甲醇抑制时重组毕赤酵母发酵的特性研究

本文对毕赤酵母进行了恒化培养研究。以甲醇为唯一碳源时,在稀释率较低时(D<0.048 h^-1),连续培养系统操作很稳定。但在稀释率高时(D>0.048h^-1),连续培养系统的定态点不止一个,实验不能维持,故采用比生长速率恒定的分批流加培养进行研究。结果表明,毕赤酵母的生长符合Andrew普遍化底物抑制模型。综合考虑水蛭素的生成、底物的消耗,在生产中维持甲醇浓度为限制性浓度(0.5 g/L),且维持比生长速率为0.02 h^-1时,水蛭素Hir65的比生成速率达到最大值0.2 mg/(g·h)且甲醇的比消耗速率为0.04 g/(g·h)。     

重组人干扰素ω在对数生长期毕赤酵母中的高效表达特性研究

用不同比生长速率μ的毕赤酵母探讨其表达外源重组蛋白的差异性,通过起始pH值、甲醇诱导浓度和周期、菌体浓度、装液量等实验,优化具有较高μ的对数生长期毕赤酵母表达rhIFNω的摇瓶条件。结果表明,μ对毕赤酵母表达rhIFNω有显著影响。μ为0.1612h-1的毕赤酵母表达rhIFNω最高为558mg/L,较μ为0.1321、0.0505和0.0052h-1的毕赤酵母分别提高50%、68%和99%。对数生长期的毕赤酵母表达rhIFNω的最适摇瓶表达条件为:250mL摇瓶装入30mL BMMY,控制菌体浓度达到200~300g/L(WCW),起始pH值自然,每24h添加甲醇15g/L一次,诱导表达周期为4d。通过表达条件的优化,rhIFNω的表达量达到1070mg/L,较优化前提高149%。     

重组巴氏毕赤酵母恒化培养动力学及代谢迁移特性研究

通过对甲醇营养型毕赤酵母基因工程菌以碳源甘油为限制性基质进行恒化培养动力学试验 ,结果认为 :(1 )细胞光密度与其干、湿重呈线性关系 ,当细胞光密度 (OD60 0 )为 1 0 0时细胞湿重 (WCW)为 1 2 8 3g L ,细胞干重 (WDW)则为 2 2 9g L ;(2 )基因工程菌P .pastoris的生长与限制性基质甘油残留浓度的关系符合Monod关系式 ,通过 1 μ对 1 S进行线性回归得 μmax=0 .366h- 1,Ks=0 .1 82 3g L ,经参数推导甘油最大菌体得率系数YG =0 .54g g ,菌体维持生长消耗底物系数m =0 .0 0 69g (g·h) ;氧最大菌体系数YX O2 =30 .96g moL ,菌体维持生长时消耗氧系数mO2 =0 .0 0 0 8mol (g·h) ,最适理论稀释速率Dm =0 .341h- 1;(3)从氨水的消耗速率和呼吸商 (RQ)的变化认为随着比生长速率 (μ)的增大 ,甘油代谢流从糖原异生和磷酸戊糖途径线性地向糖酵解和三羧酸循环途径进行代谢迁移 ,即糖酵解和三羧酸循环途径的代谢流量在线性地增大     

Modeling the biofiltration of dimethyl sulfide in the presence of methanol in inorganic biofilters at steady state

The presence of methanol (MeOH) improves DMS removal (up to 11-fold) by enhancing biomass growth in inorganic biofilters. Although the overall effect is positive, prolonged growth on methanol also negatively affects DMS degradation as a result of competition with DMS. The objectives of this study were to explore the potential to optimize DMS removal with methanol addition and to develop and experimentally validate a mathematical model describing the biofiltration of DMS in the presence of MeOH. Continuous experiments using three bench-scale biofilters packed with inorganic material were performed to examine the removal of DMS under different MeOH addition rates ranging from 0 to 140 g/m3/h. For a constant DMS loading of 3.5 g/m3/h, a maximum DMS removal rate of 1.8 g/m3/h was achieved at a MeOH addition rate of 20 g/m3/h in the inorganic biofilters. A steady-state model incorporating the competitive and activation effects of MeOH on DMS biodegradation was developed, and the modeled results on DMS and MeOH removal were in close agreement with experimental data. Both the experimental data and model simulation suggest that there is an optimum MeOH addition rate for a given DMS loading. A step-feeding strategy for MeOH addition was proposed and tested by the model to optimize DMS removal. The model-predicted results demonstrate that six-step feeding of MeOH enhances DMS treatment by 46% in the biofilters when compared to conventional feeding (one-step) of MeOH at the same total mass loading.     

