氧化葡萄糖酸杆菌生物催化1,3-丙二醇合成3-羟基丙酸

3-羟基丙酸是一种潜在的重要化工产品,可作为中间体合成多种有经济价值的工业用化合物。文中利用氧化葡萄糖酸杆菌生物催化1,3-丙二醇合成3-羟基丙酸。首先在50 mL摇瓶中(转化体系为10 mL)考察细胞加入量、底物和产物浓度等对催化反应的影响。在此基础上,在2 L鼓泡塔中(转化体系为1 L),采取适当的补料方式和生物转化与分离相耦合的手段解除抑制,以提高目标产物终浓度。结果表明:高底物和产物浓度通过降低反应初速度抑制转化的进行,并确定了最佳催化反应条件为6 g/L菌体量,pH 5.5。利用流加补料方式维持反应体系中底物浓度在15~20 g/L,经过60 h的反应,3-羟基丙酸的浓度达到60.8 g/L,生产强度为1.0g/(L.h),转化率为84.3%。采用生物转化与分离相耦合的方法,经过50 h的转化反应,3-羟基丙酸的总产量达76.3 g/L,生产强度为1.5 g/(L.h),转化率83.7%。研究结果对利用氧化葡萄糖酸杆菌的不完全氧化醇类化合物特性实现其在工业生物催化中的应用具有一定的指导意义。     

3-羟基丙酸分批发酵过程中的pH控制策略研究

本文利用重组大肠杆菌以甘油为底物发酵合成3．羟基丙酸,考察了不同pH对3．羟基丙酸产量及菌体生长的影响,发现在pH6．5条件下,细胞比生长速率达到最大值,延迟期也相对较短;而pH7．0有利于3-羟基丙酸的合成,控制pH7．0可以使3-羟基丙酸产量达到7．39g／L。基于不同pH条件下对细胞比生长速率和3-羟基丙酸比生成速率的分析,提出3．羟基丙酸分批发酵过程中的pH控制策略,即在发酵过程前5h将pH控制在6．5,5h～15h控制pH为7．0,此时有利于细胞生长;而后在15h-25h控制pH为7．5,25h后控制pH为7．0,从而使细胞具有较高的3．羟基丙酸比合成速率。在此控制策略下经过34h发酵3-羟基丙酸的终产量达到8．76g／L,比pH7．0条件下的3-羟基丙酸产量提高了18．54％。     

化学-酶法制备L-高苯丙氨酸

以苯丙酸乙酯为原料,通过正交设计优化2-氧4-苯基丁酸盐的制备条件：苯丙酸乙酯与草酸二乙酯摩尔比为1：3,缩合反应时间为2．5h,H2SO4质量分数为20％,水解反应时间为15h,优化条件下2-氧-4-苯基丁酸盐的产率为68．24％。随后,利用E．coli A5所产的天冬氨酸转氨酶为生物催化剂制备L-高笨丙氨酸。酶转化反应的最适条件为：游离细胞体系pH、温度、底物质量浓度和细胞质量浓度分别为8．5、37℃、20g/L和30g／L;而固定化细胞体系则分别为7．0—9．0、40℃、10g／L和30g/L。采用廉价的L-谷氨酸（L—Glu）作为氨基供体,添加表面活性剂有利于提高L-HPA产率。通过研究固定化细胞转化反应进程,结果发现8h内90％的底物可转化为L—HPA。     

（S）-（-）-β-羟基苯丙酸乙酯的微生物法合成

采用酿酒酵母CGMCC No．2266菌体,不对称还原β-羰基苯丙酸乙酯制备光学纯（S）-（-）-β-羟基苯丙酸乙酯。结果表明：采用初始pH为8．0的液体发酵培养基培养的CGMCCNo．2266菌体经过50℃预热处理30min后用于生物转化获得的（S）-（-）-G-羟基苯丙酸乙酯对映体过剩值可以达到100％ee。确定了合成（S）-（-）-β-羟基苯丙酸乙酯的较佳转化条件为pH7．0,温度30℃,转化时间24h,底物浓度为3．63mmol／L,菌体用量为86g/L（干重／反应体积）。以10％葡萄糖为辅助底物,产率比不加辅助底物时提高了75．4％。在最佳转化条件下反应转化率及（S）-（-）-β-羟基苯丙酸乙酯对映体过剩值可分别达到98．4％和100％ee。     

