Efficient anaerobic whole cell stereoselective bioreduction with recombinant Saccharomyces cerevisiae

In this study we investigate the NADPH-dependent stereoselective reduction of the bicyclic diketone bicyclo[2.2.2]octane-2,6-dione (BCO2,6D) to the chiral ketoalcohol (1R,4S,6S)-6-hydroxybicyclo[2.2.2]octane-2-one (BCO2one6ol). Our aim was to develop a whole cell batch process for reduction of carbonyl substrates with (i) a high cosubstrate yield (formed product/consumed cosubstrate) and (ii) a high conversion rate under anaerobic conditions with Saccharomyces cerevisiae as biocatalyst and glucose as cosubstrate. Five open reading frames (ORFs), YMR226c, YDR368w, YOR120w, YGL157w, and YGL039w, encoding reductases involved in the conversion of BCO2,6D were identified using cell-free extract from strains belonging to the ExClone collection (yeast ORF expression clones; ResGen, Invitrogen Corp., UK). We report the one-step purification and characterization of three major BCO2,6D reductases, YMR226cp, YDR368wp (YPR1p), and YOR120wp (GCY1p). The reductases were overexpressed under a strong constitutive promoter and the impact on cosubstrate yield, conversion time, glucose consumption rate, and reduction rate was investigated when reductases were overexpressed either alone or in combination with low phosphoglucose isomerase activity (encoded by YBR196c). Combining overexpression of BCO2,6D reductase with reduced glycolytic rate (low phosphoglucose isomerase activity) offers a fast whole cell stereoselective bioreduction system useful for facilitated anaerobic batch conversions.     

An improved stereoselective reduction of a bicyclic diketone by Saccharomyces cerevisiae combining process optimization and strain engineering

The stereoselective reduction of the bicyclic diketone bicyclo[2.2.2]octane-2,6-dione, to the ketoalcohol (1R,4S,6S)-6-hydroxybicyclo[2.2.2]octane-2-one, was used as a model reduction to optimize parameters involved in NADPH-dependent reductions in Saccharomyces cerevisiae with glucose as co-substrate. The co-substrate yield (ketoalcohol formed/glucose consumed) was affected by the initial concentration of bicyclic diketone, the ratio of yeast to glucose, the medium composition, and the pH. The reduction of 5 g l(-1) bicyclic diketone was completed in less than 20 h in complex medium (pH 5.5) under oxygen limitation with an initial concentration of 200 g l(-1) glucose and 5 g l(-1) yeast. The co-substrate yield was further enhanced by genetically engineered strains with reduced phosphoglucose isomerase activity and with the gene encoding alcohol dehydrogenase deleted. Co-substrate yields were increased 2.3-fold and 2.4-fold, respectively, in these strains.     

Preparative Biorganic Chemistry Part 10 Asymmetric Reduction of Bicyclo[2.2.2]Octane-2,6-Diones with Baker's Yeast

Reduction of bicyclo[2.2.2]octane-2,6-dione with baker's yeast gave (lR,4S,6S)-6-hydroxybi-cyclo[2.2.2]octan-2-one (95% e.e.) contaminated with 8% of its (1S,4R,6S)-isomer. Similarly, the yeast reduction of 1-methylbicyclo[2.2.2]octane-2,6-dione furnished (1R,4S,6S)-6-hydroxy-1-methylbi-cyclo[2.2.2.]octan-2-one (99.5% e.e.) in 59% yield. The yeast reduction of 4-methylbi-cyclo[2.2.2.]octane-2,6-dione afforded (1R,4S,6S)-6-hydroxy-4-methylbicyclo[2.2.2.]octan-2-one (98% e.e.) contaminated with 3% of its (1S,4R,6S)-isomer in 58% yield.     