比生长速率和氮源对毕赤酵母生产重组鲈鱼生长激素的影响

对毕赤酵母胞内表达重组鲈鱼生长激素(rljGH)的发酵罐上生产进行了研究.建立了指数流加甲醇的策略并考察了不同比生长速率对rljGH生产的影响.结果表明,随着比生长速率的增加,平均比生产速率相应增加,但是胞内持续积累rljGH的时间减少.最大比rljGH产量(0.58 mg/g WCW)在比生长速率为0.029/h时获得.进一步考察了在诱导阶段添加硫酸铵、蛋白胨和酵母抽提物的影响.结果表明,添加硫酸铵和蛋白胨对于rljGH生产没有显著影响;添加2.5 g/L酵母抽提物有助于胞内rljGH的积累,并使胞内积累持续时间由17 h增加到23 h,提高了发酵稳定性.     

Cultural properties and mass-energy balances in methanol fermentation by Methylomonas methanolovorans

The cultural properties of an obligate methanol utilizer, Methylomonas methanolovorans, were investigated in batch and continuous cultures, and the problems of mass-energy balances were examined. Among the culture data, an exponential increase of growth lag with increased methanol concentration, as well as the inhibition kinetics in the relation between attainable maximum specific growth rate (mu(m) <== 0.52) and methanol concentration are of interest. In the latter case, the inhibition constant (K(i)) and the index number were 40 g/L, and 3 (dimensionless), respectively. The maximum yield coefficient (Y) in both batch and chemostat cultures was around 0.52. An analysis of the behavior of respiratory activity (Q(o2)) in response to the dissolved oxygen concentration (DO) indicated that the oxygen-terminal entity should be regarded as a single one with a saturation constant for DO of 32 mug/L (1.1 x 10(-6)M). Chemostat data showed that the saturation constant for methanol is as low as 2.2 mg/L or 7 x 10(minus;5)M. A linear relationship was observed between the respiratory activity (mol O(2)g(-1)h(-1)) and the specific growth rate (mu i h(-1)), with the relationship Q(o2) = 0.0504mu + 0.00112. The theory of mass and energy balances used by Roels has been reformed to give useful relationships between RQ or the cell yield and mu. In the case of M. methanolovorans, the relations can be greatly simplified since the influence of metabolic by-product formation was negligible. Experimental RQ values (theoretical values for Y = 0.52 and 0.445) at varying mu-values were compared with theoretical ones; despite considerable fluctuations, the results were regarded to conform with theory. By use of mass balance equations and enthalpy data of known compounds, the heat evolution in methanol fermentation was estimated indirectly to be 612 kcal/100 g biomass formed. The Y(ATP) problems are also discussed.     

Growth characteristics of bakers' yeast in ethanol

The influence of temperature (15 degrees -40 degrees C) and pH (2.5-6.0) on the continuous growth of bakers' yeast (Saccharomyces cerevisiae) at steady state in 1% ethanol was investigated. Optimal temperature and pH were 30 degrees C and 4.5, respectively. The short-term effect of ethanol concentration (0.1-10.0%) on the yeast growth was assessed in batch culture. Up to 1% of ethanol, the yeast growth increased in function of the ethanol concentration in the medium. The biomass reached a maximum within the interval of 1-4% of ethanol (7.9 and 31.6 g/L, respectively) and decreased at higher concentrations. The residual ethanol concentration in the medium increased rapidly when the initial ethanol concentration exceeded 4%. The best-fit model obtained for growth inhibition as a function of ethanol concentrations was that of Tseng and Wayman: mu(m)S/)K + S( - i (S - S(theta)). With this model, the specific growth rate (mu) decreased linearly as the ethanol concentration increased between the threshold value (S(theta)) of 11.26 g/L to be fully inhibited at 70.00 g/L (S;) an inhibition constant (i) of 0.0048 g L(-1) h(-1), a maximum specific growth rate (mu(m)) of 0.284 h(-1), and a saturation constant (K) of 0.611 g/L were obtained.     

