most important factor affecting the output rate of biomass was the cell concentration. The maximum biomass productivity obtained in outdoor ponds was 24·5 g·m⁻²·day⁻¹, and the lipid production rate was 4·0 g m⁻²·day⁻¹.     

Reverse NaCa exchange requires internal Ca and/or ATP in squid axons

Classical NaCa exchange models are based on a symmetric carrier system where Na and Ca competing from the same site, can produce net movement of the other against its electrochemical gradient. We have explored this symmetric assumption by studying the Ca_o and Na_o-dependent Na efflux in dialyzed squid axons in which proper control of both external and internal medium was achieved. The results show: (1) In axons dialyzed without Ca_i and ATP, Ca_o-dependent Na efflux cannot be detected even in the absence of Na_o. Under these conditions, the level of Na efflux (1 pmol · cm⁻² · s⁻¹) is close to that predicted by an electrical ‘leak’. (2) In axons dialyzed with Ca_i (100 μM) and without ATP, Na efflux measured in 440 mM Na_o, is about 4–5 pmol · cm⁻² · s⁻¹ and rather insensitive to Ca_o between 0 and 10 mM. However, in the absence of Na_o, a Ca_o-dependent Na efflux is observed similar in magnitude to that found in the presence of external Na. (3) In the presence of both Ca_i and ATP, Na efflux into artificial sea-water (440 mM Na, 10 mM Ca) is 18 pmol · cm⁻² · s⁻¹. In the absence of Na_o the efflux of Na is 7.5 pmol · cm⁻² · s⁻¹. In the absence of both Na_o and Ca_o the efflux is close to ‘leak’. With full Na_o but no Ca_o, the Na efflux average 12.6 pmol · cm⁻² · s⁻¹. These results indicate a marked asymmetry in the modus operandi of the NaCa exchange system with respect to Ca_i and ATP. These two substrates are required from the cis side to promote Ca_o-dependent Na efflux (reversal NaCa exchange).     

Modelling and design of a high productivity ethanol process using Zymomonas mobilis — I

Growth kinetics and ethanol production of Zymomonas mobilis in a bioreactor with cell recycle were modelled. High specific growth rates can be used to control excessive biomass accumulation in the system. Predicted peak productivity with a cell concentration of 80 g l⁻¹, a dilution rate of 6.5 h⁻¹, and a feed glucose concentration of 120 g l⁻¹ is 350 g l⁻¹ h⁻¹. The design of a special recycle reactor using a filter which should permit the operating conditions required for the validation of the model is proposed.     

The production of xylitol from d-xylose by fermentation with Hansenula polymorpha

We have analysed the influence of the initial pH of the medium and the quantity of aeration provided during the batch fermentation of solutions of d-xylose by the yeast Hansenula polymorpha (34438 ATCC). The initial pH was altered between 3.5 and 6.5 whilst aeration varied between 0.0 and 0.3 vvm. The temperature was kept at 30 °C during all the experiments. Hansenula polymorpha is known to produce high quantities of xylitol and low quantities of ethanol. The most favourable conditions for the growth of xylitol turned out to be: an initial pH of between 4.5 and 5.5 and the aeration provided by the stirring vortex alone. Thus, at an initial pH of 5.5, the maximum specific production rate (μ_m) was 0.41 h⁻¹, the overall biomass yield (Y _x/s ^G) was 0.12 g g⁻¹, the specific d-xylose-consumption rate (q _s ) was 0.075 g g⁻¹ h⁻¹ (for t = 75 h), the specific xylitol-production rate (q _Xy ) was 0.31 g g⁻¹ h⁻¹ (for t = 30 h) and the overall yields of ethanol (Y _E/s ^G) and xylitol (Y _Xy/s ^G) were 0.017 and 0.61 g g⁻¹ respectively. Both q _s and q _Xy decreased during the course of the experiments once the exponential growth phase had finished. Received: 26 March 1998 / Received revision: 30 June 1998 / Accepted: 2 July 1998     

