Continuous production of gluconic acid by immobilized Gluconobacter oxydans cell bioreactor

Summary Living Gluconobacter oxydans cells were attached on fibrous nylon carrier. Free gluconic acid was directly continuously produced in an aerated tubular immobilized-cell bioreactor for at least 6 months, with a volumetric productivity of at least 5 g/lh at 100 g/l substrate glucose and about 80 g/l product gluconic acid concentrations. The highest volumetric productivity in respect to glucose concentration was obtained with 175 g/l glucose, with about 120 g/l product gluconic acid level. With self-directing optimization procedure in respect to maximum product gluconic acid level, productivities as high as about 12–15 g/lh were obtained at relatively high substrate feed rate of 0.166 l/lh and relatively low aeration rate of 0.5 l/lmin. The highest glucose conversion of about 96% was obtained with a long residence time, at the lowest substrate feed rate used at a relatively low aeration rate, resulting however in a significant increase in ketogluconic acid production.     

红托竹荪菌种快速分离培养基优化

通过对红托竹荪快速分离培养基优化,提高红托竹荪菌种分离与评价效率。采用响应面分析法,以菌种生长速度为响应值拟合二次多元回归方程,确定培养基配方;测定优化培养基与PDA对照培养基菌丝生长速度和菌丝直径,以菌丝形态、锁状联合和菌落形态等指标评价优化培养基;测定优化培养基与PDA培养基培养菌丝在木屑培养基中菌丝生长速度,验证应用效果。通过试验,筛选出快速分离培养基配方为葡萄糖20.71 g/L、全麦粉8.36 g/L、玉米粉8.07 g/L、琼脂粉18.00 g/L、木屑水1.06 L。快速分离培养基与PDA培养基对比,培养的菌落直径平均增加66.25%,快速分离培养基菌丝日平均生长速度增加33.33%,木屑培养基菌丝日平均生长速度增加44.22%。由于优化培养基中含有淀粉、纤维素等有效成分,其刺激了菌种分泌淀粉酶、纤维素酶等,维持了胞外酶系的完整性。还可根据菌丝培养基过程形成的透明圈大小判定菌种胞外酶产生能力,达到快速评价菌种质量,保障菌种质量的目的。     

Improved production of curdlan with concentrated cells ofAgrobacterium sp.

The addition of a limited concentration of yeast extract to a minimal salt medium (MSM) enhanced cell growth and increased the production of curdlan whereas nitrogenlimitation was found to be essential for the higher production of curdlan byAgrobacterium sp. ATCC 31749. As the amount of the inoculum increased, the cell growth as well as the production of curdlan also increased in the MSM without a nitrogen source. The cell growth and production of curdlan increased as the initial pH of the medium decreased as low as 5.0. The conversion rate and concentration of curdlan from 2% (w/v) glucose in the MSM with concentrated cells under nitrogen deletion was 67% and 13.4 g/L, respectively. The highest conversion rate of curdlan under the conditions optimized in this study was 71% when the glucose concentration was 1% (w/v).     

Lipid accumulation in an oleaginous yeast (Candida 107) growing on glucose in single-stage continuous culture.

Lipid accumulation of Candida 107, grown at dilution rates from 0.03 to the maximum of 0.21/h, with carbon, nitrogen, phosphate, and magnesium limitations in a chemostat, was maximal at about 40% (wt/wt) with nitrogen-limited medium at a dilution rate of 0.06/h, giving an efficiency of substrate conversion of 22 g of lipid per g of glucose consumed. At higher dilution rates the lipid content decreased. With carbon-limited growth, the highest lipid content (14%, wt/wt) was at the maximum dilution rate. High lipid contents also occurred with phosphate + nitrogen as double limitations of growth, with the lipid content of the yeast (about 35%, wt/wt) continuing to be near maximum at dilution rates also near maximum (0.17/h), thus giving the highest specific rate of lipid formation of any growth conditions (0.59 g of lipid/g of yeast per h). However, the efficiency of substrate utilization was only 5.2 g of lipid formed per 100 g of glucose consumed. The composition of the fatty acyl residues within the lipid remained constant over many weeks if the steady-state conditions remained unchanged. With carbon-limited growth, the degree of unsaturation of the fatty acids markedly decreased as the dilution rate was increased, but with nitrogen limitation the reverse trend was seen. In all cases, linoleic and oleic acids were the principal fatty acyl residues affected, and their relative proportions always varied in opposite directions. When magnesium was a limiting nutrient, there was a considerable increase in the proportion of myristic acid produced within the lipid. Neutral lipids (predominantly triglycerides) varied from 66 to 92% of the total lipid from carbon- and nitrogen-limited growth; phospholipids (varying from 2 to 25%) were highest in nitrogen-limited growth. The fatty acyl residues within each lipid fraction showed the same variations with changing growth rates.     