Identification of a Candida sp. reductase behind bicyclic exo-alcohol production

Stereoselective baker's yeast-catalysed bioreduction of bicyclo [2.2.2]octane-2,6-dione generates (1R, 4S, 6S)-6-hydroxy-bicyclo [2.2.2]octane-2-one (endo-alcohol) with high enantiomeric and diastereomeric excess. In contrast, whole cells and crude membrane fractions of Candida sp. have been reported to produce the unusual (1R, 4S, 6S)-diastereomer (exo-alcohol) as a major product. Previous in silico screening has identified seven membrane or membrane-bound reductases in C. albicans as candidates for the exo-activity. In this work, purification of the corresponding exo-reductase(s) as well as the heterologous cloning of the seven candidate genes was attempted in C. tropicalis. The overexpression of IPF4033 (AYR1) gene generated an increased exo-to-endo ratio and exo-alcohol production in whole cells and membranes of C. tropicalis. In addition, a slight increased exo-to-endo ratio was observed when overexpressing IPF4033 in S. cerevisiae, although the reduction rate and exo-to-endo ratio were several fold lower compared to those obtained with C. tropicalis.     

Biotransformations for the production of the chiral drug (S)-Duloxetine catalyzed by a novel isolate of Candida tropicalis

A yeast strain, Candida tropicalis PBR-2, isolated from soil, is capable of carrying out the enantioselective reduction of N,N-dimethyl-3-keto-3-(2-thienyl)-1-propanamine to (S)-N,N-dimethyl-3-hydroxy-3-(2-thienyl)-1-propanamine, a key intermediate in the synthesis of the chiral drug (S)-Duloxetine. The organism produced the enantiopure (S)-alcohol with a good yield (>80%) and almost absolute enantioselectivity, with an enantiomeric excess (ee) >99%. Parameters of the bioreduction reaction were optimized and the optimal temperature and pH for the reduction were found to be 30°C and 7.0, respectively. The optimized substrate and the resting cell concentration were 1 g/l and 250 g/l, respectively. The preparative-scale reaction using resting cells of C. tropicalis yielded the (S)-alcohol at 84–88% conversion and ee >99%.     

Trehalose accumulation from corn starch by Saccharomycopsis fibuligera A11 during 2-l fermentation and trehalose purification

In this study, corn starch was used as the substrate for cell growth and trehalose accumulation by Saccharomycopsis fibuligera A11. Effect of different aeration rates, agitation speeds, and concentrations of corn starch on direct conversion of corn starch to trehalose by S. fibuligera A11 were examined using a Biostat B2 2-l fermentor. We found that the optimal conditions for direct conversion of corn starch to trehalose by this yeast strain were that agitation speed was 200 rpm, aeration rate was 4.0 l/min, concentration of corn starch was 2.0% (w/v), initial pH was 5.5, fermentation temperature was 30°C. Under these conditions, over 22.9 g of trehalose per 100 g of cell dry weight was accumulated in the yeast cells, cell mass was 15.2 g/l of the fermentation medium, 0.12% (w/v) of reducing sugar, and 0.21% (w/v) of total sugar were left in the fermented medium within 48 h of the fermentation. It was found that trehalose in the yeast cells could be efficiently extracted by the hot distilled water (80°C). After isolation and purification, the crystal trehalose was obtained from the extract of the cells.     

Structural characterization of a beta-diketone hydrolase from the cyanobacterium Anabaena sp. PCC 7120 in native and product-bound forms, a coenzyme A-independent member of the crotonase suprafamily

The gene alr4455 from the well-studied cyanobacterium Anabaena sp. PCC 7120 encodes a crotonase orthologue that displays beta-diketone hydrolase activity. Anabaena beta-diketone hydrolase (ABDH), in common with 6-oxocamphor hydrolase (OCH) from Rhodococcus sp. NCIMB 9784, catalyzes the desymmetrization of bicyclo[2.2.2]octane-2,6-dione to yield [(S)-3-oxocyclohexyl]acetic acid, a reaction unusual among the crotonase superfamily as the substrate is not an acyl-CoA thioester. The structure of ABDH has been determined to a resolution of 1.5 A in both native and ligand-bound forms. ABDH forms a hexamer similar to OCH and features one active site per enzyme monomer. The arrangement of side chains in the active site indicates that while the catalytic chemistry may be conserved in OCH orthologues, the structural determinants of substrate specificity are different. In the active site of ligand-bound forms that had been cocrystallized with the bicyclic diketone substrate bicyclo[2.2.2]octane-2,6-dione was found the product of the asymmetric enzymatic retro-Claisen reaction [(S)-3-oxocyclohexyl]acetic acid. The structures of ABDH in both native and ligand-bound forms reveal further details about structural variation and modes of coenzyme A-independent activity within the crotonases and provide further evidence of a wider suprafamily of enzymes that have recruited the crotonase fold for the catalysis of reactions other than those regularly attributed to canonical superfamily members.     

