大肠杆菌中1,3-丙二醇氧化还原酶的表达与纯化

目的:在大肠杆菌中表达1,3-丙二醇氧化还原酶(PDOR),并对PDOR进行纯化.方法:从克雷伯氏肺炎杆菌(Klebsiella pneumoniae)基因组中,克隆PDOR基因dhaT.构建表达载体pDK-dhaT,在E.coli DH5α中利用IPTG诱导进行表达.细胞裂解液利用硫酸铵盐析、Sephadex G-200凝胶层析和DE23 Cellulose阴离子交换层析,进行酶蛋白分离提纯.结果:用SDS-PAGE分析表明胞内PDOR占可溶性蛋白的39.8%,酶活为14.5U/ml.纯化后酶液比酶活提高3.94倍,回收率为15.5%.结论:成功地构建了PDOR高效表达载体,并且得到了高纯度的PDOR.     

1,3-丙二醇氧化还原酶结构与功能关系的探讨

用生物信息学方法对来源于klebsiella pneumonide的1,3-丙二醇氧化还原酶(即1,3-丙二醇氧化还原酶,PDOR)进行高级结构模建,并搜索其功能位点,以所得三维结构为对象,定位其铁信号结合位点、辅酶NADP大致位置以及可能的底物结合部位;在此基础上模拟PDOR活性部位,探讨该酶的构效关系。     

代谢工程改造克雷伯氏菌生产1,3-丙二醇

1,3-丙二醇是生产聚对苯二甲酸丙二醇酯(polytrimethylene terephthalate, PTT)的重要单体,目前主要通过微生物发酵法生产,但这种方法生产效率低下,限制了1,3-丙二醇的高效生物制造。为解决这一问题,本研究首先利用常压室温等离子(atmospheric room temperature plasma, ARTP)诱变技术,经过高通量筛选,成功获得了一株具有较高渗透压耐受性的菌株,其1,3-丙二醇产量达87 g/L。在此基础上,进一步筛选出了适合克雷伯氏菌的基因表达元件,并通过代谢工程改造,阻断冗余代谢支路(敲除ldhA、budA、aldA基因),同时强化合成路径(过表达dhaB、yqhD基因),使得改造后的工程克雷伯氏菌的1,3-丙二醇产量提升至107 g/L。最终,在5 L发酵罐中,通过优化发酵过程参数,最优工程菌株KP-FMME-6的1,3-丙二醇产量达到118 g/L,甘油转化率为42%,生产强度达到2.46 g/(h·L)。本研究为1,3-丙二醇的工业化生产提供了有效的借鉴和参考。     

克雷伯氏菌产1,3-丙二醇ldhA基因缺失菌株的构建

克雷伯氏菌(Klebsiella pneumonia)甘油歧化发酵生产1,3-丙二醇(1,3-PD)的过程中,乳酸是氧化途径最主要的副产物,乳酸的产生和积累,不仅限制了菌体本身的生长,而且严重影响了1,3-丙二醇的转化率。利用λRed重组技术对Klebsiella pneumonia中的酶乳酸脱氢酶基因(ldhA)进行改造。在λRed重组系统作用下,将带有300 bp的线性同源片段ldhA1-Cm-ldh A2与基因组DNA的同源重组,经过抗性筛选和PCR鉴定最终获得了ldhA基因缺失菌株K.pneumonia2-1ΔldhA。经过24 h发酵可知,乳酸最大产出浓度由原来的10.16 g/L降为0.49 g/L,1,3-PD由原来的78.83 g/L增长为85.76 g/L,甘油转化率由60.64%增长到65.97%,提高了5.33%。     

