The proteomic response of Saccharomyces cerevisiae in very high glucose conditions with amino acid supplementation

Ethanol yield by Saccharomyces cerevisiae in very high glucose (VHG) media with an amino acid supplement was investigated. Amino acid supplementation led to positive cell responses, including reduced lag time and increased cell viability in VHG media. A quantitative shotgun proteomic analysis was used to understand how amino acid supplemented S. cerevisiae responds to high osmotic conditions. iTRAQ data revealed that most proteins involved in glycolysis and pentose phosphate pathways were up-regulated under high glucose shock. Reactivation of amino acid metabolism was also observed at the end of the lag phase. The relative abundance of most identified proteins, including aminoacyl-tRNA biosynthesis proteins, and heat-shock proteins, remained unchanged in the hours immediately following application of glucose shock. However, the expression of these proteins increased significantly at the end of the lag phase. Furthermore, the up-regulation of trehalose and glycogen biosynthesis proteins, first maintaining then latterly increasing glycolysis pathway activity was also observed. This was verified by enhanced ethanol yields at 10 and 12 h (0.43 and 0.45 g ethanol/g glucose) compared to 2 h (0.32 g ethanol/g glucose). These data combined with relevant metabolite measurements demonstrates that enhanced ethanol fermentation under VHG conditions can be achieved with the aid of amino acid supplementation.     

Proteomic analysis of calcium alginate-immobilized Saccharomyces cerevisiae under high-gravity fermentation conditions

Saccharomyces cerevisiae KAY446 cells immobilized in calcium alginate gel, and supplemented with additional amino acids, were successfully used in enhancing ethanol production. This combination succeeded in improving the ethanol yield and reducing the fermentation time. The ethanol yield under these conditions was 0.40 g of ethanol/g of glucose, with a final ethanol concentration of 118 g/L after 72 h. This is compared to yields with immobilized cells alone of 0.35 g of ethanol/g of glucose and freely suspended cells with no amino acid supplementation of 0.30 g of ethanol/g of glucose, under the same VHG conditions. The maximum specific ethanol production rates were 0.98, 0.73, and 0.61 g (g dry weight) (-1) h (-1) for immobilized cells under VHG conditions with and without amino acid supplementation and free cells, respectively. A proteomic analysis showed significant stimulation of many pathways during fermentation under these conditions, including the Ras/cAMP, glycolysis, starch, and sucrose pathways, amino acids biosynthesis, and aminoacyl-tRNA synthetases. The upregulation of ribosomal, heat-shock proteins and proteins involved in cell viability confirmed that protein biosynthesis was accelerated and revealed likely mechanisms for improving cellular viability.     

Engineering of Saccharomyces cerevisiae for efficient anaerobic alcoholic fermentation of L-arabinose

For cost-effective and efficient ethanol production from lignocellulosic fractions of plant biomass, the conversion of not only major constituents, such as glucose and xylose, but also less predominant sugars, such as l-arabinose, is required. Wild-type strains of Saccharomyces cerevisiae, the organism used in industrial ethanol production, cannot ferment xylose and arabinose. Although metabolic and evolutionary engineering has enabled the efficient alcoholic fermentation of xylose under anaerobic conditions, the conversion of l-arabinose into ethanol by engineered S. cerevisiae strains has previously been demonstrated only under oxygen-limited conditions. This study reports the first case of fast and efficient anaerobic alcoholic fermentation of l-arabinose by an engineered S. cerevisiae strain. This fermentation was achieved by combining the expression of the structural genes for the l-arabinose utilization pathway of Lactobacillus plantarum, the overexpression of the S. cerevisiae genes encoding the enzymes of the nonoxidative pentose phosphate pathway, and extensive evolutionary engineering. The resulting S. cerevisiae strain exhibited high rates of arabinose consumption (0.70 g h(-1) g [dry weight](-1)) and ethanol production (0.29 g h(-1) g [dry weight](-1)) and a high ethanol yield (0.43 g g(-1)) during anaerobic growth on l-arabinose as the sole carbon source. In addition, efficient ethanol production from sugar mixtures containing glucose and arabinose, which is crucial for application in industrial ethanol production, was achieved.     