Growth efficiency and the specific rate of the yeast Hansenula polymorpha during continuous cultivation on methanol

The growth of Hansenula polymorpha DL-1 in the chemostat (under methanol limitation) and turbidostat was measured. Cultivation with different specific rates of growth mu made it possible to determine the maximum yield of biomass Ys(max)=0.425 and the level of expendables required to maintain Ms=0.023 hr-1. The following parameters describing mu as a function of the concentration of methanol S in the fermenter were found: muo=0.154 hr-1 (maximum growth rate), Ks=1.31 mg/l, Ki=5.35 g/l. The paper emphasizes a very low value of the saturation constant Ks derived from the above experiments and reviews the literature data on the kinetic characteristics of various methanol-grown yeast.     

Regulation of calbindin-D9k expression by 1,25-dihydroxyvitamin D(3) and parathyroid hormone in mouse primary renal tubular cells

Membranes of the obligate methylotroph Methylobacillus flagellatus KT contained hemes B, O, and C and cytochromes b, o, and c both in batch and in continuous cultures. Neither heme A nor heme D was detected in the membranes. The cytochromes o and bb were the main components reversibly binding carbon monoxide (CO) in the terminal part of the respiratory chain. The alpha-region and especially the alpha-peaks at 568 and 573 nm and the alpha-troughs at 586 and 592 on the CO-difference spectra were diagnostic for the cytochromes o and bb, respectively. The cytochrome o content increased up to 1.8 times upon increasing the dilution rate of the culture from 0.15 to 0.55 h(-1) under methanol limitation. By contrast, the level of the CO-binding cytochrome bb was not affected by methanol concentration but its content increased up to 1.9 times when the level of oxygen decreased from 95 to 21 microM under the constant dilution rate (mu = 0.55 h(-1)). The maximum ratio between the cytochromes o and bb reached 2 during continuous cultivation under methanol-limited conditions (mu = 0.55 h(-1)), whereas the minimum ratio between them was about 0.7 during batch cultivation at stationary phase of growth. The synthesis of the CO-binding cytochrome bb but not of the cytochrome o in M. flagellatus KT was assumed to depend on the ambient redox potential of the medium. The cytochrome o synthesis was supposed to depend on the transmembrane gradient of protons (Delta(mu)H+).     

Decrease of proteolytic degradation of recombinant hirudin produced by Pichia pastoris by controlling the specific growth rate

The effects of the specific growth rate and methanol concentration on the degradation of hirudin produced by recombinant Pichia pastoris were investigated. When a methanol-limited state and the specific growth rate of 0.02 h^–1 were maintained during the fermentation, a minimum degradation of hirudin and a maximum specific hirudin production rate were achieved. By this strategy, the production of intact recombinant hirudin Hir65 reached 0.7 g l^–1 in fed-batch fermentation. Its proportion was 35% to all forms of hirudin.     

Morphometric evaluation of the specific growth rate of Aspergillus niger grown in agar plates at high glucose levels

