pH对克雷伯氏菌1,3-丙二醇合成关键酶酶活及发酵特性的影响

在5 L发酵罐进行甘油脉冲流加发酵,分析了不同pH值对克雷伯氏肺炎杆菌发酵特性的影响,pH 6.5为菌体最佳生长条件,克雷伯氏肺炎杆菌合成1,3-丙二醇的产量最高。在1,3-丙二醇合成速率较大的对数中前期,进行甘油脉冲流加发酵,提高甘油浓度促进甘油脱水酶、1,3-丙二醇氧化还原酶和甘油脱氢酶活性。不同pH值的脉冲试验表明,甘油脱水酶,2,3-丁二醇脱氢酶比酶活随着pH值的升高而升高,1,3-丙二醇氧化还原酶,乳酸脱氢酶比酶活在pH6.5最高,因此偏酸性的发酵条件和对数期维持一定的甘油浓度能够促进1,3-丙二醇的合成。     

补料分批发酵过程中两阶段发酵生产1,3-丙二醇

在补料分批发酵过程中提高比生长速率不仅减少乙醇、甲酸的生成,而且提高1,3-丙二醇的得率和比生产速率.发酵后期甘油的浓度在15～26 g/L时有利于提高1,3-丙二醇的生产.采取在发酵前期控制菌体较高比生长速率和发酵后期控制适宜甘油浓度相结合的策略,有效地提高了1,3-丙二醇的生产,降低副产物乳酸和乙醇的生成.     

异源表达木糖异构酶基因对克雷伯氏菌合成1,3-丙二醇的影响

【目的】提高克雷伯氏菌胞内还原力以强化1,3-丙二醇合成。【方法】将来源于大肠杆菌的木糖异构酶基因在克雷伯氏菌中异源表达,构建重组菌。研究重组菌添加不同浓度木糖为辅底物与甘油共发酵过程中代谢产物和NADH的变化规律。【结果】与对照菌相比,重组菌细胞内还原力NADH提高了0.1?0.3倍,1,3-丙二醇产量达到23.31 g/L,提高20%,1,3-丙二醇转化率从0.60 mol/mol提高到0.73 mol/mol。【结论】木糖异构酶基因的表达强化了木糖代谢途径,经磷酸戊糖途径积累大量还原力,促进了1,3-丙二醇的生成。     

1,3-丙二醇发酵过程中乳酸抑制的研究

目的:研究乳酸对克雷伯氏肺炎杆菌(Klebsiella pneumonia)产1,3-丙二醇的影响。方法:通过在摇瓶和反应器水平下分析不同菌株(包含无乳酸、2,3-丁二醇产生的基因敲除菌)的乳酸代谢特性。结果:前期添加6 g/L的乳酸使1,3-丙二醇的产量降低了19%,而发酵10h后添加乳酸几乎不表现出抑制作用。通过对乳酸敲除菌株的代谢分析发现,发酵后期能够消耗培养基中的乳酸,这在一定程度上也反映了菌体发酵后期对乳酸的耐受性。结论:乳酸的抑制作用主要发生在1,3-丙二醇发酵的前期。解除了一株无副产物2,3-丁二醇生产株前期乳酸的过早积累后,1,3-丙二醇的的产量提高了56%。     

原生质体紫外诱变技术选育1,3-丙二醇高产菌株

以肺炎克雷伯氏杆菌(Klebsiella pneumoniae)为研究对象,应用原生质体紫外诱变技术提高其对甘油及1,3-丙二醇的耐受性,获得1,3-丙二醇高产菌.在原生质体制备过程中,运用滤膜去除酶解后细胞悬液中的正常菌体,简化菌体酶解过程,提高再生率及形成率.经过原生质体诱变后,以耐受高浓度甘油和1,3-丙二醇及高产酸能力为筛选方向,最终筛选到了3株高产菌株(Kp-1、Kp-4和Kp-5).在补料发酵实验中,上述诱变菌产1,3-丙二醇能力分别为70.24 、65.21和75.51 g/L,比野生菌株WT(55.78 g/L)分别提高了25.92%、16.91%和35.37%.     