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.     

Lactic acid production by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing a <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> lactate dehydrogenase gene

This work demonstrates the first example of a fungal lactate dehydrogenase (LDH) expressed in yeast. A L(+)-LDH gene, ldhA, from the filamentous fungus Rhizopus oryzae was modified to be expressed under control of the Saccharomyces cerevisiae adh1 promoter and terminator and then placed in a 2μ-containing yeast-replicating plasmid. The resulting construct, pLdhA68X, was transformed and tested by fermentation analyses in haploid and diploid yeast containing similar genetic backgrounds. Both recombinant strains utilized 92 g glucose/l in approximately 30 h. The diploid isolate accumulated approximately 40% more lactic acid with a final concentration of 38 g lactic acid/l and a yield of 0.44 g lactic acid/g glucose. The optimal pH for lactic acid production by the diploid strain was pH 5. LDH activity in this strain remained relatively constant at 1.5 units/mg protein throughout the fermentation. The majority of carbon was still diverted to the ethanol fermentation pathway, as indicated by ethanol yields between 0.25–0.33 g/g glucose. S. cerevisiae mutants impaired in ethanol production were transformed with pLdhA68X in an attempt to increase the lactic acid yield by minimizing the conversion of pyruvate to ethanol. Mutants with diminished pyruvate decarboxylase activity and mutants with disrupted alcohol dehydrogenase activity did result in transformants with diminished ethanol production. However, the efficiency of lactic acid production also decreased. Electronic Publication     

Candida krusei produces ethanol without production of succinic acid; a potential advantage for ethanol recovery by pervaporation membrane separation

The development of fermentative yeasts secreting no organic acids is highly desirable for ethanol production coupled with membrane separation processes, because the acidic byproduct, succinic acid, significantly inhibits the membrane permeation of ethanol. Of the Pichia and Candida yeasts tested, Candida krusei IA-1 showed the highest ethanol productivity [55 g L(-1) day(-1) from 150 g L(-1) (w/v) of glucose], comparable to the strains of Saccharomyces cerevisiae, and produced much less of the acid (0.6 g L(-1) day(-1)) than the Saccharomyces strains (1.5-1.8 g L(-1) day(-1)) under semi-aerobic conditions. Interestingly, under aerobic conditions, strain IA-1 showed no production of the acid. Stain IA-1 exhibited a good assimilation of the acid, while S. cerevisiae NBRC 0216 showed no assimilation. The activity of succinate dehydrogenase (SDH) in strain IA-1 was 37.5 mU mg(-1), and 7.8-fold higher than that in S. cerevisiae strain NBRC 0216. More significantly, SDH1 was abundantly transcribed in strain IA-1, different from that in strain NBRC 0216, regardless of the culture conditions. From these results, C. krusei IA-1 efficiently takes up succinic acid and metabolizes it in the Krebs cycle, producing an extremely low level of byproducts in the culture medium. Therefore, C. krusei is not only a promising alternative to S. cerevisiae but also a suitable model for metabolic engineering of S. cerevisiae.     

Synthesis of FAEEs from glycerol in engineered Saccharomyces cerevisiae using endogenously produced ethanol by heterologous expression of an unspecific bacterial acyltransferase

The high price of petroleum-based diesel fuel has led to the development of alternative fuels, such as ethanol. Saccharomyces cerevisiae was metabolically engineered to utilize glycerol as a substrate for ethanol production. For the synthesis of fatty acid ethyl esters (FAEEs) by engineered S. cerevisiae that utilize glycerol as substrate, heterologous expression of an unspecific acyltransferase from Acinetobacter baylyi with glycerol utilizing genes was established. As a result, the engineered YPH499 (pGcyaDak, pGupWs-DgaTCas) strain produced 0.24 g/L FAEEs using endogenous ethanol produced from glycerol. And this study also demonstrated the possibility of increasing FAEE production by enhancing ethanol production by minimizing the synthesis of glycerol. The overall FAEE production in strain YPH499 fps1Δ gpd2Δ (pGcyaDak, pGupWs-DgaTCas) was 2.1-fold more than in YPH499 (pGcyaDak, pGupWs-DgaTCas), with approximately 0.52 g/L FAEEs produced, while nearly 17 g/L of glycerol was consumed. These results clearly indicated that FAEEs were synthesized in engineered S. cerevisiae by esterifying exogenous fatty acids with endogenously produced ethanol from glycerol. This microbial system acts as a platform in applying metabolic engineering that allows the production of FAEEs from cheap and abundant substrates specifically glycerol through the use of endogenous bioethanol.     