Updated model of the batch acetone-butanol fermentation

Summary The recent models of the Acetone-Butanol fermentation did not adequately describe the culture inhibition by the accumulating metabolites and were unable to simulate the acidogenic culture dynamics at elevated pH levels. The present updated modification of the model features a generalised inhibition term and a pH dependent terms for intracellular conversion of undissociated acids into solvent products. The culture dynamics predictions by the developed model compared well with experimental results from an unconventional acidogenic fermentation ofC. acetobutylicum.Nomenclature A acetone concentration in the fermentation broth, [g/L] - AA total concentration of dissociated and undissociated acetic acid, [g/L] - AA _undiss concentration of undissociated acetic acid, [g/L] - APS Absolute Parameter Sensitivity - AT acetoin concentration in the fermentation broth, [g/L] - B butanol concentration in the fermentation broth, [g/L] - BA total concentration of dissociated and undissociated butyric acid, [g/L] - BA _undiss concentration of undissociated butyric acid, [g/L] - E ethanol concentration in the fermentation broth, [g/L] - f(T) inhibition function as defined in Equation (2) - k ₁ constant in Equation (4), [g substrate/g biomass] - k ₂ constant in Equation (4), [g substrate/(g biomass.h)] - k ₁ constant in Equation (5), [g substrate/(g biomass] - k ₂ constant in Equation (5), [g substrate/(g biomass.h)] - k ₃ constant in Equation (6), [g butyric acid/g substrate] - k ₄ constant in Equation (6), [g butyric acid/(g biomass.h)] - k ₅ constant in Equation (7), [g butanol/g substrate] - k ₆ constant in Equation (8), [g acetic acid/g substrate] - k ₇ constant in Equation (8), [g acetic acid/(g biomass.h)] - k ₈ constant in Equation (9), [g acetone/g substrate] - k ₉ constant in Equation (10), [g ethanol/g substrate] - k ₁₀ constant in Equation (11), [g acetoin/g substrate] - k ₁₁ constant in Equation (12), [g lactic acid/g substrate] - K _I Inhibition constant, [g inhibitory products/L] - ke maintenance energy requirement for the cell, [g substrate/(g biomass.h)] - K _AA acetic acid saturation constant, [g acetic acid/L] - K _BA butyric acid saturation constant, [g butyric acid/L] - K _S Monod's saturation constant, [g substrate/L] - LA lactic acid concentration in the fermentation broth, [g/L] - m _i ,n _i constants in Equation (14) - n empirical constant, dependent on degree of inhibition. - P concentration of inhibitory products (B+BA+AA), [g/L] - P _max maximum value of product concentration to inhibit the fermentation, [g/L] - pK_a equilibrium constant - r _A rate of acetone production, [g acetone/L.h] - r _AA rate of acetic acid production, [g acetic acid/L.h] - r _AT rate of acetoin production, [g acetoin/L.h] - r _B rate of butanol production, [g butanol/L.h] - r _BA rate of butyric acid production, [g butyric acid/L.h] - r _E rate of ethanol production, [g ethanol/L.h] - RPS Relative Parameter Sensitivity - r _LA rate of lactic acid production, [g lactic acid/L.h] - r _S dS/dt=total substrate consumption rate, [g substrate/L.h] - r _S substrate utilization rate, [g substrate/L.h] - S substrate concentration in the fermentation broth, [g substrate/L] - S ₀ initial substrate concentration, [substrate/L] - t time, [h] - X biomass concentration, [g/L] - Y _X yield of biomass with respect to substrate, [g biomass/g substrate] - Y _{P i} yield of metabolic product with respect to substrate, [g product/g substrate] Derivatives dX/dt rate of biomass production, [g biomass/L.h] - dP _i /dt rate of product formation, [g product/L.h] Greek letters specific growth rate of the culture, [h^–1] - I specific growth rate of the culture in the presence of the inhibitory products, [h^–1] - µ_max maximum specific growth rate of the culture, [h^–1]     

