Improvement of cloned alpha-amylase gene expression in fed-batch culture of recombinant Saccharomyces cerevisiae by regulating both glucose and ethanol concentrations using a fuzzy controller

The effect of ethanol concentration on cloned gene expression in recombinant Saccharomyces cerevisiae strain 20B-12 containing one of two plasmids, pNA3 and pNA7, was investigated in batch cultures. Plasmids pNA3 and pNA7 contain the alpha-amylase gene under the control of the SUC2 or PGK promoter, respectively. When the ethanol concentration was controlled at 2 to 5 g/L, the gene expressions were two times higher than those at 20 g/L ethanol. The increase the gene expression by maintaining both the ethanol and glucose concentrations at low levels, a fuzzy ontroller was developed. The concentrations of glucose and ethanol were controlled simultaneously at 0.15 and 2 g/L, respectively, in the production phase using the fuzzy controller in fed-batch culture. The synthesis of alpha-amylase was induced by the low glucose concentration and maintained at a high level of activity by regulating the ethanol concentration at 2 g/L. The secretory alpha-amylase was induced by the low glucose concentration and maintained at a high level of activity by regulating the ethanol concentration at 2 g/L. The secretory alpha-amylase activities of cells harboring plasmids pNA3 and pNA7 in fed-batch culture were 175 and 395 U/mL, and their maximal specific activities 7.7 and 12.4 U/mg dry cells, respectively. These values are two to three times higher in activity and three to four times higher in specific activity than those obtained when glucose only was controlled. (c) 1994 John Wiley & Sons, Inc.     

Characteristics of Saccharomyces cerevisiae gal1 Delta and gal1 Delta hxk2 Delta mutants expressing recombinant proteins from the GAL promoter

Galactose can be used not only as an inducer of the GAL promoters, but also as a carbon source by Saccharomyces cerevisiae, which makes recombinant fermentation processes that use GAL promoters complicated and expensive. To overcome this problem during the cultivation of the recombinant strain expressing human serum albumin (HSA) from the GAL10 promoter, a gal1 Delta mutant strain was constructed and its induction kinetics investigated. As expected, the gal1 Delta strain did not use galactose, and showed high levels of HSA expression, even at extremely low galactose concentrations (0.05-0.1 g/L). However, the gal1 Delta strain produced much more ethanol, in a complex medium containing glucose, than the GAL1 strain. To improve the physiological properties of the gal1 Delta mutant strain as a host for heterologous protein production, a null mutation of either MIG1 or HXK2 was introduced into the gal1 Delta mutant strain, generating gal1 Delta mig1 Delta and gal1 Delta hxk2 Delta double strains. The gal1 Delta hxk2 Delta strain showed a decreased rate of ethanol synthesis, with an accelerated rate of ethanol consumption, compared to the gal1 Delta strain, whereas the gal1 Delta mig1 Delta strain showed similar patterns to the gal1 Delta strain. Furthermore, the gal1 Delta hxk2 Delta strain secreted much more recombinant proteins (HSA and HSA fusion proteins) than the other strains. The results suggest that the gal1 Delta hxk2 Delta strain would be useful for the large-scale production of heterologous proteins from the GAL10 promoter in S. cerevisiae.     

Different expression systems for production of recombinant proteins in Saccharomyces cerevisiae

Yeast Saccharomyces cerevisiae has become an attractive cell factory for production of commodity and speciality chemicals and proteins, such as industrial enzymes and pharmaceutical proteins. Here we evaluate most important expression factors for recombinant protein secretion: we chose two different proteins (insulin precursor (IP) and α-amylase), two different expression vectors (POTud plasmid and CPOTud plasmid) and two kinds of leader sequences (the glycosylated alpha factor leader and a synthetic leader with no glycosylation sites). We used IP and α-amylase as representatives of a simple protein and a multi-domain protein, as well as a non-glycosylated protein and a glycosylated protein, respectively. The genes coding for the two recombinant proteins were fused independently with two different leader sequences and were expressed using two different plasmid systems, resulting in eight different strains that were evaluated by batch fermentations. The secretion level (μmol/L) of IP was found to be higher than that of α-amylase for all expression systems and we also found larger variation in IP production for the different vectors. We also found that there is a change in protein production kinetics during the diauxic shift, that is, the IP was produced at higher rate during the glucose uptake phase, whereas amylase was produced at a higher rate in the ethanol uptake phase. For comparison, we also refer to data from another study, (Tyo et al. submitted) in which we used the p426GPD plasmid (standard vector using URA3 as marker gene and pGPD1 as expression promoter). For the IP there is more than 10-fold higher protein production with the CPOTud vector compared with the standard URA3-based vector, and this vector system therefore represent a valuable resource for future studies and optimization of recombinant protein production in yeast.     