克雷伯杆菌甘油脱氢酶和1,3-丙二醇氧化还原酶的动力学机制

本研究主要对克雷伯杆菌甘油转化1,3-丙二醇代谢途径中的2个关键酶甘油脱氢酶(GDH)、1,3-丙二醇氧化还原酶(PDOR)反应机制和动力学进行了研究。首先,通过初速度和产物抑制动力学研究确定了GDH、PDOR双底物酶促反应机制为有序BiBi机制,明确了由反应物消耗到产物生成之间的历程。其次,建立了GDH、PDOR双底物酶促反应动力学模型,由动力学模型可知,在偶合反应中,如果GDH和PDOR酶量相同,GDH氧化反应成为限速反应,而辅酶I将主要以氧化型NAD+形式存在。动力学信息为酶法合成1,3-丙二醇和代谢工程研究提供理论指导。     

克雷伯肺炎杆菌1,3-丙二醇氧化还原酶基因克隆及表达条件研究

1,3-丙二醇氧化还原酶是甘油歧化为1,3-丙二醇的一种关键酶。本研究从克雷伯肺炎杆菌(Klebsiella pneumoniae)基因组中,用PCR方法克隆了其编码基因dhaT。TA克隆测序正确后,构建胞内表达载体pET-28a-dhaT和分泌表达载体pET-22b-dhaT,然后转化E.coliBL21(DE3)进行原核表达。表达部位确定、SDS-PAGE和酶活分析表明,该酶得到了高水平表达。其中使用pET-22b表达的目的蛋白大都是不溶的包涵体;而使用pET-28a表达的目的蛋白胞内可溶,占胞内可溶总蛋白的45%,占菌体总蛋白的25%。常规(30℃)诱导表达即呈现1,3-丙二醇氧化还原酶活性,但低温(20℃)14 h诱导显示3.7倍的酶活性。     

丙酮酸对肺炎克雷伯氏菌微氧发酵甘油产1,3-丙二醇的影响

微氧条件下,考察肺炎克雷伯氏菌发酵生产1,3-丙二醇过程中柠檬酸和丙酮酸对发酵过程的影响。摇瓶实验结果表明:添加柠檬酸能抑制菌体生长和1,3-丙二醇合成;丙酮酸对菌体生长和1,3-丙二醇合成有一定的促进作用。5 L发酵罐批式发酵表明:补料培养基中加入8 g/L丙酮酸,1,3-丙二醇的产量提高了约10.8%,转化率提高了约4.4%,比生长速率提高了约10.8%。上述结果初步表明,强化能量的产生能够有效促进1,3-丙二醇的合成,可以利用分子生物学手段强化丙酮酸的产生以促进1,3-丙二醇的合成。     

提高肺炎克雷伯氏菌产1,3-丙二醇的分子生物学方法研究进展

1,3-丙二醇(1,3-propanediol,1,3-PD)可用于工业合成多种化合物,包括聚酯、聚醚和聚氨酯。发酵法生产1,3-PD具有巨大潜力。本文从代谢途径分析入手,梳理了肺炎克雷伯氏菌厌氧代谢途径的相关酶及催化作用,较详细地综述了其产1,3-PD关键酶的分子改造、基因工程菌株的构建和关键酶基因表达、副产物相关代谢酶基因敲除等方面的最新进展,并展望了其今后的发展前景。     

编码1,3-丙二醇氧化还原酶基因的克隆和表达

采用PCR法克隆了巴氏梭菌（Clostridium pasteurianum）CpN86菌株编码1,3丙二醇氧化还原酶基因（dhaT基因）;完成了dhaT基因测序、表达载体构建和在大肠杆菌中表达;分离和纯化了dhaT基因表达的重组蛋白。实验结果：（1）PCR法克隆的dhaT基因和肺炎克雷伯氏菌Klebsiella pneumoniae菌株dhaT基因的序列同源性为829%;（2）dhaT基因表达蛋白的酶活为108U/mg;（3）dhaT基因表达的蛋白分子量为43kD;（4）Western blot确定了dhaT基因表达的蛋白和CpN86菌株天然蛋白有相同的抗原反应。     