Ethanol fermentation in a magnetically fluidized bed reactor with immobilized Saccharomyces cerevisiae in magnetic particles

Ethanol fermentation by immobilized Saccharomyces cerevisiae cells in magnetic particles was successfully carried out in a magnetically stabilized fluidized bed reactor (MSFBR). These immobilized magnetic particles solidified in a 2 % CaCl(2) solution were stable and had high ethanol fermentation activity. The performance of ethanol fermentation of glucose in the MSFBR was affected by initial particle loading rate, feed sugar concentration and dilution rate. The ethanol theoretical yield, productivity and concentration reached 95.3%, 26.7 g/L h and 66 g/L, respectively, at a particle loading rate of 41% and a feed dilution rate of 0.4 h(-1) with a glucose concentration of 150 g/L when the magnetic field intensity was kept in the range of 85-120 Oe. In order to use this developed MSFBR system for ethanol production from cheap raw materials, cane molasses was used as the main fermentation substrate for continuous ethanol fermentation with the immobilized S. cerevisiae cells in the reactor system. Molasses gave comparative ethanol productivity in comparison with glucose in the MSFBR, and the higher ethanol production was observed in the MSFBR than in a fluidized bed reactor (FBR) without a magnetic field.     

液泡蛋白酶B对酿酒酵母高温乙醇发酵效率的影响

【目的】提高酿酒酵母的高耐温性,从而提高菌株在高温下的乙醇发酵性能。【方法】利用染色体整合过表达酿酒酵母液泡蛋白酶B编码基因PRB1。【结果】在41 °C高温条件下进行乙醇发酵,过表达PRB1基因的重组酿酒酵母菌株可在31 h内消耗全部的葡萄糖,而对照菌株在相同时间内仅消耗不到一半的葡萄糖。【结论】利用蛋白酶B基因过表达可构建耐高温酿酒酵母菌株,提高在高温条件下乙醇的发酵效率。     

Effect of air supplement on the performance of continuous ethanol fermentation system

For the purpose of improving ethanol productivity, the effect of air supplement on the performance of continuous ethanol fermentation system was studied. The effect of oxygen supplement on yeast concentration, cell yield, cell viability, extracellular ethanol concentration, ethanol yield, maintenance coefficient, specific rates of glucose assimilation, ethanol production, and ethanol productivity have been evaluated, using a high alcohol tolerant Saccharomyces cerevisiae STV89 strain and employing a continuous fermentor equipped with an accurate air metering system in the flow rate range 0-11 mL air/L/h. It was found that, when a small amount of oxygen up to about 80mu mol oxygen/L/h was supplied, the ethanol productivity was significantly enhanced as compared to the productivity of the culture without any air supplement. It was also found that the oxygen supplement improved cell viability considerably as well as the ethanol tolerance level of yeast. As the air supply rate was increased, from 0 to 11 mL air/L/h while maintaining a constant dilution rate at about 0.06 h(-1), the cell concentration increased from 2.3 to 8.2 g/L and the ethanol productivity increased from 1.7 to 4.1 g ethanol/L/h, although the specific ethanol production rate decreased slightly from 0.75 to 0.5 g ethanol/g cell/h. The ethanol yield was slightly improved also with an increase in air supply rate, from about 0.37 to 0.45 ethanol/g glucose. The maintenance coefficient increased by only a small amount with the air supplement. This kind of air supplement technique may very well prove to be of practical importance to a development of a highly productive ethanol fermentation process system especially as a combined system with a high density cell culture technique.     