Enhanced production of alpha-amylase in fed-batch cultures of Bacillus subtilis TN106[pAT5

Growth of Bacillus subtilis TN106[pAT5] and synthesis of plasmid-encoded protein (alpha-amylase) are investigated in batch, continuous, and fed-batch cultures using a defined medium containing glucose and/or starch as the carbohydrate source. The batch culture studies reveal that reduced availability of arginine hampers growth of recombinant cells (which lack an arginine synthesis gene) but promotes production of alpha-amylase and substitution of glucose by starch as the carbohydrate source leads to slower growth of recombinant cells and increased production of alpha-amylase per unit cell mass. Retention of recombinant cells over prolonged periods in continuous cultures is not possible without continuous application of antibiotic selection pressure owing to segregational plasmid instability. Fed-batch experiments with constant volumetric feed rate demonstrate that alpha-amylase production is enhanced at lower feed concentration of starch (sole carbohydrate source) and lower volumetric feed rate. Such slow addition of starch is however not conducive for growth of recombinant cells. The expression of the thermostable alpha-amylase gene carried on the recombinant plasmid pAT5 (derived from a plasmid isolated from a thermophilic bacterium) is promoted at higher temperatures, while growth of recombinant cells is depressed. In all batch and fed-batch experiments, production of alpha-amylase is observed to be inversely related to growth of recombinant cells. The efficacy of two-stage bioreactor operations, with growth of recombinant cells being promoted in the first stage and alpha-amylase production in the second stage, in attaining increased bulk alpha-amylase activity is demonstrated. (c) 1993 John Wiley & Sons, Inc.     

Enhancement of production of cloned glucoamylase under conditions of low aeration from recombinant yeast using a SUC2 promoter

The effect of aeration rate on the production of cloned glucoamylase in a recombinant yeast was investigated. This system consisted of Saccharomyces cerevisiae transformed with the 2 μ-based plasmid YEpSUCSTA which contains the SUC2 promoter, the STA signal sequence, and the STA structural gene. In contrast to typical yeast expression reports, high production of cloned glucoamylase was achieved at low aeration level (0·3 vvm). The recombinant yeast grown at 0·3 vvm aeration produced more glucoamylase (0·94 units/ml) than when grown at 0·0 vvm, 0·6 vvm, or 0·9 vvm (9·4, 1·4, and 3·1 times more, respectively). A high dissolved oxygen level early in the cultivation was important for cell growth and a low dissolved oxygen level during the production stage was important for glucoamylase production. In large scale processes for the production of recombinant proteins, the maintenance of aeration and dissolved oxygen at high levels is difficult and expensive. In this work, we have evaluated the coordination of oxygen level with growth and protein production and developed optimal conditions. Since a low aeration rate was optimal, our results demonstrate that the method described at the laboratory scale should be successfully applied at an industrial scale.     

Enhancement of plasmid stability and protein productivity using multi-pulse, fed-batch culture of recombinant Saccharomyces cerevisiae

The plasmid stability of a recombinant Saccharomyces cerevisiae strain, which expresses cloned -amylase, was increased when glucose or yeast extract was fed with multi-pulse mode in fed-batch culture. Using a novel strategy combining constant rate fed-batch culture and multi-pulse feeding of yeast extract, the plasmid stability was maintained over 90%, meanwhile, 36 g cells l^–1 and 208 units of cloned -amylase activity ml^–1 were obtained.     

Specific processing of the bacterial beta-lactamase precursor in Saccharomyces cerevisiae

Synthesis and processing of the bacterial enzyme beta-lactamase (E.C. 3.5. 2.6) were studied in Saccharomyces cerevisiae. The 2-micron DNA vector pADH040-2 containing the yeast ADH1 promoter fused to the bacterial gene was used in order to obtain enhanced synthesis of the bacterial protein in yeast transformants. Both precursor and mature beta-lactamase were shown to be present in yeast cells, the precursor being the major product. The mature enzyme was purified about 500-fold over crude extracts to apparent homogeneity and thus represents nearly 0.2% of the total yeast protein. No difference in specific activity and molecular weight could be observed when compared with the authentic beta-lactamase from Escherichia coli. Specificity of the processing of beta-lactamase in yeast cells was verified by partial amino acid sequence analysis demonstrating the removal of the signal peptide at the correct position.     