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%。     

利用PDOR同工酶基因yqhD对产1,3-丙二醇克雷伯氏杆菌进行基因工程改造

由于Klebsiella pneumoniae 1,3-丙二醇合成途径中,加强甘油脱水酶基因表达,导致因NADH供应不足使3-羟基丙醛累积,并对菌体生长及1,3-丙二醇合成造成负面影响。为改善Klebsiella pneumoniae 1,3-丙二醇合成途径,本文利用PCR技术从大肠杆菌(Escherichia coli)中扩增出以NADPH 为辅酶的1,3-丙二醇氧化还原酶同工酶编码基因yqhD,从克雷伯氏杆菌中扩增出2.66kb的甘油脱水酶基因（dhaB）,构建了产1,3-丙二醇关键酶基因的串联载体pEtac-dhaB-tac-yqhD,并将其转入到野生克雷伯氏杆菌(Klebsiella pneumoniae)中,重组载体得到了表达。通过初步发酵,重组后的克雷伯氏杆菌产量比原始菌高20%左右,副产物中乙酸和丁二醇分别下降30%左右。     

利用克雷伯肺炎杆菌限制性底物发酵生产1，3-丙二醇

研究了克雷伯肺炎杆菌（Klebsiella pneumoniae）批式流加发酵生产1,3-丙二醇的发酵工艺,根据1,3-丙二醇的生产和菌体生长相关的特点,采用营养基质限制性流加的发酵工艺,通过控制氮源氯化铵以保持细胞稳定生长。结果表明：过低的氮源浓度,细胞生长受到限制,影响产物1,3-PD的合成;过高的氮源浓度,细胞比生长速率增加,但1,3-PD关于消耗甘油的得率降低,用于生长和维持代谢所消耗的甘油量增加。以0.41 g/(L·h)的氮源流加速率,残余氯化铵浓度在0.1 g/L时,转化率和生产强度最高。发酵25 h～28 h后,1,3-丙二醇最终浓度达到52.03 g/L,生产强度为2.04 g/(L·h),相对于甘油的摩尔转化率为0.66,分别比氮源限制前提高了28.0 ％、35.1 ％及29.4 ％。通过限制性流加氯化铵,控制细胞的比生长速率,使底物甘油有效转变为发酵的目标产物1,3-PD,有效实现产物1,3-PD的高生产强度以及对甘油的高转化率。     

丙酮酸发酵过程中光滑球拟酵母过程功能的强化

对不同葡萄糖浓度下光滑球拟酵母分批发酵生产丙酮酸的动力学模型分析发现, 葡萄糖浓度是影响光滑球拟酵母发酵生产丙酮酸过程功能的关键因素。在发酵初始阶段, 低浓度葡萄糖可维持较高的菌体比生长速率; 对数生长中前期, 葡萄糖快速进料使菌体浓度接近最大值, 并实现碳流从菌体生长转向丙酮酸积累; 对数生长后期葡萄糖浓度控制在33.4 g/L以维持高丙酮酸对葡萄糖产率系数 (0.71 g/g)。采用奇异控制的葡萄糖流加方式, 在7 L发酵罐上控制不同发酵阶段葡萄糖浓度处于最佳水平以强化光滑球拟酵母过程功能, 丙酮酸产量 (83.1 g/L)、产率 (0.621 g/g)、生产强度[1.00 g/(L·h)]与分批发酵对比, 分别提高了21.3%、21.6%和29.9%。     