Comparison of engineered <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> and engineered <Emphasis Type="Italic">Escherichia coli</Emphasis> for the production of an optically pure keto alcohol

In this study, the production of enantiomerically pure (1R,4S,6S)-6-hydroxy-bicyclo[2.2.2]octane-2-one ((−)-2) through stereoselective bioreduction was used as a model reaction for the comparison of engineered Saccharomyces cerevisiae and engineered Escherichia coli as biocatalysts. For both microorganisms, over-expression of the gene encoding the NADPH-dependent aldo-keto reductase YPR1 resulted in high purity of the keto alcohol (−)-2 (>99% ee, 97–98% de). E. coli had three times higher initial reduction rate but S. cerevisiae continued the reduction reaction for a longer time period, thus reaching a higher conversion of the substrate (95%). S. cerevisiae was also more robust than E. coli, as demonstrated by higher viability during bioreduction. It was also investigated whether the NADPH regeneration rate was sufficient to supply the over-expressed reductase with NADPH. Five strains of each microorganism with varied carbon flux through the NADPH regenerating pentose phosphate pathway were genetically constructed and compared. S. cerevisiae required an increased NADPH regeneration rate to supply YPR1 with co-enzyme while the native NADPH regeneration rate was sufficient for E. coli. Nádia Skorupa Parachin and Magnus Carlquist have contributed equally to the paper.     

Fed-batch fermentation of glucose to acetate by an improved strain ofClostridium thermoaceticum

The fed-batch approach to the production of acetate from glucose by an improved strain ofClostridium thermoaceticum resulted in better performance than the batch fermentation, especially in media containing an excess (3X) of nutrients and trace salts. At pH 6.6, 46 g/l acetic acid was produced in 192 hours with 93% substrate utilization. In contrast, batch fermentation under similar conditions resulted in a maximum of 35 g/l acetic acid with less than 82% substrate utilization.     

Optimization of sorbose production from sorbitol by Gluconobacter oxydans

The basic parameters were studied influencing the conversion of orbitol to sorbose by Gluconobacter oxydans(industrial strain from FARMAKON Co., Czechoslovakia). The most effective conversion in the stationary phase was reached at pH 5.0, no inhibitory effect of sorbitol in a concentration ranging from 20 to 200 g/l and a minimum inhibitory effect of the sorbose concentration up to 200 g/l were observed. According to the optimum conditions mentioned above the optimized course of the fed-batch cultivation was proposed. The final concentration of sorbose of 410 g/l was reached after 36 hours.     

Optimization of enantioselective synthesis of methyl (R)-2-chloromandelate by whole cells of Saccharomyces cerevisiae

Methyl (R)-2-chloromandelate, a key intermediate in the synthesis of clopidogrel, was obtained by the reduction of methyl-2-chlorobenzoylformate using whole cells of Saccharomyces cerevisiae. A 100% conversion and 96.1% of enantiomeric excess (ee) value was obtained when 17 methyl-2-chlorobenzoylformate/l was reacted with 8 g S. cerevisiae/l and 83 g glucose/l at pH 7.     

Improved production of (R)-2-octanol via asymmetric reduction of 2-octanone with Oenococcus oeni CECT4730 in a biphasic system

Abstract

Oenococcus oeni CECT4730, which catalyses the asymmetric reduction of 2-octanone to (R)-2-octanol with high enantioselectivity, was further studied to exploit its potential for production of (R)-2-octanol in an aqueous/organic solvent biphasic system. Variables such as the volume ratio of aqueous to organic phase (V_a/V_o), buffer pH, reaction temperature, shaking speed, co-substrates and the ratio of biocatalyst to substrate were examined with respect to the molar conversion, the initial reaction rate and the product enantiomeric excess (e.e.). Under the optimized conditions (V_a/V_o=1:1 (v/v), buffer pH=8.0, reaction temperature=30°C, shaking speed=150 rev/min, ratio of glucose to biomass=5.4:l (w/w), ratio of biocatalyst to substrate=0.51:l (g/mol)), the highest space time yield of (R)-2-octanol, 24 mmol L^?1 per h, and >98% product e.e. were obtained at a substrate concentration close to 1.0 mol L^?1 after 24 h reduction.     