Enhanced beta-galactosidase production by high cell-density culture of recombinant Bacillus subtilis with glucose concentration control

Cell concentration, recombinant protein (beta-galactosidase) level, and the specific enzyme expression level were increased from 19 to 184 g/L, 18.3 to 129 U/mL, and 3.2 to 5.7 U/mg protein, respectively, in fed-batch culture of recombinant Bacillus subtilis when glucose concentration was controlled at 1 g/L as compared with those of conventional fed-batch culture. Glucose concentration of the culture broth was monitored by an automatic on-line glucose analyzer and controlled with a moving identification combined with optimal control (MICOC) strategy. When glucose concentrations were controlled at 10, 1, and 0.2 g/L, accumulated propionic acid concentrations and specific enzyme activities were 18.5, 4.4, and 0.6 g/L and 2.9, 5.7, and 7.1 U/mg protein, respectively. The addition of various concentrations of sodium propionate to the growth medium in batch cultures resulted in a drastic decrease in the growth rate with respect to propionate concentration. The propionic acid was shown to be responsible for cell growth inhibition and enzyme activity reduction in fed-batch culture. (c) 1992 John Wiley & Sons, Inc.     

不同宿主来源的重组酿酒酵母混合糖代谢比较

【目的】研究不同工业酿酒酵母宿主背景对重组酵母木糖利用效率的影响。【方法】将木糖利用途径的木糖还原酶(XR)、木糖醇脱氢酶(XDH)和木酮糖激酶(XK)编码基因串联后分别转入3株不同的工业酿酒酵母中,得到重组酵母ZQ1、ZQ5和ZQ7。分别对3个木糖途径代谢基因的表达水平、酶活和重组菌株的木糖发酵效率进行比较。【结果】重组菌株在木糖代谢基因转录、酶活性和木糖利用性能方面有很大差异,其中ZQ5木糖代谢能力最强,ZQ7其次,ZQ1木糖利用能力最弱。ZQ7在初始木糖浓度为20 g/L时木糖利用速率快于ZQ5,表明木糖浓度对重组菌发酵性能评价具有影响。【结论】不同菌株的遗传背景和木糖浓度对重组菌木糖利用的影响很大,评价重组酵母的木糖利用需考虑宿主的遗传背景和底物浓度的影响。     

调控酿酒酵母类异戊二烯合成途径强化芳樟醇合成

芳樟醇是一种重要单萜,广泛应用于食品、医药、日化等工业领域.然而芳樟醇在植物中含量低且难提取,限制了其大规模生产.目前通常以酿酒酵母Saccharomyces cerevisiae作为单萜生物合成宿主,其内源类异戊二烯合成途径提供合成单萜物质的前体——香叶基二磷酸(GPP).由于该途径代谢通量较低,导致GPP供应不足,极大地降低了异源单萜的合成效率.为了调节该途径的代谢通量,构建酿酒酵母整合表达载体pRS305-tHMG1和游离表达载体pYLIS-IDI1,并分别转入酿酒酵母CEN.PK2-lC中,获得酿酒酵母工程菌LS01和LS02.同时将载体pYLIS-IDIl转入酿酒酵母工程菌LS01中,构建酿酒酵母工程菌LS03.GC-MS检测结果显示,通过提高异戊二烯二磷酸异构酶(IDIl)和羟甲基戊二酸单酰辅酶A(HMG-CoA)还原酶活性区域(tHMGl)的表达水平,最终使芳樟醇产量提高1.3倍至(127.71±7.68) tg/L.结果表明,通过调控类异戊二烯合成途径,强化GPP合成前体供给,可以显著提高酿酒酵母中芳樟醇的产量.     