Asymmetric synthesis of (S)-ethyl-4-chloro-3-hydroxybutanoate using Candida parapsilosis ATCC 7330

Asymmetric reduction of ethyl-4-chloro-3-oxobutanoate to (S)-ethyl-4-chloro-3-hydroxybutanoate in aqueous medium by resting cells of Candida parapsilosis ATCC 7330 was optimized. The influence of culture parameters (inoculum size, inoculum age and biocatalyst harvest time) and reaction parameters (co-substrate, resting cell, pH and substrate concentrations) on the asymmetric reduction were studied. It was found that these parameters significantly influenced the rate of the asymmetric reduction. Under the optimum conditions, the final concentration of (S)-ethyl-4-chloro-3-hydroxybutanoate, enantiomeric excess and the isolated yield of (S)-ethyl-4-chloro-3-hydroxybutanoate were 1.38 M (230 g/l), >99 and 95%, respectively. The space time yield was 115 mmol/lh, which is significantly higher than other whole cell biocatalysts reported so far.     

Fermentation parameters of Peptostreptococcus productus on gaseous substrates (CO,H2/CO2)

Intrinsic growth and substrate uptake parameters were obtained for Peptostreptococcus productus, strain U-1, using carbon monoxide as the limiting substrate. A modified Monod model with substrate inhibition was used for modeling. In addition, a product yield of 0.25 mol acetate/mol CO and a cell yield of 0.034 g cells/g CO were obtained. While CO was found to be the primary substrate, P. productus is able to produce acetate from CO₂ and H₂, although this substrate could not sustain growth. Yeast extract was found to also be a growth substrate. A yield of 0.017 g cell/g yeast extract and a product yield of 0.14 g acetate/g yeast extract were obtained. In the presence of acetate, the maximum specific CO uptake rate was increased by 40% compared to the maximum without acetate present. Cell replication was inhibited at acetate concentrations of 30 g/l. Methionine was found to be an essential nutrient for growth and CO uptake by P. productus. A minimum amount of a complex medium such as yeast extract (0.01%) is, however, required.     

羰基还原酶产生菌Candida ontarioensis制备(R)-2-氯-1-(3-氯苯基)乙醇

从实验室保藏的菌株中筛选获得Candida sp.PT2A,并通过18S rRNA鉴定为安大略假单胞菌Candida on-tarioensis。对C.ontarioensis不对称还原合成(R)-2-氯-1-(3-氯苯基)乙醇的发酵产酶条件和转化条件进行优化,确定了最适的发酵产酶条件和转化条件:温度30℃,初始pH 6.5,摇床转速180 r/min,菌体质量浓度200 g/L。采用2-氯-1-(3-氯苯基)乙酮质量浓度为10 g/L时,还原反应72 h,(R)-2-氯-1-(3-氯苯基)乙醇的e.e.值为99.9%,产率为99%;底物质量浓度提高至30 g/L时,产率下降为84.3%。采用十六烷基三甲基溴化铵(CTAB)对C.ontarioensis细胞进行通透性处理(CTAB g/L,4℃下处理20 min),在30 g/L底物下反应24 h,产物的e.e.和产率分别达到99.9%和97.5%。     

Alternative pathways of glucose transport in Prevotella bryantii B(1)4(1)