Factors affecting l-arginine production in the continuous culture of an l-arginine producer of Corynebacterium acetoacidophilum

The effects of culture conditions on l-arginine production by continuous culture were studied using a stable l-arginine hyperproducing strain of Corynebacterium aceto-acidophilum, SC-190. Strain SC-190 demonstrated a volumetric productivity of 35 g l⁻¹·h⁻¹ at a dilution rate of 0.083h⁻¹ and feeding sugar concentration of 8%, and a product yield of 29.2% at a dilution rate 0.021h⁻¹ and feeding sugar concentration of 15%. The corresponding values for fed-batch culture are 0.85 g·l⁻¹·h⁻¹ and 26%. However, the product yield decreased with an increase in the volumetric productivity. To achieve stable l-arginine production, aeration and agitation conditions sufficient to maintain an optimal level of redox potential (>−100 mV) were necessary. The addition of phosphate to the feeding medium led to a decrease in l-arginine production. It was confirmed in the steady state that growth and l-arginine formation were inhibited by a high concentration of l-arginine.     

Continuous production of an antibiotic polypeptide (nisin) by Lactococcus lactis using a bioreactor coupled to a microfiltration module

The continuous production of nisin, an antibiotic polypeptide, by Lactococcus lactis in a bioreactor system coupled to a microfiltration module is described. Nisin productivity with respect to both cultivation time (ND) and the quantity of glucose consumed (ND/S_f) in continuous production was enhanced by maintaining a low concentration of lactic acid in the broth. A maximum ND of 7.80 × 10⁴ U·l⁻¹·h⁻¹ and ND/S_f of 5.20 × 10³ U·g⁻¹·h⁻¹ were obtained when the glucose concentration in the feed medium was 15 g/l. These values represent about 4.1- and 4.5-fold increases, respectively, over those obtained in batch culture.     

Comparative anaerobic treatment of wastewater from pharmaceutical,brewery, paper and amino acid producing industries

This study concerned the anaerobic treatment of five different industrial wastewaters with a diverse and complex chemical composition. The kinetics of biotransformation of this wastewater at different chemical oxygen demand (COD) were studied in a batch reactor. Wastewater from an amino acid producing industry (Fermex) and from a tank that received several types of wastewaters (collector) contained 0.83 g l⁻¹ and 0.085 g l⁻¹ sulfate, respectively. During the study period of 20 days, methane formation was observed in all types of wastewaters. Studies on COD biodegradation showed the reaction velocity was higher for Fermex wastewater and lower for collector wastewater, with values of 0.0022 h⁻¹ and 0.0011 h⁻¹, respectively. A lower methanogenic activity of 0.163 g CH₄ day⁻¹ g⁻¹ volatile suspended solids (VSS) and 0.20 g CH₄ day⁻¹ g⁻¹ VSS, respectively, was observed for paper producing and brewery wastewater. Adapted granular sludge showed the best biodegradation of COD during the 20-day period. The sulfate-reducing activity in pharmaceutical and collector wastewater was studied. A positive effect of sulfate-reducing activity on methanogenic activity was noted for both types of wastewaters, both of which contained sulfate ions. All reactions of methane generation for the tested industrial wastewaters were first-order. The results of this study suggest that the tested wastewaters are amenable to anaerobic treatment.

     

Bioethanol production in batch mode by a native strain of <Emphasis Type="Italic">Zymomonas mobilis</Emphasis>