Development of surface grown cultures of Aspergillus niger no. 10 was studied at two experimental levels: (a) following the time course of the biomass density (X [=] mg cm(-2)) and fitting the data by the logistic expression, which yielded a macroscopic specific growth rate expressed as mu(obs) = (dX/Xdt)[1-(X/X(max))](-1); and (b) measuring morphometric parameters like the specific elongation rate (k) of the germ tubes and their diameters (D(h)), the colony rate of radial extension (u(r)), and the mean length of distal hyphae (L(av)) to estimate the specific growth rate with the following proposed expression: mu(calc) = u(r)ln2[L(av)ln(L(av)/D(h))](-1). Increases in the initial glucose concentration (10, 40, 70, 120, 200, and 300 g L(-1)) caused reductions in the specific growth rates, the elongation kinetics of the germ tubes, and the hyphal diameter, nevertheless, u(r) and X(max) presented parabolic behavior, showing their maxima in the interval of 90 to 120 g L(-1) of glucose. The overall macroscopic effect of the tested concentrations of glucose on surface grown cultures of A. niger was to produce densely packed and slowly extending colonies, where changes in hyphal lengths and diameters were significant. There was good agreement between mu(obs) and mu(calc) values. Hence, this work validates a kinetic model based on morphometric data to estimate the specific growth rate of molds, obtained from dry weight data, using mold cultures grown in the same solid medium i.e., agar plates. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 287-294, 1997.     

Production of heterologous protein by Methylobacterium extorquens in high cell density fermentation

The green fluorescent protein (GFP) was used as a model protein to study the recombinant protein production by the strain Methylobacterium extorquens ATCC 55366. Scale-up from shake flasks to 20 l fed-batch fermentation was achieved using methanol as a sole carbon and energy source and a completely minimal culture medium. Two different expression vectors were used to express GFP. Clone PCM-GFP containing the vector pCM110 with native promoter of the methanol dehydrogenase PmxaF produced approximately 100-fold more GFP than the clone PRK-GFP containing the vector pRK310 with the heterogeneous promoter Plac. Several fed-batch fermentations with and without selective pressure (tetracycline) were run in a 20 l stirred tank fermenter using the two different clones of M. extorquens. The methanol concentration was monitored with an on-line semiconductor gas sensor in the culture broth. It was maintained at a non-toxic level of 1.4 g l(-1) with an adaptative control which regulates the methanol feed rate. The same growth profile was achieved in all fermentations. The maximum growth rate (micro(max)) was 0.18 h(-1) with an overall yield (Y(X/S)) of 0.3 g g(-1) methanol. With this high cell density fermentation process, we obtained high levels (up to 4 g l(-1)) of GFP with the clone PCM-GFP. The maximum specific GFP production (Y(GFP/X)) with this clone was 80 mg g(-1) representing approximately 16% of the total cell protein. Additional feeding of pure oxygen to the fermenter permitted a longer phase of exponential growth but had no effect on the total yields of biomass and GFP. The specific GFP production of clone PCM-GFP remained unaffected in the presence or absence of selective pressure (tetracycline), within the initial 50 h of the fermentation culture. These results suggest that M. extorquens ATCC 55366 could be an interesting candidate for overexpression of recombinant proteins.     

A rational approach to improving productivity in recombinant Pichia pastoris fermentation

A Mut(S) Pichia pastoris strain that had been genetically modified to produce and secrete sea raven antifreeze protein was used as a model system to demonstrate the implementation of a rational, model-based approach to improve process productivity. A set of glycerol/methanol mixed-feed continuous stirred-tank reactor (CSTR) experiments was performed at the 5-L scale to characterize the relationship between the specific growth rate and the cell yield on methanol, the specific methanol consumption rate, the specific recombinant protein formation rate, and the productivity based on secreted protein levels. The range of dilution rates studied was 0. 01 to 0.10 h(-1), and the residual methanol concentration was kept constant at approximately 2 g/L (below the inhibitory level). With the assumption that the cell yield on glycerol was constant, the cell yield on methanol increased from approximately 0.5 to 1.5 over the range studied. A maximum specific methanol consumption rate of 20 mg/g. h was achieved at a dilution rate of 0.06 h(-1). The specific product formation rate and the volumetric productivity based on product continued to increase over the range of dilution rates studied, and the maximum values were 0.06 mg/g. h and 1.7 mg/L. h, respectively. Therefore, no evidence of repression by glycerol was observed over this range, and operating at the highest dilution rate studied maximized productivity. Fed-batch mass balance equations, based on Monod-type kinetics and parameters derived from data collected during the CSTR work, were then used to predict cell growth and recombinant protein production and to develop an exponential feeding strategy using two carbon sources. Two exponential fed-batch fermentations were conducted according to the predicted feeding strategy at specific growth rates of 0.03 h(-1) and 0.07 h(-1) to verify the accuracy of the model. Cell growth was accurately predicted in both fed-batch runs; however, the model underestimated recombinant product concentration. The overall volumetric productivity of both runs was approximately 2.2 mg/L. h, representing a tenfold increase in the productivity compared with a heuristic feeding strategy.     