牛瘤胃分离菌株静息细胞培养体系生物转化黄豆苷原

从牛瘤胃胃液中分离了一株在厌氧条件下能利用其生长细胞将大豆异黄酮黄豆苷原高效还原为二氢黄豆苷原的革兰氏阳性细菌菌株Niu-O16。研究了菌株Niu-O16静息细胞体系转化黄豆苷原的最佳转化条件,通过单因素试验确定菌株Niu-O16静息细胞转化黄豆苷原的最佳条件是:初始pH6.0～8.0,静息细胞浓度32～64mg/mL(湿重),加入底物浓度0.8～1.2mmol/L。通过正交试验确定了静息细胞浓度、加入底物浓度及转化时间的最佳组合为:静息细胞浓度32mg/mL、加入底物浓度0.8mmol/L、转化时间24h;最佳转化条件下底物转化率最高为63.9%。该结果为厌氧菌的静息细胞转化及工业应用提供了参考。     

重组大肠杆菌生物转化甘油生产3-羟基丙酸

目的:以甘油为底物构建高效的3-羟基丙酸生产菌株。方法:以自身携带乙醛脱氢酶的E.coli BL21(DE3)plysS作为宿主,异源表达源自Klebsiella pneumoniae的甘油脱水酶基因dhaB。结果:重组菌E.coli HP获得的甘油脱水酶比活力在1.0mmol/L IPTG的诱导下达到了77.2 U/mg,摇瓶条件下,3-HP的最大产量为5.44 g/L,摩尔转化率为53%,该产量比目前报道的最高水平(4.4 g/L)提高了23.6%。结论:重组菌株E.coli HP实现了甘油向3-羟基丙酸(3-HP)的高效生物转化。     

甘油脱水酶再激活因子提高重组大肠杆菌3-羟基丙酸合成能力

甘油脱水酶是甘油转化3-羟基丙酸生物合成途径中的关键性限速酶,然而底物甘油的存在会抑制该酶的活性,从而引起3-羟基丙酸合成量的下降.因此解除底物甘油对甘油脱水酶活性的抑制作用,是提高生物合成3-羟基丙酸产量的方法之一.克隆来源于克雷伯氏菌(Klebsiella pneumoniae)的甘油脱水酶编码基因dhaB、甘油脱...     

产3-羟基丙酸重组菌的构建及其转化甘油的研究

将连接编码甘油脱水酶的基因重组质粒pEtac-dhaB和连接编码乙醛脱氢酶编码基因aldh的重组质粒pUCtac共转化大肠杆菌,得到产3-羟基丙酸重组大肠杆菌JM109(pUCtac-aldh,pEtac-dhaB),并对影响该重组菌发酵的营养因子进行研究.试验结果表明:该重组菌转化甘油合成3-羟基丙酸的适宜培养基组成为甘油40 g/L、酵母膏6 g/L、维生素B12 0.02 g/L以及KH2PO4 7.5 g/L; 3-羟基丙酸产量和转化率分别达到4.92 g/L和12.3 %.     

羰基还原酶不对称还原（R）-6-氰基-5-羟基-3-羰基己酸叔丁酯

选择R-羰基还原酶和葡萄糖脱氢酶双酶,协同催化（R）-6-氰基5-羟基-3-羰基己酸叔丁酯不对称还原制备阿托伐他汀关键手性合成子6-氰基-（3R,5R）-二羟基已酸叔丁酯。转化条件优化结果显示：在不添加外源性辅酶NADP（H）、菌体用量15．0g/L、147．0g/L（R）-6-氰基-5-羟基-3-羰基己酸叔丁酯、128．2g／L葡萄糖,30℃、pH6．5条件下反应6h后,底物转化率达到100％,产物d．e．值大于99．5％。     

S-苯乙醇高产菌株的筛选及鉴定

以苯乙酮为底物,从成都某化工厂污水池及其附近土壤中分离到224株可将苯乙酮不对称还原成S-苯乙醇的菌株。经过多次复筛,最终获得了1株具有较高催化活性的酵母菌bs5-1。在以该菌株的静息细胞为催化剂不对称苯乙酮合成S-苯乙醇的反应中,当底物浓度为80 mmol/L、静息细胞量为0.1 g/mL、添加的辅助底物葡萄糖浓度为2%、转化体系初始pH值为6.8、转化温度为30℃的条件下,转化48 h获得的底物转化率为43.02%,产物S-苯乙醇的e.e.值为96.84%。通过对其形态学、生理生化特征及其26S rDNA D1/D2区域的分析表明,bs5-1为胶红酵母。     

An integrated process for the production of 1,3-propanediol,lactate and 3-hydroxypropionic acid by an engineered Lactobacillus reuteri

The process economy of food grade 1,3-propanediol (1,3-PD) production by GRAS organisms like Lactobacillus reuteri (L. reuteri), is negatively impacted by the low yield and use of expensive feedstocks. In order to improve the process economy, we have developed a multiproduct process involving the production of three commercially important chemicals, namely, 1,3-PD, lactate and 3-Hydroxypropionic acid (3-HP), by engineered L. reuteri. The maximum 1,3-PD and lactate titer of 41 g/L and 31 g/L, with a volumetric productivity of 1.69 g/L/h and 0.67 g/L/h were achieved, respectively. The maximum 3-HP titer of 5.2 g/L with a volumetric productivity of 1.3 g/L/h, was obtained by biotransformation using cells recovered from the repeated fed-batch process. The volumetric productivity of 1,3-PD obtained in this study is the highest ever reported for this organism. Further cost reduction can be achieved by using waste feedstocks like milk whey, biomass hydrolysate, and crude glycerol.     