Prevotella bryantii B(1)4 grew faster on glucose than mannose (0.70 versus 0.45 h(-1)), but these sugars were used simultaneously rather than diauxically. 2-deoxy-glucose (2DG) decreased the growth rate of cells that were provided with either glucose or mannose, but 2DG did not completely prevent growth. Cells grown on glucose or mannose transported both (14)C-glucose and (14)C-mannose, but cells grown on glucose had over three-fold higher rates of (14)C-glucose transport than cells grown on mannose. The (14)C-mannose transport rates of glucose- and mannose-grown cells were similar. Woolf-Augustinsson-Hofstee plots were not linear, and it appeared that the glucose/mannose/2DG carrier acted as a facilitated diffusion system at high substrate concentrations. When cultures were grown on nitrogen-deficient (excess sugar) medium, isolates had three-fold lower (14)C-glucose transport, but the (14)C-mannose transport did not change significantly. (14)C-glucose and (14)C-mannose transport rates could be inhibited by 2DG and either mannose or glucose, respectively. The (14)C-glucose transport of mannose-grown cells was inhibited more strongly by mannose and 2DG than those grown on glucose. Cells grown on glucose or mannose had similar ATP-dependent glucokinase activity, and 2DG was a competitive inhibitor (K(i)=0.75 mM). Thin layer chromatography indicated that cell extracts also had ATP-dependent mannose phosphorylation, but only a small amount of phosphorylated 2DG was detected. Glucose, mannose or 2DG were not phosphorylated in the presence of PEP. Based on these results, it appeared that P. bryantii B(1)4 had: (1) two mechanisms of glucose transport, a constitutive glucose/mannose/2DG carrier and an alternative glucose carrier that was regulated by glucose availability, (2) an ATP-dependent glucokinase that was competitively inhibited by 2DG but was unable to phosphorylate 2DG at a rapid rate, and (3) virtually no PEP-dependent glucose, mannose or 2DG phosphorylation activities.     

重组青霉素G酰化酶拆分制备（S）-邻氯苯甘氨酸

对产青霉素G酰化酶的重组枯草芽胞杆菌发酵产酶条件进行优化,确定优化后的发酵条件：可溶性淀粉10g/L、蛋白胨12g/L、酵母粉3g/L、NaCl10g,／L;pH7．5、培养温度37℃、装液量80mL（500mL三角瓶）、培养28h,青霉素G酰化酶的表达水平由最初的7．34U／mL提高至18．23U／mL。以表达青霉素G酰化酶的枯草芽胞杆菌发酵液为酶源,在水相中对映选择性催化N-苯乙酰-（R,S）-邻氯苯甘氨酸制备（S）-邻氯苯甘氨酸,当底物浓度为100mol／L时转化4h,转化率达44．2％。对底物浓度为80mmoL／L反应液中的（S）-邻氯苯甘氨酸进行分离,达到理论收率的94．29％（以N-苯乙酰-（R,S）-邻氯苯甘氨酸的0．5倍摩尔量为理论产率）,e．e．值大于99．9％。170℃条件下,N-苯乙酰-（R）-邻氯苯甘氨酸与苯乙酸共熔消旋为N-苯乙酰-（R,S）-邻氯苯甘氨酸可用于循环拆分。     

Conversion to adipocytes of a clonal bone marrow preadipocyte line (H-1/A) and fatty acid composition of the resultant adipocytes

Conversion to adipocytes and fatty acid composition were investigated in a clonal bone marrow preadipocyte line (H-1/A). The growing cells exhibited a fibroblastic appearance. After the cessation of growth, triacylglyceride (TG) synthesis in the cells increased as they incorporated precursor from the growth medium and became adipocytes. Hydrocortisone and insulin accelerated the TG synthesis in H-1/A cells in a dose-dependent manner when they were cultured in the growth medium containing 10% horse serum. The rate of conversion to adipocytes was reduced as the concentration of horse serum was decreased, and this reduction was not influenced by the addition of insulin and/or hydrocortisone. These results suggest that conversion to adipocytes of H-1/A cells is primarily dependent on some component(s) of the serum. Conversion to adipocytes of the cells may involve a process of differentiation since the conversion was completely inhibited when the cells were cultured in the presence of bromodeoxyuridine. Fatty acid composition was significantly different between adipose H-1/A cells and adipocytes derived from other marrow preadipocyte line MC3T3-G2/PA6 cells. Unsaturated fatty acids accounted for 76% of the fatty acid composition of adipose H-1/A cells; in contrast, saturated fatty acids constituted 65% of the fatty acid composition of the adipose MC3T3-G2/PA6 cells. These results suggest that there is a heterogeneity of preadipocytes in bone marrow. These two preadipocyte lines thus provide a useful tool for the study of marrow adipocytes and can also be used to analyze the hematopoietic microenvironment through studies of the effect of these cells on hematopoietic cell proliferation.     