Kinetics of hydrogen production with continuous anaerobic cultures utilizing sucrose as the limiting substrate

In this study, local sewage sludge was acclimated to establish H2-producing enrichment cultures, which were used to convert sucrose to H2 with continuously stirred anaerobic bioreactors. The steady-state behaviors of cell growth, substrate utilization, and product formation were closely monitored. Kinetic models were developed to describe and predict the experimental results from the H2-producing cultures. Operation at dilution rates (D) of 0.075-0.167 h(-1) was preferable for H2 production, resulting in a H2 concentration of nearly 0.02 mol/l. The optimal hydrogen production rate was 0.105 mol/h occurring at D=0.125 h(-1). The major volatile fatty acid produced was butyric acid (HBu), while acetic acid and propionic acid were also produced in lesser quantities. The major solvent product was ethanol, whose concentration was only 15% of that of HBu, indicating that the metabolic flow favors H2 production. The proposed model was able to interpret the trends of the experimental data. The maximum specific growth rate (mu(max)), Monod constant (Ks), and yield coefficient for cell growth (Y(x/s)) were estimated as 0.172 h(-1), 68 mg COD/l, and 0.1 g/g, respectively. The model study also suggests that product formation in the continuous hydrogen-producing cultures was essentially a linear function of biomass concentration.     

Use of fed-batch cultivation for achieving high cell densities for the pilot-scale production of a recombinant protein (phenylalanine dehydrogenase) in Escherichia coli

A fed-batch process for the high cell density cultivation of E. coli TG1 and the production of the recombinant protein phenylalanine dehydrogenase (PheDH) was developed. A model based on Monod kinetics with overflow metabolism and incorporating acetate utilization kinetics was used to generate simulations that describe cell growth, acetate production and reconsumption, and glucose consumption during fed-batch cultivation. Using these simulations a predetermined feeding profile was elaborated that would maintain carbon-limited growth at a growth rate below the critical growth rate for acetate formation (mu < mu(crit)). Two starvation periods are incorporated into the feed profile in order to induce acetate utilization. Cell concentrations of 53 g dry cell weight (DCW)/L were obtained with a final intracellular product concentration of recombinant protein corresponding to approximately 38% of the total cell protein. The yield of PheDH was 129 U/mL with a specific activity of 1.2 U/mg DCW and a maximum product formation rate of 0.41 U/mg DCW x h. The concentration of aectate was maintained below growth inhibitory levels until 3 h before the end of the fermentation when the concentration reached a maximum of 10.7 g/L due to IPTG induction of the recombinant protein.     

Kinetics of microbial growth and biodegradation of methanol and toluene in biofilters and an analysis of the energetic indicators

The kinetics of microbial growth and the biodegradation of methanol and toluene in (a) biofilters (BFs), and (b) biotrickling filters (BTFs), packed with inert materials, has been studied and analyzed. The specific growth rate, mu, for the treatment of methanol was 0.037h(-1) for a wide range of operating conditions. In the BF, mu was found to be a function of the methanol and toluene concentrations in the biofilm. In the BF used for treating methanol, mu was found to be affected by (1) the nitrogen concentration present in the nutrient solution, and (2) the kind of packing material employed. The kinetics of the methanol and toluene biodegradations were also analyzed using "mixed order" models. A Michaelis-Menten model type provided a good fit for the elimination capacity (EC) of the BTF treating methanol, while a Haldane model type provided a good fit to the EC of the BF treating methanol and toluene. The carbon dioxide production rate was related to the packed bed temperature and the content of the volatile solids within the biofilm. For the BF, the ratio of temperature/carbon dioxide production rate (PCO(2)) was 0.024 degrees C per unit of PCO(2), and for the BTF it was 0.15 degrees C per unit of PCO(2).     