Production of high amounts of 3-hydroxypropionaldehyde from glycerol by Lactobacillus reuteri with strongly increased biocatalyst lifetime and productivity

3-hydroxypropionaldehyde (3HPA) is a promising versatile substance derived from the renewable feedstock glycerol. It is a product of glycerol metabolism in Lactobacillus reuteri. Because of toxic effects, the biotechnological production is poor. In this work the biocatalyst lifetime and product formation could be drastically increased. In the established two-step process already applied, cells are grown in the first step under anaerobic conditions, and in the second step the immobilised or suspended biocatalyst is used for 3HPA-production under strict anaerobic conditions. In the first step it was possible to reach a biomass concentration of 5.5g CDW/L (OD(600)≈23.4). In the second step, normally, 3HPA accumulates to a toxic concentration and the reaction stops in less than 60min because of the interaction of 3HPA with cell components. To prevent this, the toxic product is bound to the newly found scavenger carbohydrazide to form the hydrazone. For the first time it was possible to recycle the immobilised biocatalyst for at least ten cycles (overall life time>33hours) in a repeated batch biotransformation with an overall production of 67g 3HPA. The optimal pH-value was between 6.8 and 7.2 at an optimal temperature of 40-45°C. In a single batch biotransformation with suspended resting cells it was possible to produce 150g/L 3HPA as carbohydrazone at an overall productivity of 10.7gL(-1)hours(-1). In a single fed-batch biotransformation at 45°C 138g/L glycerol was converted into 108g/L 3HPA with an overall productivity of 21.6gL(-1)hours(-1). This is the highest 3HPA concentration and productivities reported so far for the microbial production of 3HPA from glycerol.     

Use of glycerol for producing 1,3-dihydroxyacetone by Gluconobacter oxydans in an airlift bioreactor

1,3-Dihydroxyacetone can be produced by biotransformation of glycerol with glycerol dehydrogenase from Gluconobacter oxydans cells. Firstly, improvement the activity of glycerol dehydrogenase was carried out by medium optimization. The optimal medium for cell cultivation was composed of 5.6 g/l yeast extract, 4.7 g/l glycerol, 42.1 g/l mannitol, 0.5 g/l K₂HPO₄, 0.5 g/l KH₂PO₄, 0.1 g/l MgSO₄·7H₂O, and 2.0 g/l CaCO₃ with the initial pH of 4.9. Secondly, an internal loop airlift bioreactor was applied for DHA production from glycerol by resting cells of G. oxydans ZJB09113. Furthermore, the effects of pH, aeration rate and cell content on DHA production and glycerol feeding strategy were investigated. 156.3 ± 7.8 g/l of maximal DHA concentration with 89.8 ± 2.4% of conversion rate of glycerol to DHA was achieved after 72 h of biotransformation using 10 g/l resting cells at 30 °C, pH 5.0 and 1.5 vvm of aeration rate.     

Production of 3-hydroxypropionic acid from glycerol by acid tolerant Escherichia coli

The biological production of 3-hydroxypropionic acid (3-HP) has attracted significant attention because of its industrial importance. The low titer, yield and productivity, all of which are related directly or indirectly to the toxicity of 3-HP, have limited the commercial production of 3-HP. The aim of this study was to identify and select a 3-HP tolerant Escherichia coli strain among nine strains reported to produce various organic acids efficiently at high titer. When transformed with heterologous glycerol dehydratase, reactivase and aldehyde dehydrogenase, all nine E. coli strains produced 3-HP from glycerol but the level of 3-HP production, protein expression and activities of the important enzymes differed significantly according to the strain. Two E. coli strains, W3110 and W, showed higher levels of growth than the others in the presence of 25 g/L 3-HP. In the glycerol fed-batch bioreactor experiments, the recombinant E. coli W produced a high level of 3-HP at 460 ± 10 mM (41.5 ± 1.1 g/L) in 48 h with a yield of 31 % and a productivity of 0.86 ± 0.05 g/L h. In contrast, the recombinant E. coli W3110 produced only 180 ± 8.5 mM 3-HP (15.3 ± 0.8 g/L) in 48 h with a yield and productivity of 26 % and 0.36 ± 0.02 g/L h, respectively. This shows that the tolerance to and the production of 3-HP differ significantly among the well-known, similar strains of E. coli. The titer and productivity obtained with E. coli W were the highest reported thus far for the biological production of 3-HP from glycerol by E. coli.     