克雷伯氏肺炎杆菌LDH526产1,3-丙二醇的甘油自动流加策略

1,3-丙二醇是一种重要的化工原料,主要作为平台化合物用于合成聚酯,如聚对苯二甲酸丙二醇酯。经基因工程改造的克雷伯氏肺炎杆菌LDH526能以甘油作为唯一碳源合成1,3-丙二醇,最终发酵浓度超过90 g/L。甘油浓度是影响1,3-丙二醇合成的关键因素。为了实现对甘油浓度的精确控制,设计并优化了基于发酵动力学的甘油自动流加策略。通过将底物流加速率与易观察变量p H和发酵时间偶联,实现了发酵过程中甘油流加的自启动和甘油浓度的动态控制。发酵72 h,1,3-丙二醇的浓度可稳定超过95 g/L。自动控制甘油流加的发酵过程具有可重复性、连续性以及人工工作量少的特点,有望从实验室规模扩大到生产规模。     

Physiologic mechanisms of sequential products synthesis in 1,3-propanediol fed-batch fermentation by Klebsiella pneumoniae

The glycerol fed-batch fermentation by Klebsiella pneumoniae CGMCC 1.6366 exhibited the sequential synthesis of products, including acetate, 1,3-propanediol (1,3-PD), 2,3-butanediol, ethanol, succinate, and lactate. The dominant flux distribution was shifted from acetate formation to 1,3-PD formation in early- exponential growth phase and then to lactate synthesis in late-exponential growth phase. The underlying physiological mechanism of the above observations has been investigated via the related enzymes, nucleotide, and intermediary metabolites analysis. The carbon flow shift is dictated by the intrinsic physiological state and enzymatic activity regulation. Especially, the internal redox state could serve as a rate-controlling factor for 1,3-PD production. The q(1,3-PD) formation was the combined outcomes of regulations of glycerol dehydratase activity and internal redox balancing. The q(ethanol)/q(acetate) ratios demonstrated the flexible adaptation mechanism of K. pneumoniae preferring ATP generation in early-exponential growth phase. A low PEP to pyruvate ratio corresponded LDH activity increase, leading to lactate accumulation in stationary phase.     

Microbial fed-batch production of 1,3-propanediol by Klebsiella pneumoniae under micro-aerobic conditions

The microbial production of 1,3-propanediol (1,3-PD) by Klebsiella pneumoniae under micro-aerobic conditions was investigated in this study. The experimental results of batch fermentation showed that the final concentration and yield of 1,3-PD on glycerol under micro-aerobic conditions approached values achieved under anaerobic conditions. However, less ethanol was produced under microaerobic than anaerobic conditions at the end of fermentation. The batch micro-aerobic fermentation time was markedly shorter than that of anaerobic fermentation. This led to an increment of productivity of 1,3-PD. For instance, the concentration, molar yield, and productivity of 1,3-PD of batch micro-aerobic fermentation by K. pneumoniae DSM 2026 were 17.65 g/l, 56.13%, and 2.94 g l^–1 h^–1, respectively, with a fermentation time of 6 h and an initial glycerol concentration of 40 g/l. Compared with DSM 2026, the microbial growth of K. pneumoniae AS 1.1736 was slow and the concentration of 1,3-PD was low under the same conditions. Furthermore, the microbial growth in fed-batch fermentation by K. pneumoniae DSM 2026 was faster under micro-aerobic than anaerobic conditions. The concentration, molar yield, and productivity of 1,3-PD in fed-batch fermentation under micro-aerobic conditions were 59.50 g/l, 51.75%, and 1.57 g l^–1 h^–1, respectively. The volumetric productivity of 1,3-PD under microaerobic conditions was almost twice that of anaerobic fed-batch fermentation, at 1.57 and 0.80 g l^–1 h^–1, respectively.     