木薯粉同步糖化发酵(SSF)产丁二酸

【目的】通过优化产琥珀酸放线杆菌GXAS137同步糖化发酵木薯粉产丁二酸的发酵培养基,提高丁二酸产量,降低生产成本。【方法】在单因素试验的基础上,先利用Plackett-Burman试验设计筛选出影响丁二酸发酵的重要参数,再采用正交试验确定重要参数的最佳水平。【结果】价格低廉玉米浆可用作氮源,影响丁二酸产量的重要参数是木薯粉、玉米浆、碱式碳酸镁和糖化酶浓度。最佳条件为(g/L):木薯粉100,玉米浆14,糖化酶2.0 AGU/g底物,碱式碳酸镁75。优化后丁二酸产量达到69.31 g/L,丁二酸得率为90.01%,生产强度为1.44 g/(L·h)。与初始条件(52.34 g/L)相比,丁二酸浓度提高了32.42%。并利用1.3 L发酵罐对SSF与SHF两种发酵工艺进行了比较,SSF丁二酸产量(72.21 g/L)远高于SHF(56.86 g/L)。【结论】产琥珀酸放线杆菌同步糖化发酵木薯粉丁二酸产量高,生产成本低,具有较好的工业化应用前景。     

Microbial production of xylitol from D-xylose using Candida tropicalis

Candida tropicalis DSM 7524 was used to produce xylitol from d-xylose. The fermentation conditions were optimized during continuous cultivation. The strain employed showed no great dependence upon temperature in a range between 30° C and 37° C. It achieved its best yield of xylitol from d-xylose at a pH value of 2.5. Such low pH values allow non sterile cultivation, which is a major economic factor. With an oxygen uptake rate of 0.8–1 ml oxygen per litre culture medium, the C. tropicalis produce xylitol at a yield of between 77% and 80% of the theoretical value. Higher yeast extract concentrations prevent the conversion of d-xylose into xylitol. d-xylose acts as a growth inhibitor in higher concentrations. The maximum xylitol yield was reached at a d-xylose concentration of around 100 g/l. In a non sterile batch culture with substrate shift 220 g/l xylitol were produced from 300 g/l d-xylose at a xylitol productivity rate of 0.37 g/(lh). In order to increase the specific yield, C. tropicalis was immobilised on porous glass and cultivated in a fluidized bed reactor. In a continuous non sterile cultivation with immobilised cells 155 g/l d-xylose produced 90–95% g/l xylitol with a productivity of 1.35 g/(lh).Mr. S. S. da Silva was a visiting scientist to the GBF. He was supported by a scholarship from the National Council of Scientific and Technological Development, Brasilia, Brazil (CNPq).We also would like to gratefully acknowledge the support of Prof. Dr. Michele Vitolo of the University of Sao Paulo, and the Centre for Biotechnology and Chemistry, Lorena, S. P. Brazil, in particular the Department of Fermentative Process.We are grateful to Prof. Rainer Jonas, head of the International Cooperation between Germany/Brazil for the helpful discussions and Dr. Heinrich Lönsdorf (GBF) for the Scanning electron micrographs.Dedicated to the 65th birthday of Prof. Dr. Fritz Wagner.     

Ethanol fermentation in an immobilized cell reactor using Saccharomyces cerevisiae