Transcriptional repression of ADH2-regulated beta-xylanase production by ethanol in recombinant strains of Saccharomyces cerevisiae

The regulation of endo-beta-(1,4)-xylanase production by two different strains of Saccharomyces cerevisiae, each transformed with the XYN2 gene from Trichoderma reesei under control of the promoter of the alcohol dehydrogenase II (ADH2) gene of S. cerevisiae, was investigated. In batch culture, the rate of xylanase production was severely reduced by the pulse addition of 390 mmol ethanol l(-1). Pulses of 190-630 mmol ethanol l(-1) into aerobic glucose-limited steady-state continuous cultures reduced the xylanase activity about five-fold and showed that ethanol repressed the ADH2 promoter, as was evident from Northern blot analyses. Derepression of the ADH2-regulated xylanase gene occurred at ethanol concentrations below approximately 50 mmol l(-1).     

MHF组蛋白折叠复合体组分编码基因MHF1过表达对重组酿酒酵母纤维素酶生产的影响

【背景】重组酿酒酵母可用于生产多种药用蛋白和工业酶等外源蛋白,但蛋白分泌水平低是限制其异源蛋白高效生产的重要因素。异源蛋白表达和分泌过程可能会对宿主细胞产生多种胁迫,因此,研究胁迫响应相关基因对重组酵母异源蛋白生产的影响具有重要意义。Mhf1p是MHF组蛋白折叠复合体的组分之一,与DNA损伤修复及维持基因组稳定性有关,但其对异源蛋白生产的作用尚不清楚。【目的】研究MHF1过表达对重组酿酒酵母蛋白生产的影响。【方法】在分泌表达纤维素酶的重组酿酒酵母菌株中利用基于CRISPR-Cas9的基因组编辑技术整合过表达MHF1,分析其对产酶的影响,并探讨影响产酶的分子机理。【结果】与出发菌株相比,过表达MHF1菌株的外切纤维素酶CBH酶活性提高了38%。对过表达MHF1的CBH生产菌株中蛋白合成和分泌途径相关基因转录水平进行检测,发现与对照菌株相比,CBH1基因和与分泌相关的SEC22、ERV29等基因在不同时间点呈现不同程度显著上调。【结论】MHF1过表达可促进酿酒酵母异源外切纤维素酶的生产,并影响外源酶基因和分泌途径基因的表达,可能通过对多基因的协同表达影响促进产酶。     

Role of gamma-glutamyltranspeptidase in detoxification of xenobiotics in the yeasts Hansenula polymorpha and Saccharomyces cerevisiae

GGT1 gene of the methylotrophic yeast Hansenula polymorpha appears to be a structural and functional homologue of Saccharomyces cerevisiae CIS2/ECM38 gene encoding gamma-glutamyltranspeptidase (gammaGT). This is confirmed by the absence of the corresponding activity of gammaGT in the mutant with disrupted GGT1 gene. It was shown that gammaGT of both H. polymorpha and S. cerevisiae are involved in detoxification of electrophilic xenobiotics, as the corresponding mutants appeared to be defective in the disappearance of the fluorescent vacuolar complex of GSH with xenobiotic bimane and the further diffuse distribution of this complex in the cytosol. We hypothesize that metabolism of electrophilic xenobiotics in the yeasts H. polymorpha and S. cerevisiae occurs through a gammaGT-dependent mercapturic acid pathway of GSH-xenobiotic detoxification, similar to that known for mammalian cells, with cysteine-xenobiotics and/or N-acetylcysteine-xenobiotics as the end products.     

Cellulosic alcoholic fermentation using recombinant Saccharomyces cerevisiae engineered for the production of Clostridium cellulovorans endoglucanase and Saccharomycopsis fibuligeraβ-glucosidase

In this study, Saccharomyces cerevisiae was engineered for simultaneous saccharification and fermentation of cellulose by the overexpression of the endoglucanase D (EngD) from Clostridium cellulovorans and the β-glucosidase (Bgl1) from Saccharomycopsis fibuligera . To promote secretion of the two enzymes, the genes were fused to the secretion signal of the S. cerevisiae α mating factor gene. The recombinant developed yeast could produce ethanol through simultaneous production of sufficient extracellular endoglucanase and β-glucosidase. When direct ethanol fermentation from 20 g L⁻¹β-glucan as a substrate was performed with our recombinant strains, the ethanol concentration reached 9.15 g L⁻¹ after 50 h of fermentation. The conversion ratio of ethanol from β-glucan was 80.3% of the theoretical ethanol concentration produced from 20 g L⁻¹β-glucan. In conclusion, we have demonstrated the construction of a yeast strain capable of conversion of a cellulosic substrate to ethanol, representing significant progress towards the realization of processing of cellulosic biomass in a consolidated bioprocessing configuration.