Hydrolysis of insoluble cellulose to glucose catalyzed by cellulase‐containing liposomes in an aqueous solution of 1‐butyl‐3‐methylimidazolium chloride

The liposome containing cellulase from Trichoderma viride was prepared under the condition that an appreciable amount of cellulase was incorporated in lipid membranes. The liposomal cellulase and free enzyme were examined in their hydrolytic activities to insoluble cellulose powder CC31 in the acetate buffer solution (pH 4.8) of 15 w/w% [Bmim][Cl] (1‐butyl‐3‐methylimidazolium chloride). The mean diameter and size distribution of cellulase‐containing liposome were practically unchanged under the above condition. The free cellulase was deactivated more rapidly than the liposomal cellulase in catalyzing the hydrolysis of 2.0 g/l CC31 at 45°C in the presence of [Bmim][Cl] for 48 h. The activities of liposomal and free cellulase to cellobiose as soluble substrate were less susceptible to [Bmim][Cl] than their cellulolytic activities to CC31, meaning that β‐glucosidase is relatively stable among the three enzyme components of cellulase. The rate of glucose production could be appreciably improved by the pretreatment of CC31 with [Bmim][Cl] alone at 120°C for 30 min followed by the liposomal cellulase‐catalyzed hydrolysis of the substrate at 45°C at the [Bmim][Cl] concentration of 15 w/w%. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1190–1196, 2013     

Production of poly(β-hydroxybutyric acid) and exopolysaccharide by Azotobacter beijerinckii WDN-01

The physico-chemical factors influencing the production of poly(-hydroxybutyric acid) [PHB] and exopolysaccharide (EPS) by a yellow pigmented Azotobacter beijerinckii strain WDN-01 were investigated. Under N-free condition with excess carbon, PHB accumulation attained its maximum at the late exponential phase followed by a sharp decline while EPS production was more or less parallel with growth. Polymer synthesis, however, was carbon-source-specific, the highest yield of PHB (2.73 g/l) and EPS (1.5 g/l) was obtained with 3% (w/v) glucose and mannitol respectively. Organic N-sources enhanced PHB production significantly, but inorganic nitrogenous compounds were inhibitory to both PHB and EPS synthesis. At optimum K₂HPO₄ concentration, the polymer yield was attributed to biomass yield. Oxygen-limiting conditions, irrespective of carbon sources favoured production of PHB and EPS.     

Ammonium lactate from deproteinized alfalfa juice byStreptococcus faecium

Summary Deproteinized alfalfa juice is a by-product of the mechanical fractionation of alfalfa to obtain protein. In this work the juice was used as the substrate for the production of ammonium lactate (l-lactic acid) by a strain ofStreptococcus faecium. Batch fermentation with a constant pH of 5.8 gave 27.2 g/l of lactic acid (90% conversion and 1.1 g/l/h productivity) and 6×10¹² cells/l after 24 h. Semicontinuous fermentation allowed the conversion of 3-times the volume of deproteinized juice after 44 h, finally giving 29.7 g/l of ammonium lactate (99% conversion and 2.5 g/l/h productivity) and 4–6×10¹² cells/l.     