Fermentation of sugar by Saccharomyces cerevisiae, for production of ethanol in an immobilized cell reactor (ICR) was successfully carried out to improve the performance of the fermentation process. The fermentation set-up was comprised of a column packed with beads of immobilized cells. The immobilization of S. cerevisiae was simply performed by the enriched cells cultured media harvested at exponential growth phase. The fixed cell loaded ICR was carried out at initial stage of operation and the cell was entrapped by calcium alginate. The production of ethanol was steady after 24 h of operation. The concentration of ethanol was affected by the media flow rates and residence time distribution from 2 to 7 h. In addition, batch fermentation was carried out with 50 g/l glucose concentration. Subsequently, the ethanol productions and the reactor productivities of batch fermentation and immobilized cells were compared. In batch fermentation, sugar consumption and ethanol production obtained were 99.6% and 12.5% v/v after 27 h while in the ICR, 88.2% and 16.7% v/v were obtained with 6 h retention time. Nearly 5% ethanol production was achieved with high glucose concentration (150 g/l) at 6 h retention time. A yield of 38% was obtained with 150 g/l glucose. The yield was improved approximately 27% on ICR and a 24 h fermentation time was reduced to 7 h. The cell growth rate was based on the Monod rate equation. The kinetic constants (K(s) and mu(m)) of batch fermentation were 2.3 g/l and 0.35 g/lh, respectively. The maximum yield of biomass on substrate (Y(X-S)) and the maximum yield of product on substrate (Y(P-S)) in batch fermentations were 50.8% and 31.2% respectively. Productivity of the ICR were 1.3, 2.3, and 2.8 g/lh for 25, 35, 50 g/l of glucose concentration, respectively. The productivity of ethanol in batch fermentation with 50 g/l glucose was calculated as 0.29 g/lh. Maximum production of ethanol in ICR when compared to batch reactor has shown to increase approximately 10-fold. The performance of the two reactors was compared and a respective rate model was proposed. The present research has shown that high sugar concentration (150 g/l) in the ICR column was successfully converted to ethanol. The achieved results in ICR with high substrate concentration are promising for scale up operation. The proposed model can be used to design a lager scale ICR column for production of high ethanol concentration.     

The two-step biotransformation of monosodium glutamate to GABA by Lactobacillus brevis growing and resting cells

Gama-aminobutyric acid (GABA) is a natural functional amino acid. In the current study, Lactobacillus brevis TCCC13007, a high GABA-producing strain, was isolated from naturally pickled Chinese vegetables. A two-step cellular bioconversion process was established using L. brevis TCCC13007 for the production of GABA. First, L. brevis cells were grown anaerobically in 7% monosodium glutamate (MSG)-containing medium at an initial pH of 6.0 and a controlled pH of 4.6 for 16 to 66 h; approximately 38 g L(-1) of GABA was obtained after 66 h of fermentation at a conversion rate of 98.6%. In the second stage of the process, about 7.6 g L(-1) of GABA was produced three more times at a conversion rate of 92.2% using the same batch of resting cells in the substrate-containing buffer under optimized conditions. Thus, the total GABA yield reached 61 g L(-1). A model system for the biotransformation of MSG to GABA was established using L. brevis TCCC13007 resting cells. The reaction rates were found to follow the classic Michaelis-Menten equation at low substrate concentrations (<80 mM). Kinetic analysis of the biotransformation revealed that L. brevis TCCC13007 resting cells produced GABA similar to that produced by purified glutamate decarboxylase from L. brevis.     

Production of fatty acids and lipid by a Candida sp. growing on a fraction of n-alkanes predominating in tridecane

A Candida sp. was grown on a fraction of n-alkanes (dodecane 22%, tridecane 48%, tetradecane 28%) as sole carbon source. The growth rate was increased most markedly by using high concentrations of n-alkanes (16.7% v/v). When grown in a 5 liter fermentor, the yeast reached its highest yield (60 g. of cell dry wt/l) with a concomitant high yield of fatty acids (21 g of fatty acids/l), by using a nitrogen-deficient medium. To achieve good growth, it was essential to use an inoculum (1 part into 10) of rapidly growing cells and beneficial to increase the agitation rate gradually once growth had begun. After 108 hr maximum conversions of substrate to product were: 71.5% (w/w) for alkanes into cells and 24.8% (w/w) for alkanes into fatty acids. Of the, total fatty acids at the end of the fat-accumulating phase of growth 54% were shorter in chain length than palmitic acid (C₁₆H₃₂O₂). When grown on glucose, as sole carbon source, less than 2% of the total fatty acids were shorter than palmitic acid. When n-alkanes were added to cells growing on glucose, short-chain fatty acids (C₁₀ to C₁₄) were synthesized immediately, indicating a derepressed enzyme system for hydrocarbon assimilation and the absence of diauxie. The production of these acids was at the apparent sacrifice of linoleic acid synthesis. In spite of the high conversion ratios, it is concluded that it would be uneconomical to produce fatty acids, even expensive ones such as lauric acid, by microbial transformation of n-alkanes.     

Kinetics of repeated batch production of ethanol by immobilized growing yeast cells

Summary Kinetic and yield parameters for growth and ethanol production from sucrose (100 g/l) bySaccharomyces cerevisia entrapped in K-carrageenan and calcium alginate were identical to those of free cells. Cell leakage was minimum with calcium alginate gel. For the sixth batch, 4.51 g/lh ethanol productivity (94% conversion of sucrose) was obtained; 60.5 g/l of ethanol was obtained from 200 g/l sucrose with 83.2% conversion, indicating inhibition effects.     