Fermentation strategies for 1,3-propanediol production from glycerol using a genetically engineered Klebsiella pneumoniae strain to eliminate by-product formation

We generated a genetically engineered Klebsiella pneumoniae strain (AK-VOT) to eliminate by-product formation during production of 1,3-propanediol (1,3-PD) from glycerol. In the present study, the glycerol-metabolizing properties of the recombinant strain were examined during fermentation in a 5 L bioreactor. As expected, by-product formation was completely absent (except for acetate) when the AK-VOT strain fermented glycerol. However, 1,3-PD productivity was severely reduced owing to a delay in cell growth attributable to a low rate of glycerol consumption. This problem was solved by establishing a two-stage process separating cell growth from 1,3-PD production. In addition, nutrient co-supplementation, especially with starch, significantly increased 1,3-PD production from glycerol during fed-batch fermentation by AK-VOT in the absence of by-product formation.     

Construction and Characterization of a 1,3-Propanediol Operon

The genes for the production of 1,3-propanediol (1,3-PD) in Klebsiella pneumoniae, dhaB, which encodes glycerol dehydratase, and dhaT, which encodes 1,3-PD oxidoreductase, are naturally under the control of two different promoters and are transcribed in different directions. These genes were reconfigured into an operon containing dhaB followed by dhaT under the control of a single promoter. The operon contains unique restriction sites to facilitate replacement of the promoter and other modifications. In a fed-batch cofermentation of glycerol and glucose, Escherichia coli containing the operon consumed 9.3 g of glycerol per liter and produced 6.3 g of 1,3-PD per liter. The fermentation had two distinct phases. In the first phase, significant cell growth occurred and the products were mainly 1,3-PD and acetate. In the second phase, very little growth occurred and the main products were 1,3-PD and pyruvate. The first enzyme in the 1,3-PD pathway, glycerol dehydratase, requires coenzyme B₁₂, which must be provided in E. coli fermentations. However, the amount of coenzyme B₁₂ needed was quite small, with 10 nM sufficient for good 1,3-PD production in batch cofermentations. 1,3-PD is a useful intermediate in the production of polyesters. The 1,3-PD operon was designed so that it can be readily modified for expression in other prokaryotic hosts; therefore, it is useful for metabolic engineering of 1,3-PD pathways from glycerol and other substrates such as glucose.     

Fermentation of 1,3-propanediol by a lactate deficient mutant of Klebsiella oxytoca under microaerobic conditions

Klebsiella oxytoca M5al is an excellent 1,3-propanediol (1,3-PD) producer, but too much lactic acid yielded greatly lessened the fermentation efficiency for 1,3-PD. To counteract the disadvantage, four lactate deficient mutants were obtained by knocking out the ldhA gene of lactate dehydrogenase (LDH) of K. oxytoca M5al. The LDH activities of the four mutants were from 3.85 to 6.92% of the parental strain. The fed-batch fermentation of 1,3-PD by mutant LDH3, whose LDH activity is the lowest, was studied. The results showed that higher 1,3-PD concentration, productivity, and molar conversion rate from glycerol to 1,3-PD can be gained than those of the wild type strain and no lactic acid is produced under both anaerobic and microaerobic conditions. Sucrose fed during the fermentation increased the conversion and sucrose added at the beginning increased the productivity. In fed-batch fermentation with sucrose as cosubstrate under microaerobic conditions, the 1,3-PD concentration, conversion, and productivity were improved significantly to 83.56 g l⁻¹, 0.62 mol mol⁻¹, and 1.61 g l⁻¹ h⁻¹, respectively. Furthermore, 60.11 g l⁻¹ 2,3-butanediol was also formed as major byproduct in the broth.     