酿酒酵母工程菌高密度培养生产香紫苏醇

为提高酿酒酵母工程菌S7香紫苏醇产量,采用摇瓶培养,研究了其生长和代谢特点,发现产物合成与菌体生长密切关联。在3 L发酵罐中通过补料-溶氧联动控制的方式,以葡萄糖、乙醇和葡萄糖/乙醇混合物为碳源进行高密度培养,香紫苏醇产量分别达到253 mg/L、386 mg/L和408 mg/L,最高产量是摇瓶培养的27倍。说明添加乙醇作为碳源有助于香紫苏醇合成。研究结果对优化酿酒酵母细胞工厂,高效生产萜类化合物具有重要参考价值。     

Glycerol production by yeasts under osmotic and sulfite stress.

The yeasts Saccharomyces cerevisiae, Candida boidinii, Pichia augusta, and Pichia anomala were tested for glycerol production both under osmotic stress and by addition of a sulfite-steering agent. The osmotic pressure was increased by employing glucose concentrations from 50 to 200 g/L and by supplementing with NaCl (40 g/L). Of all the yeasts, S. cerevisiae exhibited the highest level of osmotolerance. The increased osmotic pressure affected glycerol formation the most in C. boidinii. In both Pichia species, glycerol formation was not sufficiently induced when exposed to sugar and salt stress. The addition of 40 g/L Na2SO3 to the medium containing 100 g/L glucose shifted the metabolism of all yeasts towards glycerol formation. Saccharomyces cerevisiae achieved 68.6%, while C. boidinii reached 25.5% of the theoretical glycerol yield, respectively. The highest glycerol yield, 82.3% of the theoretical, was produced by S. cerevisiae under microaerophilic conditions.     

混合糖发酵重组酿酒酵母的菌株构建和菊芋秸秆同步糖化发酵研究

【目的】构建可用于纤维素乙醇高效生产的混合糖发酵重组酿酒酵母菌株,并利用菊芋秸秆为原料进行乙醇发酵。【方法】筛选在木糖中生长较好的酿酒酵母YB-2625作为宿主菌,构建木糖共代谢菌株YB-2625 CCX。进一步通过r DNA位点多拷贝整合的方式,以YB-2625 CCX为出发菌株构建木糖脱氢酶过表达菌株,并筛选得到优势菌株YB-73。采用同步糖化发酵策略研究YB-73的菊芋秸秆发酵性能。【结果】YB-73菌株以90 g/L葡萄糖和30 g/L木糖为碳源进行混合糖发酵,乙醇产量比出发菌株YB-2625 CCX提高了13.9%,副产物木糖醇产率由0.89 g/g降低至0.31 g/g,下降了64.6%。利用重组菌YB-73对菊芋秸秆进行同步糖化发酵,48 h最高乙醇浓度达到6.10%(体积比)。【结论】通过转入木糖代谢途径以及r DNA位点多拷贝整合过表达木糖脱氢酶基因可有效提高菌株木糖发酵性能,并用于菊芋秸秆的纤维素乙醇生产。这是首次报道利用重组酿酒酵母进行菊芋秸秆原料的纤维素乙醇发酵。     

超高浓度培养基条件下酵母细胞生长及酒精生成的准稳态动力学研究

在1．5L搅拌式发酵罐中,使用葡萄糖质量浓度分别为120、200、280g／L的培养基进行酿酒酵母Saccharomyces cerevisiae连续发酵生成酒精的动力学研究。研究发现,当培养基中葡萄糖浓度为200和280g／L时,发酵液中残糖浓度、酒精浓度以及菌体生物量从小幅度波动的准稳态发展到大幅度波动的振荡状态。提出了伴有周期性振荡现象准稳态过程的概念,并针对该过程,建立了兼有底物和产物抑制的酵母细胞生长和产物酒精生成动力学模型。     