D-乳酸合成阻断对肺炎克雷伯氏菌的1,3-丙二醇发酵的影响

利用Red同源重组技术,快速敲除肺炎克雷伯氏菌中的编码D-乳酸脱氢酶的两个基因——ldhA和dld,获得KG1-1和KG1-2两个突变株,并研究了敲除编码D-乳酸脱氢酶基因丧失合成D-乳酸的KG1-1菌株的1,3-PD产量和菌体生长变化,实验结果表明乳酸合成缺失对现有工艺1,3-丙二醇发酵无影响。     

Identification and utilization of a 1,3-propanediol oxidoreductase isoenzyme for production of 1,3-propanediol from glycerol in Klebsiella pneumoniae

In a previous study, we showed that 1,3-propanediol (1,3-PD) was still produced from glycerol by the Klebsiella pneumoniae mutant strain defective in 1,3-PD oxidoreductase (DhaT), although the production level was lower compared to the parent strain. As a potential candidate for another putative 1,3-PD oxidoreductase, we identified and characterized a homolog of Escherichia coli yqhD (88% homology in amino acid sequence), which encodes an alcohol dehydrogenase and is well known to replace the function of DhaT in E. coli. Introduction of multiple copies of the yqhD homolog restored 1,3-PD production in the mutant K. pneumoniae strain defective in DhaT. In addition, by-product formation was still eliminated in the recombinant strain due to the elimination of the glycerol oxidative pathway. An increase in NADP-dependent 1,3-PD oxidoreductase activity was observed in the recombinant strain harboring multiple copies of the yqhD homolog. The level of 1,3-PD production during batch fermentation in the recombinant strain was comparable to that of the parent strain; further engineering can generate an industrial strain producing 1,3-propanediol.     

Expression of 1,3-propanediol oxidoreductase and its isoenzyme in Klebsiella pneumoniae for bioconversion of glycerol into 1,3-propanediol

In the Klebsiella pneumoniae reduction pathway for 1,3-propanediol (1,3-PD) synthesis, glycerol is first dehydrated to 3-hydroxypropionaldehyde (3-HPA) and then reduced to 1,3-PD with NADH consumption. Rapid conversion of 3-HPA to 1,3-PD is one of the ways to improve the yield of 1,3-PD from glycerol and to avoid 3-HPA accumulation, which depends on enzyme activity of the reaction and the amount of reducing equivalents available from the oxidative pathway of glycerol. In the present study, the yqhD gene, encoding 3-propanediol oxidoreductase isoenzyme from Escherichia coli and the dhaT gene, encoding 3-propanediol oxidoreductase from K. pneumoniae were expressed individually and co-expressed in K. pneumoniae using the double tac promoter expression plasmid pEtac-dhaT-tac-yqhD. The three resultant recombinant strains (K. pneumoniae/pEtac-yqhD, K. pneumoniae/pEtac-dhaT, and K. pneumoniae/pEtac-dhaT-tac-yqhD) were used for fermentation studies. Experimental results showed that the peak values for 3-HPA production in broth of the three recombinant strains were less than 25% of that of the parent strain. Expression of dhaT reduced formation of by-products (ethanol and lactic acid) and increased molar yield of 1,3-PD slightly, while expression of yqhD did not enhance molar yield of 1,3-PD, but increased ethanol concentration in broth as NADPH participation in transforming 3-HPA to 1,3-PD allowed more cellular NADH to be used to produce ethanol. Co-expression of both genes therefore decreased by-products and increased the molar yield of 1,3-PD by 11.8%, by catalyzing 3-HPA conversion to 1,3-propanediol using two cofactors (NADH and NADPH). These results have important implications for further studies involving use of YqhD and DhaT for bioconversion of glycerol into 1,3-PD.     

Production of 1,3-propanediol by Klebsiella pneumoniae from glycerol broth

Broth containing 152 g glycerol l⁻¹ from Candida krusei culture was converted to 1,3-propanediol by Klebsiella pneumoniae. Residual glucose in the broth promoted growth of K. pneumoniae while acetate was inhibitory. After desalination treatment of glycerol broth by electrodialysis, the acetate in the broth was removed. A fed-batch culture with electrodialytically pretreated broth as␣substrate was developed giving 53 g 1,3-propanediol l⁻¹ with a yield of 0.41 g g⁻¹ glycerol and a productivity of 0.94 g l⁻¹ h⁻¹.     