Elongation Factor P is Dispensable in Escherichia coli and Pseudomonas aeruginosa

3-Hydroxypropionic acid (3-HP) is a commercially important platform chemical from which a panel of chemicals can be generated. Klebsiella pneumoniae has been regarded as a promising host strain in glycerol-based 3-HP production for its exceptional ability to metabolize glycerol. Since the glycerol dissimilation mechanism governs the carbon flux distribution from glycerol, inducible strong promoters were usually employed to enhance the glycerol consumption and 3-HP production. Here, we report an alternative strategy that the native promoter of dhaB gene was applied to enhance 3-HP production in K. pneumoniae. The key enzyme genes (ald4 and dhaB) for 3-HP biosynthesis were co-expressed under this promoter. Metabolic analysis revealed that the 3-HP formation was partially coupled with cell metabolism. To optimize the production of 3-HP, the effects of glucose as energy source assistant were investigated based on the analysis of fermentation process kinetics. The highest 3-HP yield (3.77 g/L in flask) was observed upon optimized conditions. Since there were no additional inducers needed, the strategy of employing native promoter seems more feasible to industrial application. More importantly, the employment of constitutive promoter demonstrated an effective approach for decoupling the natural correlation between respiratory metabolism and glycerol dissimilation in K. pneumoniae.     

Heterologous Expression of Aldehyde Dehydrogenase from Saccharomyces cerevisiae in Klebsiella pneumoniae for 3-Hydroxypropionic Acid Production from Glycerol

3-Hydroxypropionic acid (3-HP) is a commercially valuable platform compound. Klebsiella pneumoniae has been concerned as an appropriate host for 3-HP production because of its robust capacity to metabolize glycerol. Glycerol conversion to 3-HP in K. pneumoniae comprises two successive reactions: glycerol dehydratase catalyzes glycerol to 3-hydroxypropionaldehyde (3-HPA); aldehyde dehydrogenase catalyzes 3-HPA to 3-HP. Previous studies focusing on inducible expression of aldehyde dehydrogenase have shown defects of high cost of inducer and low catalytic activity due to inclusion body. Here we show a different strategy that a native promoter in the host K. pneumoniae was used to drive the heterologous expression of aldehyde dehydrogenase gene ald4 from Saccharomyces cerevisiae. The 3-HP yield of the recombinant reached a peak of 4.23 g/L at log phase, but it decreased during later period of fermentation. Except the validation of high activity of ald4, particularly, the 3-HP formation was uncovered to be closely coupled with cell division, and the lacking of NAD and ATP at latter fermentation phase became the bottleneck for cell growth and 3-HP accumulation. Furthermore, 3-HP is postulated to be converted to 3-HPA via feedback inhibition or other metabolite via unknown mechanism. Since glycerol dissimilation is a common mechanism in a variety of bacteria, the expression strategy using native promoter and implications may provide significant insight into the metabolic engineering for 3-HP production.     

Environmental conditions during glycerol bioconversion affect 3-hydroxypropionic acid bioproduction by Limosilactobacillus reuteri DSM 17938

3-Hydroxypropionic acid (3-HP) is a platform molecule whose biological production was carried out by the bacterium Limosilactobacillus reuteri according to a two-step process: first, a growth phase in batch mode on glucose, then a glycerol bioconversion into 3-HP in fed-batch mode. With the objective of improving 3-HP bioproduction, this study aimed at defining the operating conditions during the bioconversion phase that increases the bioproduction performance. A central composite rotatable design allowed testing various pH levels and specific glycerol feeding rates. By establishing response surfaces, optimal conditions have been identified that were different depending on the considered output variable (final 3-HP quantity, 3-HP production yield and production rate). Of them, 3-HP final quantity and 3-HP production yield were maximized at pH 6.0 and at specific glycerol feeding rates of 60 and 55 mg_gly g_CDW⁻¹ h⁻¹, respectively. The specific 3-HP production rate was the highest at the upper limit of the specific substrate feeding rate (80 mg_gly g_CDW⁻¹ h⁻¹) but was not affected by the pH. An additional experiment was carried out at pH 6.0 and a specific glycerol feeding rate of 80 mg_gly g_CDW⁻¹ h⁻¹ to validate the previous observations. In conclusion, the results showed a significant improvement of 3-HP concentration by 13%, of specific production rate by 34% and of 3-HP volumetric productivity by 39%, as compared to the initial values.