Fermentation of cellodextrins to ethanol using mixed-culture fermentations

The potential for enhancing ethanol production from cellodextrins by employing mixed-culture (Candida wickerhamii-Saccharomyces cerevisiae) fermentations was investigated. Initially, ethanol production was monitored in fermentation medium containing 50 g/L glucose plus 45 g/L cellobiose. Inoculum levels and times of inoculum addition were varied. Of the conditions tested, the most rapid rates of ethanol formation occurred in fermentations in which either C. wickerhamii and S. cerevisiae were coinoculated at a ratio of 57 : 1 cell/mL or in fermentations in which a 10-fold-greater S. cerevisiae inoculum was added to a pure culture C. wickerhamii fermentation after 1 day incubation. These conditions were used to attempt to enhance fermentations in which cellodextrins produced by trifluoroacetic acid hydrolysis of cellulose served as the sole carbon source. Cellodextrins that were not further purified after cellulose hydrolysis contained compounds that were slightly inhibitory to C. wickerhamii. In this case the mixed-culture fermentations produced 12-45% more ethanol than a pure culture C. wickerhamii fermentation. However, if the substrate was treated with Darco G-60 charcoal, the toxic materials were apparently removed and the pure culture C. wickerhamii fermentations performed as well as the mixed-culture fermentations.     

Ethanol production from galactose by a newly isolated Saccharomyces cerevisiae KL17

A wild-type yeast strain with a good galactose-utilization efficiency was newly isolated from the soil, and identified and named Saccharomyces cerevisiae KL17 by 18s RNA sequencing. Its performance of producing ethanol from galactose was investigated in flask cultures with media containing various combination and concentrations of galactose and glucose. When the initial galactose concentration was 20 g/L, it showed 2.2 g/L/h of substrate consumption rate and 0.63 g/L/h of ethanol productivity. Although they were about 70 % of those with glucose, such performance of S. cerevisiae KL17 with galactose was considered to be quite high compared with other strains reported to date. Its additional merit was that its galactose metabolism was not repressed by the existence of glucose. Its capability of ethanol production under a high ethanol concentration was demonstrated by fed-batch fermentation in a bioreactor. A high ethanol productivity of 3.03 g/L/h was obtained with an ethanol concentration and yield of 95 and 0.39 g/L, respectively, when the cells were pre-cultured on glucose. When the cells were pre-cultured on galactose instead of glucose, fermentation time could be reduced significantly, resulting in an improved ethanol productivity of 3.46 g/L/h. The inhibitory effects of two major impurities in a crude galactose solution obtained from acid hydrolysis of galactan were assessed. Only 5-Hydroxymethylfurfural (5-HMF) significantly inhibited ethanol fermentation, while levulinic acid (LA) was benign in the range up to 10 g/L.     

A process for the production of human proinsulin in Saccharomyces cerevisiae

In order to develop a large-scale fermentation process for the production of human proinsulin in yeast, the intra-cellular expression of a human superoxide dismutase-human proinsulin fusion product (SOD-PI) has been studied. The expression of SOD-PI in Saccharomyces cerevisiae is regulated by a hybrid alcohol dehydrogenase 2/glyceraldehyde-3-phosphate dehydrogenase promoter. The promoter is repressed by glucose and derepressed by depletion of glucose. Although the genetic stability of the construction is shown to be poor under product-inducing conditions, it is demonstrated in shake flask experiments that a stable expression potential can be maintained in a complex medium for more than 60 generations by maintaining excess glucose throughout the cultivations. These results have been confirmed in continuous cultures in chemostat and turbidostat experiments. Addition of the glucose analogs glucosamine, 2-desoxyglucose, methylglucose, and thioglucose also leads to repression of SOD-PI formation. The analogs, however, are not suitable for improving genetic stability during propagation because of growth inhibition. In batch fermentation experiments in a complex medium at 30 degrees C, it has been demonstrated that initial glucose concentrations up to 50 g/L result in high specific SOD-PI yields giving an overall yield of up to 700 mg SOD-PI/L whereas higher glucose concentrations lead to both lower specific and overall yields due to depletion of critical medium components in the production period. In fed-batch experiments at 30 degrees C it has been possible to obtain high specific SOD-PI yields even at high biomass concentrations by feeding glucose at a constant rate of 1.5 g/L/h for 40 h followed by a feeding of ethanol at 1.0 g/L/h for 24 h, thus giving an overall yield of 1200 mg/L. Decreasing the temperature from 30 to 26 degrees C leads to improved yields in batch as well as fed-batch experiments. The optimized fed-batch fermentation process which is suitable to be scaled up to the cubic meter level has been tested in 200-L fermentations resulting in yields of more than 1500 mg/L of the fusion protein which conveniently can be used as a precursor in the production of recombinant human proinsulin.     