Two wild strains of Zymomonas mobilis were isolated (named as ML1 and ML2) from sugar cane molasses obtained from different farms of Santander, Colombia. Initially, selection of the best ethanol-producer strains was carried out using ethanol production parameters obtained with a commercial strain Z. mobilis DSM 3580. Three isolated strains were cultivated in a culture medium containing yeast extract, peptone, glucose and salts, at pH 6 and 32°C with stirring rate of 65 rpm during 62 h. The best results of ethanol production were obtained with the native strain ML1, reaching a maximum ethanol concentration of 79.78 g l⁻¹. ML1 and ML2 strains were identified as Z. mobilis, according to the morphology, biochemical tests and molecular characterization by PCR of specific DNA sequences from Z. mobilis. Subsequently, the effect of different nitrogen sources on production of ethanol was evaluated. The best results were obtained using urea at a 0.73 g/l. In this case, maximum concentration of ethanol was 83.81 g l⁻¹, with kinetic parameters of yield of ethanol on biomass (Y_P/X) = 69.01(g g⁻¹), maximum volumetric productivity of ethanol (Qp_max) = 2.28 (g l⁻¹ h⁻¹), specific productivity of ethanol (q_P) = 3.54 (h⁻¹) and specific growth rate (μ) = 0.12 h⁻¹. Finally, we studied the effect of different culture conditions (pH, temperature, stirring, C/N ratio) with a Placket-Burman′s experimental design. This optimization indicated that the most significant variables were temperature and stirring. In the best culture conditions a significant increase in all variables of response was achieved, reaching a maximum ethanol concentration of 93.55 g l⁻¹.     

The effect of glycerol mixed substrate on the heterologous production of a Rhizopus oryzae lipase in Pichia pastoris system

A recombinant Rhizopus oryzae lipase producing Mut^s Pichia pastoris strain was used as a model organism to study the effect of mixed substrates (glycerol and methanol) on the specific product productivity. Different fed-batch cultivations were performed under three constant specific growth rates (0.02, 0.05 and 0.1 h⁻¹), maintaining a constant methanol concentration of 2 g l⁻¹.At the lowest μ tested (0.02 h⁻¹), the specific productivity was 1.23 and 1.61 fold higher and the specific methanol consumption rate (q_sMeOH) was 3 and 3.5 fold higher than values obtained when μ was 0.05 and 0.1 h⁻¹, respectively. This implies a relation between the q_sMeOH and the specific productivity, yielding higher specific productivities whenever the consumption of methanol is higher. Although glycerol was maintained under limiting conditions in all μ tested, when the relation between the μ_Gly and μ_MeOH was larger than 4, an important decrease on the maximal activity value was observed.Finally, a comparison under the same conditions using glycerol or sorbitol as co-substrates was also performed, obtaining better specific productivity when sorbitol was used. In addition, protease activity was detected when glycerol was used as co-substrate.     

Oleaginous yeast Meyerozyma guilliermondii shows fermentative metabolism of sugars in the biosynthesis of ethanol and converts raw glycerol and cheese whey permeate into polyunsaturated fatty acids

We studied the biotechnological potential of the recently isolated yeast Meyerozyma guilliermondii BI281A to produce polyunsaturated fatty acids and ethanol, comparing products yields using glucose, raw glycerol from biodiesel synthesis, or whey permeate as substrates. The yeast metabolism was evaluated for different C/N ratios (100:1 and 50:1). Results found that M. guilliermondii BI281A was able to assimilate all tested substrates, and the most efficient conversion obtained was observed using raw glycerol as carbon source (C/N ratio 50:1), concerning biomass formation (5.67 g·L⁻¹) and lipid production (1.04 g·L⁻¹), representing 18% of dry cell weight. Bioreactors experiments under pH and aeration-controlled conditions were conducted. Obtained fatty acids were composed of ~67% of unsaturated fatty acids, distributed as palmitoleic acid (C_16:1, 9.4%), oleic acid (C_18:1, 47.2%), linoleic acid (C_{18:2 n−6}, 9.6%), and linolenic acid (C_{18:3 n−3}, 1.3%). Showing fermentative metabolism, which is unusual for oleaginous yeasts, M. guilliermondii produced 13.7 g·L⁻¹ of ethanol (yields of 0.27) when growing on glucose medium. These results suggest the promising use of this uncommonly studied yeast to produce unsaturated fatty acids and ethanol using cheap agro-industrial residues as substrates in bioprocess.     

Recombinant Protein Production with Pichia pastoris in Continuous Fermentation – Kinetic Analysis of Growth and Product Formation

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 Monod approach. Maximum growth rate μ_max was determined to 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 π_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.