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.     

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.     

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.     

Klebsiella pneumoniae 1,3-propanediol:NAD+ oxidoreductase.

Fermentative utilization of glycerol, a more reduced carbohydrate than aldoses and ketoses, requires the disposal of the two extra hydrogen atoms. This is accomplished by sacrificing an equal quantity of glycerol via an auxiliary pathway initiated by glycerol dehydratase. The product, 3-hydroxypropionaldehyde, is then reduced by 1,3-propanediol NAD+:oxidoreductase (1,3-propanediol dehydrogenase; EC 1.1.1.202), resulting in the regeneration of NAD+ from NADH. The pathway for the assimilation of glycerol is initiated by an NAD-linked dehydrogenase. In Klebsiella pneumoniae the two pathways are encoded by the dha regulon which is inducible only anaerobically. In this study 1,3-propanediol:NAD+ oxidoreductase was purified from cells grown anaerobically on glycerol. The enzyme was immunochemically distinct from the NAD-linked glycerol dehydrogenase and was an octamer or hexamer of a polypeptide of 45,000 +/- 3,000 daltons. When tested as a dehydrogenase, only 1,3-propanediol served as a substrate; no activity was detected with ethanol, 1-propanol, 1,2-propanediol, glycerol, or 1,4-butanediol. The enzyme was inhibited by chelators of divalent cations. An enzyme preparation inhibited by alpha,alpha'-dipyridyl was reactivated by the addition of Fe2+ or Mn2+ after removal of the chelator by gel filtration. As for glycerol dehydrogenase, 1,3-propanediol oxidoreductase is apparently inactivated by oxidation during aerobic metabolism, under which condition the enzyme becomes superfluous.     

The effects of cell recycling on the production of 1,3-propanediol by Klebsiella pneumoniae

The effects of both biomass age and cell recycling on the 1,3-propanediol (1,3-PDO) production by Klebsiella pneumoniae were investigated in a membrane-supported bioreactor using hollow-fiber ultrafiltration membrane module in two separate experiments. It was determined that older cells have a negative effect on 1,3-PDO production. The concentrations of by-products, such as acetic acid and ethanol, increased in cultures with older cells, whereas the concentrations of succinic acid, lactic acid and 2,3-butanediol decreased. The effect of cell recycling was comparatively studied at a cell recycling ratio of 100 %. The results showed that cell recycling had also negative effects on 1,3-PDO fermentation. It was hypothesized that both cell recycling and biomass age caused metabolic shifts to undesired by-products which then inhibited the 1,3-PDO production. On the other hand, the use of hollow-fiber ultrafiltration membrane module was found to be very effective in terms of removal of cells from the fermentation broth.     

一株产1，3-丙二醇的克雷伯氏菌的噬菌体生物学特性

[目的]克雷伯氏菌发酵生产1,3-丙二醇过程中发生噬菌体感染会严重影响宿主菌的生长和目标产物的生成,因此分离克雷伯氏菌噬菌体并考察其生物学特性对预防和控制噬菌体感染具有重要意义.[方法]采用敏感指示菌法及Adams双层平板法从感染噬菌体的肺炎克雷伯氏杆菌发酵液中分离得到一株噬菌体;纯化后用磷钨酸负染法电镜观察;手工法提取噬菌体核酸,酶切后琼脂糖凝胶电泳分析;同时考察了其最佳感染复数、一步生长曲线及对温度、pH、紫外线、乙醚和氯仿等理化因素的敏感性等生理特性;最后考察了噬菌体对肺炎克雷伯氏杆菌生长和发酵的影响.[结果]分离出一株肺炎克雷伯氏杆菌溶源性噬菌体,其噬菌斑为无晕环透明圆斑,直径约1.5 mm;其头部为直径约60 nm-70 nm的球体,有一长约160 nm的丝状长尾;基因组核酸能被双链DNA内切酶EcoR Ⅰ及HindⅢ切开,大小约42 kb;对高温和紫外线敏感,耐碱性而受强酸抑制,对氯仿不敏感;最佳感染复数为1,潜伏期与裂解期均为50 min,裂解量为343个;感染噬菌体的肺炎克雷伯氏杆菌的细胞生长延滞约8h,代谢流偏向乳酸途径.[结论]该噬菌体属于无包膜长尾噬菌体,能改变克雷伯氏菌发酵生产1,3-丙二醇的代谢规律,为1,3-丙二醇发酵生产过程中噬菌体感染的预防和控制研究奠定了基础.     

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.     