一株耐受低pH、高浓度乳酸及琥珀酸菌株的筛选与鉴定

【目的】通过构建的人工耐酸系统,筛选耐受低pH值、乳酸及琥珀酸的菌株。【方法】构建人工耐酸系统长期驯化菌株,利用不同p H的酸性平板进行筛选,从环境中筛选出一株对低p H值、高浓度乳酸以及琥珀酸有很好耐受性的菌株。通过形态学特征、生理生化特征研究,并结合18S rDNA基因序列分析及分子系统发育树的构建结果,确定菌株的种类。【结果】经过酸性人工系统的长期驯化,筛选分离出一株耐受低pH值、高浓度乳酸以及琥珀酸的菌株WJ-2,经鉴定该菌株为酿酒酵母(Saccharomyces cerevisiae),其最适生长温度为30°C。酸性平板实验显示该菌株能够耐受pH2.5的酸性环境,同时对9%的乳酸及8%的琥珀酸也有很好的耐受性。另外,耐酸菌株WJ-2在pH 2.5、9%乳酸和8%琥珀酸的培养环境中仍能保持相对中性的细胞内pH值。【结论】通过构建人工酸性系统,成功筛选出一株对低pH值、高浓度乳酸以及琥珀酸具有耐受性的菌株——酿酒酵母菌WJ-2,该方法可为筛选具有特定耐受能力菌株提供一个新思路。     

Production of (R)-3-Chloro-1,2-Propanediol from Prochiral 1,3-Dichloro-2-Propanol by Corynebacterium sp. Strain N-1074

The production of (R)-3-chloro-1,2-propanediol [(R)-MCP] from prochiral 1,3-dichloro-2-propanol (DCP) was examined with a bacterial strain identified as a Corynebacterium strain. The addition of glycerol as a carbon source or some chlorinated alcohols to a medium was effective for the induction of activity catalyzing the transformation of DCP into MCP. The optimum pH for (R)-MCP production by the resting cell reaction was around 8.0. The optical purity of (R)-MCP formed was improved by keeping the level of DCP in the reaction mixture at a low concentration. (R)-MCP was obtained from 77.5 mM DCP with a 97.3% molar conversion yield and an 83.8% enantiomeric excess of its optical purity by periodic feeding of the substrate.     

The effect of pH,temperature and sucrose concentration on high productivity continuous ethanol fermentation using Zymomonas mobilis

Summary A flocculent strain of Zymomonas mobilis was used for ethanol production from sucrose. Using a fermentor with cell recycle (internal and external settler) high sugar conversion and ethanol productivity were obtained. At a dilution rate of 0.5 h^-1 (giving 96% sugar conversion) the ethanol productivity, yield and concentrations respectively were 20 g/l/h, 0.45 g/g and 40 g/l using a medium containing 100 g/l sucrose. At a sucrose concentration of 150 g/l, the ethanol concentration reached 60 g/l. The ethanol yield was 80% theoretical due to levan and fructo-oligomer formation. No sorbitol was detected. This fermentation was conducted at a range of conditions from 30 to 36°C and from pH 4.0 to 5.5.     

一种新型(S)-羰基还原酶的克隆及其功能表达

【目的】从近平滑假丝酵母(Candida parapsilosis CCTCC M203011)基因组中钓取新型(S)-羰基还原酶基因(scrⅡ),对其生物转化手性醇的功能进行了验证。【方法】采用PCR的方法,从C.parapsilosis基因组中扩增出一段可能的羰基还原酶基因scrⅡ。以构建的重组菌Escherichia coli BL21/pET28a-scrⅡ为生物催化剂,2-羟基苯乙酮为底物进行催化反应,经HPLC分析,计算终产物的光学纯度和产率,确定了转化反应的最适温度和pH值。【结果】scrⅡ基因全长为840bp,编码279个氨基酸,与已报道的(S)-羰基还原酶基因scr的一致性为85%。氨基酸序列分析表明SCRⅡ具有典型短链醇脱氢酶的功能域:辅酶结合区域Thr40-Gly41-(X)3-Gly45-X-Gly47和催化三联体结构Ser172-(X)n-Tyr187-(X)3-Lys191。在30℃,0.1mmol/LIPTG的诱导下,(S)-羰基还原酶(SCRⅡ)在E.coli中过量表达。以10%(w/v)的重组菌为催化剂,高浓度(6g/L)2-羟基苯乙酮为底物,在最适反应温度35℃和pH5.5的条件下,转化产物(S)-苯基乙二醇的光学纯度高达99.1%e.e.,产率为89.6%。与(S)-羰基还原酶SCR相比较,底物浓度提高了一倍,产物的光学纯度和产率分别提高了10%和28%。【结论】采用分子克隆技术分离出新型羰基还原酶SCRⅡ的编码基因,该酶的发现为手性醇的高效制备奠定了坚实的研究基础。