基于差分进化算法的酿酒酵母分批补料培养在线自适应控制

酿酒酵母分批补料培养中,葡萄糖添加过量会导致乙醇大量积累,破坏细胞结构及功能,降低葡萄糖利用效率;葡萄糖添加不足会限制细胞生长。为解决这一矛盾,提出了一种基于差分进化算法的在线自适应控制策略,并利用计算机仿真方法对该策略、传统的间歇流加、分段恒速流加及PID控制策略的控制性能进行了研究和比较。结果表明,在该控制策略下,发酵液中的乙醇浓度能够被稳定地控制在1g/L的低水平,而细胞浓度却达到34.45g/L的高水平,比采用间歇流加、分段恒速流加及PID控制策略的批次分别提高了243%、18%和29%。由此可知,该自适应控制策略能够将葡萄糖流加速率控制在适宜水平,避免乙醇过量积累的同时保证细胞的快速增殖。     

Controlled expression and purification of human immune interferon from high-cell-density fermentations of Saccharomyces cerevisiae

Conditions for high-cell-density fermentations of Saccharomyces cerevisiae strains producing recombinant-DNA-derived proteins were established. Strains producing human immune interferon (IFN-gamma) from the constitutive PGK promoter failed to grow to high cell densities and exhibited low plasmid stability. Regulated expression of IFN-gamma was obtained in similar strains by employing a hybrid yeast GPD promoter that was subject to carbon source regulation due to the presence of regulatory DNA sequences from the yeast GAL 1,10 intergenic region. IFN-gamma expression programmed by this vector was low during growth on glucose and was induced by galactose. Previously defined fermentation conditions employing glucose as a carbon source were applied to this strain, resulting in high ceil densities with higher plasmid stability. Various methods of galactose induction of IFN-gamma expression in high-cell-density fermentations were investigated. Optimal conditions resulted in a 2000-fold induction and production of 2 g IFN-gamma/L fermentation culture.     

Bat2p is essential in Saccharomyces cerevisiae for fusel alcohol production on the non-fermentable carbon source ethanol

Branched-chain amino acids (BCAAs) are key substrates in the formation of fusel alcohols, important flavour components in fermented foods. The first step in the catabolic BCAA degradation is a transaminase step, catalyzed by a branched-chain amino acid transaminase (BCAAT). Saccharomyces cerevisiae possesses a mitochondrial and a cytosolic BCAAT, Bat1p and Bat2p, respectively. In order to study the impact of the BCAATs on fusel alcohol production derived from the BCAA metabolism, S. cerevisiae BCAAT-deletion mutants were constructed. The BCAA l-leucine was exogenously supplied during cultivations with mutants of S. cerevisiae. BAT1 deletion is not essential for fusel alcohol production, neither under glucose nor under ethanol growth conditions. The 3-methyl-1-butanol production rate of bat1Delta-cells on ethanol was decreased in comparison with that of wild-type cells, but the cells were still able to produce 3-methyl-1-butanol. However, drastic effects in fusel alcohol production were obtained in cells lacking BAT2. Although the constructed bat2Delta-single deletion strain and the bat1Deltabat2Delta-double deletion strain were still able to produce 3-methyl-1-butanol when grown on glucose, they were incapable of producing any 3-methyl-1-butanol when ethanol was the sole carbon source available. In the circumstances used, gene expression analysis revealed a strong upregulation of BAT2 gene activity in the wild type, when cells grew on ethanol as carbon source. Apparently, the carbon metabolism is able to influence the expression of BCAATs and interferes with the nitrogen metabolism. Furthermore, analysis of gene expression profiles shows that the expression of genes coding for other transaminases present in S. cerevisiae was influenced by the deletion of one or both BCAATs. Several transaminases were upregulated when a BCAAT was deleted. Strikingly, none of the known transaminases was significantly upregulated when BAT2 was deleted. Therefore we conclude that the expression of BAT2 is essential for 3-methyl-1-butanol formation on the non-fermentable carbon source, ethanol.