固定化光合细菌利用有机物产氢的研究

应用固定化细胞技术包埋荚膜红假单胞菌(Rhodopseudomonas capsulata)菌株386．研究在光照下利用有机物产氢的特性。实验观察到,光照培养120小时,悬浮培养物的产氢量为68．2ml·比产氢速率为104．1ml H2/g(生物量)·h;用琼脂包埋后．其产氢能力得到改善,产氢量和比产氢速率分别达到128．4ml和l 9s．8mlH2/g·h。该菌株除可利用苹果酸外,还可利用葡萄糖、乳酸、丙酸等基质高效地产氢。基质浓度只有控制在适当水平时,才具有较高的基质转化产氢效率。此外．菌体生物量、菌龄、培养液pH、光照强度、光照／黑暗时间比以及温度对产氢过程均有不同程度的影响。     

Effects of glucose and glycerol on gamma-poly(glutamic acid) formation by Bacillus licheniformis ATCC 9945a

Bacillus licheniformis ATCC 9945a is one of the bacterial strains that produce gamma-poly(glutamic acid) (gamma-PGA). The use of carbohydrate medium components for gamma-PGA production was explored. Cells were grown in shake flasks or in controlled pH fermentors using medium formulations that contain different carbon sources. During the cultivations, aliquots were removed to monitor cell growth, carbon utilization, polymer production, and polymer molecular weight. Glucose was a better carbon source than glycerol for cell growth. Furthermore, glucose was utilized at a faster rate than glycerol, citrate, or glutamate. However, by using mixtures of glucose and glycerol in medium formulations, the efficiency of gamma-PGA production increased. For example, by increasing the glycerol in medium formulations from 0 to 40 g/L, the gamma-PGA broth concentration after 96 h increased from 5.7 to 20.5 g/L. Considering that glycerol utilization was low for the glucose/glycerol mixtures studied, it was unclear as to the mechanism by which glycerol leads to enhanced product formation. Cell growth and concomitant gamma-PGA production (12 g/L) at pH 6.5 was possible using glucose as a carbon source if trace amounts (0.5 g/L each) of citrate and glutamate were present in the medium. We suggested that citrate and glutamate were useful in preventing salt precipitation from the medium. In addition, glutamate may be preferred relative to ammonium chloride as a nitrogen source. The conversion of glucose to gamma-PGA by the strain ATCC 9945a was believed to occur by glycolysis of glucose to acetyl-CoA and tricarboxylic acid (TCA) cycle intermediates that were then metabolized via the TCA cycle to form alpha-ketoglutarate, which is a direct glutamate precursor.     

Two-stage fermentation method for production of protein-enriched feed from cassava

Studies have been carried out into the production of microbial protein from cassava using Trichoderma reesei and yeast. In monoculture studies, T. reesei was grown on whole cassava medium to give 0.74g dry cell/g cassava. The dry material contained 42% protein. The culture filtrate contained 5.8 g/l glucose, which supported the growth of yeast. Mixed culture fermentation was also carried out with the two microorganisms. Besides accelerating the rate of degradation and conversion of cassava to cells (0.85g cell/g cassava) the yeast boosted the protein content of the growth product to 51%.     

Production of (R)-1-(4-Bromo-phenyl)-ethanol by locally isolated Aspergillus niger using ram horn peptone

Aspergillus niger EBK-9 was isolated from soil sample. This isolate was evaluated for production of (R)-1-(4-Bromo-phenyl)-ethanol 2 from 1-(4-Bromo-phenyl)-ethanone 1. In this work, the production of the 2 was achieved via fermenter. Glucose, yeast extract and ram horn peptone as medium in fermenter for growth of A. niger was used. A. niger EBK-9 isolate was found to be an effective biocatalyst with excellent enantiomeric excess (>99%) and good conversion (100%) for the production of the 2 in batch culture. The 8.2 mmol/l product from 10 mmol substrate under the optimum conditions could be produced. The yield was calculated as 82%. Because of the easy availability of the fungus besides simple reaction conditions, this process and medium must be potentially useful for production of chiral alcohols.