不同pH调节剂对补料批式发酵产1,3-丙二醇的影响

对肺炎克雷伯氏菌（Klebsiellapneumoniae）发酵生产1,3-丙二醇（1,3-Propanediol,1,3．PD）的补碱策略进行了研究。分别利用NaOH、氨水、KOH三种溶液作为pH调节剂,优化三种pH调节剂并得到按一定比例混合的混合碱。当采用混合碱调控发酵pH值为7．0时,1,3-丙二醇的产量达到了55dL,比无pH调控（对照）发酵过程发酵水平提高了10．6倍。     

Effects of different pH regulators on 1,3-propanediol production by Klebsiella pneumoniae in fed-batch culture

对肺炎克雷伯氏菌(Klebsiella pneumoniae)发酵生产1,3-丙二醇(1,3-Propanediol,1,3-PD)的补碱策略进行了研究.分别利用NaOH、氨水、KOH三种溶液作为pH调节剂,优化三种pH调节剂并得到按一定比例混合的混合碱.当采用混合碱调控发酵pH值为7.0时,1,3-丙二醇的产量达到了55 g/L,比无pH调控(对照)发酵过程发酵水平提高了10.6倍.     

Consequences of cps mutation of Klebsiella pneumoniae on 1,3-propanediol fermentation

The filtration in 1,3-propanediol (1,3-PD) downstream process is influenced by the large amounts of capsular polysaccharides (CPS) produced by Klebsiella pneumoniae CGMCC 1.6366. The morphological and fermentation properties were investigated with the CPS-deficient mutant K. pneumoniae CGMCC 1.6366 CPS. Similar biomass was obtained with CGMCC 1.6366, and the mutant strain in batch cultures indicating the cell growth was slightly inhibited by CPS defection. The viscosity of fermentation broth by mutant strain decreased by 27.45%. The flux with ceramic membrane filter was enhanced from 168.12 to 303.6 l h⁻¹ m⁻², exhibiting the great importance for downstream processing of 1,3-PD fermentation. The products spectrum of mutant isolate changed remarkably regarding to the concentration of fermentation products. The synthesis of important 1,3-PD and 2,3-butanediol was enhanced from 9.73 and 4.06 g l⁻¹ to 10.37 and 4.77 g l⁻¹ in batch cultures. The noncapsuled K. pneumoniae provided higher 1,3-PD yield of 0.54 mol mol⁻¹ than that of encapsuled wild parent in batch cultures. The fed-batch fermentation of mutant strain resulted in 1,3-PD concentration, yield, and productivity of 78.13 g l⁻¹, 0.53 mol mol⁻¹, and 1.95 g l⁻¹ h⁻¹, respectively.     

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。     

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.     

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.     

Inactivation of aldehyde dehydrogenase: a key factor for engineering 1,3-propanediol production by Klebsiella pneumoniae

Production of 1,3-propanediol (1,3-PD) from glycerol by Klebsiella pneumoniae is restrained by ethanol formation. The first step in the formation of ethanol from acetyl-CoA is catalyzed by aldehyde dehydrogenase (ALDH), an enzyme that competes with 1,3-PD oxidoreductase for the cofactor NADH. This study aimed to improve the production of 1,3-PD by engineering the ethanol formation pathway. An inactivation mutation of the aldA gene encoding ALDH in K. pneumoniae YMU2 was generated by insertion of a tetracycline resistance marker. Inactivation of ALDH resulted in a nearly abolished ethanol formation but a significantly improved 1,3-PD production. Metabolic flux analysis revealed that a pronounced redistribution of intracellular metabolic flux occurred. The final titer, the productivity of 1,3-PD and the yield of 1,3-PD relative to glycerol of the mutant strain reached 927.6 mmol L(-1), 14.05 mmol L(-1)h(-1) and 0.699 mol mol(-1), respectively, which were much higher than those of the parent strain. In addition, the specific 1,3-PD-producing capability (1,3-PD produced per gram of cells) of the mutant strain was 2-fold that of the parent strain due to a lower growth yield of the mutant. By increasing NADH availability, this study demonstrates an important metabolic engineering approach to improve the efficiency of oxidoreduction-coupled bioprocesses.     

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。     

Fermentation of glycerol to 1,3-propanediol and 2,3-butanediol by Klebsiella pneumoniae

Klebsiella pneumoniae was shown to convert glycerol to 1,3-propanediol, 2,3-butanediol and ethanol under conditions of uncontrolled pH. Formation of 2,3-butanediol starts with some hours' delay and is accompanied by a reuse of the acetate that was formed in the first period. The fermentation was demonstrated in the type strain of K. pneumoniae, but growth was better with the more acid-tolerant strain GT1, which was isolated from nature. In continuous cultures in which the pH was lowered stepwise from 7.3 to 5.4, 2,3-butanediol formation started at pH 6.6 and reached a maximum yield at pH 5.5, whereas formation of acetate and ethanol declined in this pH range. 2,3-Butanediol and acetoin were also found among the products in chemostat cultures grown at pH 7 under conditions of glycerol excess but only with low yields. At any of the pH values tested, excess glycerol in the culture enhanced the butanediol yield. Both effects are seen as a consequence of product inhibition, the undissociated acid being a stronger trigger than the less toxic diols and acid anions. The possibilities for using the fermentation type described to produce 1,3-propanediol and 2,3-butanediol almost without by-products are discussed. Received: 4 February 1998 / Received revision: 30 March 1998 / Accepted: 13 April 1998     

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...     

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。