Multi-modular engineering of 1,3-propanediol biosynthesis system in Klebsiella pneumoniae from co-substrate

Applied Microbiology and Biotechnology - 1,3-Propanediol (1,3-PDO) is a monomer for the synthesis of various polyesters. It is widely used in industries including cosmetics, solvents, and...     

High-level expression of the 1,3-propanediol oxidoreductase from klebsiella pneumoniae in escherichia coli

As one of four key enzymes in glycerol dismutation process, 1,3-propanediol oxidoreductase (EC.1.1.1.202) is important in converting glycerol to 1,3-propanediol in Klebsiella pneumoniae. The dhaT gene encoding 1,3-propanediol oxidoreductase was amplified by polymerase chain reaction (PCR) using the genome DNA of K. pneumoniae as template, and then cloned into cloning vector pMD18-T. After DNA sequence was determined, the dhaT gene was subcloned into Escherichia coli expression vector pET-22b (+) and pET-28a (+). Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) analysis revealed that both the recombinant E. coli BL21 (DE3) (pET-22b (+)-dhaT) and E. coli BL21(DE3)(pET-28a (+)-dhaT) expressed predicted 42-kDa 1,3-propanediol oxidoreductase after induced by isopropyl-β-d-thiogalactopyranoside (IPTG), and the recombinant enzyme of E. coli BL21 (DE3) (pET-28a (+)-dhaT) was mostly in soluble form, and exhibited high activity (96.8 U/mL culture). The recombinant enzyme was purified and biochemically characterized. The apparent K _m values of the enzyme for 1,3-propanediol and NAD⁺ were 8.5 and 0.21 mM, respectively. The enzyme had maximum activity at pH 9.5 and 30°C.     

1,3-Propanediol oxidoreductase production with Klebsiella pneumoniae DSM2026

We report a Klebsiella pneumoniae DSM2026 fermentation procedure for the efficient production of a key enzyme of 1,3-propanediol formation: 1,3-propanediol oxidoreductase (E.C. 1.1.1.202). The fermentation process is composed of an aerobic batch phase on glucose and glycerol and an anaerobic phase on glycerol. The role of the aerobic phase is to produce sufficiently high cell mass (12.9–14.6 g/l dry weight) and to activate the aerobic branch of the Klebsiella glycerol pathway, whereas in the anaerobic phase there is a rapid initiation of 1,3-propanediol oxidoreductase formation. A fast change from an aerobic to an anaerobic environment led to a redox imbalance, which resulted in the abrupt activation of the anaerobic branch of glycerol utilization, with the occurrence of a high 1,3-propanediol-oxidoreductase activity. A mathematical model with substrate inhibition showed that the adequate glycerol concentration for enzyme production was 14–16 g/l. The combination of the optimal substrate concentration together with the subsequent use of glucose and glycerol resulted in 90.6 ± 11.6 U enzyme activity referred to 1 l of fermentation broth and 10.3 ± 0.9 U/(1 h) productivity.     

Microbial production of 1,3-propanediol by Klebsiella pneumoniae using crude glycerol from biodiesel preparations

1,3-Propanediol (1,3-PD) was produced by Klebsiella pneumoniae using crude glycerol obtained from biodiesel production. The 1,3-PD concentration of 51.3 g/l⁻¹ on crude glycerol from alkali-catalyzed methanolysis of soybean oil was comparable to that of 53 g/l⁻¹ on crude glycerol derived from a lipase-catalyzed process. The productivities of 1.7 g l⁻¹ h⁻¹ on crude glycerol were comparable to that of 2 g l⁻¹ h⁻¹ on pure glycerol. It could be concluded that the crude glycerol could be directly converted to 1,3-PD without any prior purification.