Microbial production of 1,3-propanediol

1,3-Propanediol (1,3-PD) production by fermentation of glycerol was described in 1881 but little attention was paid to this microbial route for over a century. Glycerol conversion to 1,3-PD can be carried out by Clostridia as well as Enterobacteriaceae. The main intermediate of the oxidative pathway is pyruvate, the further utilization of which produces CO₂, H₂, acetate, butyrate, ethanol, butanol and 2,3-butanediol. In addition, lactate and succinate are generated. The yield of 1,3-PD per glycerol is determined by the availability of NADH₂, which is mainly affected by the product distribution (of the oxidative pathway) and depends first of all on the microorganism used but also on the process conditions (type of fermentation, substrate excess, various inhibitions). In the past decade, research to produce 1,3-PD microbially was considerably expanded as the diol can be used for various polycondensates. In particular, polyesters with useful properties can be manufactured. A prerequisite for making a “green” polyester is a more cost-effective production of 1,3-PD, which, in practical terms, can only be achieved by using an alternative substrate, such as glucose instead of glycerol. Therefore, great efforts are now being made to combine the pathway from glucose to glycerol successfully with the bacterial route from glycerol to 1,3-PD. Thus, 1,3-PD may become the first bulk chemical produced by a genetically engineered microorganism. Received: 12 January 1999 / Received revision: 9 March 1999 / Accepted: 14 March 1999     

Improved 1,3-propanediol production with hemicellulosic hydrolysates (corn straw) as cosubstrate: Impact of degradation products on Klebsiella pneumoniae growth and 1,3-propanediol fermentation

To improve 1,3-propanediol (1,3-PD) production by an economic and efficient approach, hemicellulosic hydrolysates (HH) used as cosubstrate resulted in more biomass and higher reducing power for 1,3-PD production. The effects of primary degradation products such as individual sugars (xylose, glucose, mannose, arabinose and galactose) and major inhibitors (furfural, acetate and formate) on the Klebsiella pneumoiae growth and 1,3-PD production were investigated in this study. Xylose and mannose could efficiently promote the 1,3-PD production and cell growth. Furfural (0.28 g/l) and sodium acetate (1.46 g/l) in low concentration were not inhibitory to Klebsiella pneumoniae, rather they have stimulatory effect on the growth and 1,3-PD biosynthesis, especially the acetate. In fed-batch fermentation with HH as cosubstrate, the final 1,3-PD production, conversion from glycerol and productivity were 71.58 g/l, 0.65 mol/mol and 1.93 g/l/h, respectively, which were 17.8%, 25.0% and 17.7% higher than that from glycerol alone.     

Study of two-stage processes for the microbial production of 1,3-propanediol from glucose

The microbial production of 1,3-propanediol (1,3-PD) from glucose was studied in a two-stage fermentation process on a laboratory scale. In the first stage, glucose was converted to glycerol either by the osmotolerant yeast Pichia farinosa or by a recombinant Escherichia coli strain. In the second stage, glycerol in the broth from the first stage was converted to 1,3-PD by Klebsiella pneumoniae. The culture broth from P. farinosa was shown to contain toxic metabolites that strongly impair the growth of K. pneumoniae and the formation of 1,3-PD. Recombinant E. coli is more suitable than P. farinosa for producing glycerol in the first stage. The fermentation pattern from glycerol can be significantly altered by the presence of acetate, leading to a significant reduction of PD yield in the second stage. However, in the recombinant E. coli culture acetate formation can be prevented by fed-batch cultivation under limiting glucose supply, resulting in an effective production of 1,3-PD in the second stage with a productivity of 2.0 g l(-1) h(-1) and a high yield (0.53 g/g) close to that of glycerol fermentation in a synthetic medium. The overall 1,3-PD yield from glucose in the two stage-process with E. coli and K. pneumoniae reached 0.17 g/g.     

Change in proteomic profiles of genetically modified 1,3-propanediol-producing recombinant E. coli

The recombinant E. coli Delta6 mutant (galR, glpK, gldA, IdhA, lacI, tpiA) was used to produce 1,3-propanediol (PD) from glucose. The 1,3-PD production increased with feedback control of the glucose concentration using fed-batch fermentation. The maximum 1,3-PD concentration produced was 43 g/l after 60 h of fermentation. Glycerol production was minimized when controlling the glucose concentration at less than 1 g/l. The expression levels of seven enzymes related to the 1,3-PD production metabolism were compared during the cell growth phase and 1,3-PD production phase, and their expression levels all increased during 1,3-PD production, with the exception of alcohol dehydrogenase.