Production of biomass and beta-D-galactosidase by Candida pseudotropicalis grown in continuous culture on whey

The production of biomass and beta-D-galactosidase by the lactose-utilizing yeast Candida pseudotropicalis NCYC 744 in whey medium was studied. Apparent optimization of growth conditions and medium was done in continuous culture. Optimaql pH and temperature were 2.6 and 36-38 degrees C, respectively, Limitations in Cu, Zn, and possbily Mn were detected in deproteinized whey medium. Additions of tryptophan estimulated growth of the yeast. Under optimal conditions in medium supplemented with excess tryptophan, Cu, Zn, and Mn the maximum values obtained: yeast concentration, 4.6 g/L; yeast productivity, 1.4 g/L h (at D = 0.35 h(-1)); enzyme volumetric productivity, 2100 U/L h (at D = 0.25 h(-1)); maintenance coefficient, 5-10 mg lactose/g cell h; saturation constant (K(s)) for lactose, 4.76mM; maximum specific growth rate, (mu(max)), 0.47 h(-1). No significant increase in specific enzyme activity (U/mg cell) was observed after medium optimiztion evidencing the importance of regulatory controls in enzyme synthesis.     

Quantitative comparison of lactose and glucose utilization in Bifidobacterium longum cultures

In batch cultures, Bifidobacterium longum SH2 has a higher final cell concentration and greater substrate consumption when grown on lactose versus glucose. Continuous cultures were used to compare lactose and glucose utilization by B. longum quantitatively. In the continuous culture, the estimated maintenance coefficients (m) were similar when on lactose and glucose; the maximum cell yield coefficient (Y(X/S)(max)) was higher on lactose; and the specific consumption rate of lactose (q(S)) was lower than that of glucose. Assuming that cell growth followed the Monod model, the maximum specific growth rates (mu(max)) and saturation constants (K(S)) in lactose and glucose media were determined using the Hanes-Woolf plots. The respective values were 0.40 h(-)(1) and 78 mg/L for lactose and 0.46 h(-)(1) and 697 mg/L for glucose. The kinetic parameters of the continuous cultures showed that B. longum preferred lactose to glucose, although the specific consumption rate of glucose was higher than that of lactose.     

Polyhydroxyalkanoate production from whey by Pseudomonas hydrogenovora

Whey permeate from dairy industry was hydrolyzed enzymatically to cleave its main carbon source, lactose, to glucose and galactose. The hydrolysis products were chosen as carbon sources for the production of poly-3-hydroxybutyric acid (PHB) by Pseudomonas hydrogenovora. In shaking flask experiments, the utilization of whey permeate as a cheap substrate was compared to the utilization of pure glucose and galactose for bacterial growth under balanced conditions as well as for the production of PHB under nitrogen limitation. After determination of the inhibition constant Ki for sodium valerate on biomass production (Ki=1.84 g/l), the biosynthesis of PHA co-polyesters containing 3-hydroxybutyrate (3HB) and 3-hydroxyvalerate (3HV) units from hydrolyzed whey permeate and valerate was investigated. The application of hydrolyzed whey permeate turned out to be advantageous compared with the utilization of pure sugars. Therefore, fermentation under controlled conditions in a bioreactor was performed with hydrolyzed whey permeate to obtain detailed kinetic data (maximum specific growth rate, mu max=0.291/h, maximum polymer concentration, 1.27 g/l PHB), values for molecular mass distribution (weight average molecular weight Mw=353.5 kDa, polydispersity index PDI=3.8) and thermo analytical data. The fermentation was repeated with co-feeding of valerate (maximum specific growth rate, mu(max)=0.201/h, maximum polymer concentration, 1.44 g/l poly-(3HB-co-21%-3HV), weight average molecular weight M(w)=299.2 kDa, polydispersity index PDI=4.3).