Cloning and Sequence Analysis of the dhaT Gene of the 1,3-Propanediol Regulon from Klebsiella Pneumoniae

1,3-Propanediol oxidoreductase encoded by dhaT gene, a gene of 1,3-propanediol regulon, is important in converting glycerol to 1,3-propanediol in Klebsiella pneumoniae. DhaT gene was amplified from the genome of K. pneumoniae, sequenced and its amino acid sequence deduced. A predicted secondary structure and 3D-structural model was constructed by homology modelling. Based on these results, we infer that 1,3-propanediol oxidoreductase belongs to NAD(P)-dependent alcohol dehydrogenase group III of iron-activated dehydrogenases.     

Structural and biochemical characterisation of a NAD+-dependent alcohol dehydrogenase from Oenococcus oeni as a new model molecule for industrial biotechnology applications

Alcohol dehydrogenases are highly diverse enzymes catalysing the interconversion of alcohols and aldehydes or ketones. Due to their versatile specificities, these biocatalysts are of great interest for industrial applications. The adh3-gene encoding a group III alcohol dehydrogenase was isolated from the gram-positive bacterium Oenococcus oeni and was characterised after expression in the heterologous host Escherichia coli. Adh3 has been identified by genome BLASTP analyses using the amino acid sequence of 1,3-propanediol dehydrogenase DhaT from Klebsiella pneumoniae and group III alcohol dehydrogenases with known activity towards 1,3-propanediol as target sequences. The recombinant protein was purified in a two-step column chromatography approach. Crystal structure determination and biochemical characterisation confirmed that Adh3 forms a Ni²⁺-containing homodimer in its active form. Adh3 catalyses the interconversion of ethanol and its corresponding aldehyde acetaldyhyde and is also capable of using other alcoholic compounds as substrates, such as 1,3-propanediol, 1,2-propanediol and 1-propanol. In the presence of Ni²⁺, activity increases towards 1,3-propanediol and 1,2-propanediol. Adh3 is strictly dependent on NAD⁺/NADH, whereas no activity has been observed with NADP⁺/NADPH as co-factor. The enzyme exhibits a specific activity of 1.1 U/mg using EtOH as substrate with an optimal pH value of 9.0 for ethanol oxidation and 8.0 for aldehyde reduction. Moreover, Adh3 exhibits tolerance to several metal ions and organic solvents, but is completely inhibited in the presence of Zn²⁺. The present study demonstrates that O. oeni is a group III alcohol dehydrogenase with versatile substrate specificity, including Ni²⁺-dependent activity towards 1,3-propanediol.     

Sulfate reduction and anaerobic glycerol degradation by a mixed microbial culture

Anaerobic glycerol degradation by a mixed microbial culture from a fermenter fed with industrial alcohol distillation waste water, was investigated in the absence or presence of sulfate, at 37°C and at a constant pH of 7.2. In the absence of sulfate, glycerol utilization was found to be characterized by the transient formation of 1,3-propanediol prior to propionate and acetate accumulation. In the presence of sulfate, 1,3-propanediol production was minor, and the carbon balance reflected a considerable accumulation of intermediate(s). A study of the role of sulfate reduction and methanogenesis on anaerobic 1,3-propanediol degradation showed that consumption of this substrate by the mixed microbial culture required a terminal electron acceptor. The number of fermentative and sulfate-reducing bacteria with glycerol or 1,3-propanediol as carbon and energy source revealed that sulfate-reducing bacteria outcompete fermentative bacteria for these substrates. The possible ecological role of sulfate-reducing bacteria in the metabolism of these reduced substrates is discussed.     

Ferrous-activated nicotinamide adenine dinucleotide-linked dehydrogenase from a mutant of Escherichia coli capable of growth on 1, 2-propanediol

A nicotinamide adenine dinucleotide-linked dehydrogenase has been partially purified from a mutant of Escherichia coli K-12 able to grow on l-1,2-propanediol as carbon and energy source. This enzyme catalyzes the dehydrogenation at carbon 1 of l-1,2-propanediol, glycerol, 1,3-propanediol, ethylene glycol, and ethyl alcohol. The purified protein requires added ferrous or managanous ions. The V(max) and the apparent K(m) for a given substrate vary with the particular metal used.     

甘油歧化生产1,3-丙二醇过程的代谢和基因调控机理研究进展

用生物转化法将可再生资源(如淀粉、纤维素等)转化为重要的化工原料是目前生物技术领域的一个重要课题。本文以甘油生物转化为1,3丙二醇过程为考察对象,系统综述了该过程代谢和基因调控的研究现状,并对今后的研究提出了一些建议。     

1,3-丙二醇发酵液后提取技术研究进展

1,3-丙二醇是一种重要的化工原料,以甘油或葡萄糖为原料发酵法制备1,3-丙二醇具有原料可再生、反应条件温和等优点,是近年来国内外的研究热点。由微生物发酵获得的1,3-丙二醇发酵液是含多种强极性的醇及盐类的稀溶液,这使得采用传统的分离方法难以经济、有效地的将1,3-丙二醇从发酵液中纯化出来,后提取过程成为发酵法工业化生产1,3-丙二醇的瓶颈。1,3-丙二醇后提取过程主要包括微生物菌体等高分子物质的去除,盐的去除、回收,有机物的纯化和水的去除。以下对应用于以上分离过程的技术的研究进展进行讨论,提出在该领域应该重视的发展方向。     

Use of oxidoreduction potential as an indicator to regulate 1,3-propanediol fermentation by Klebsiella pneumoniae

Anaerobic fermentation was relatively difficult to optimize due to lack of monitoring parameters. In this paper, a new method was reported using extracellular oxidoreduction potential (ORP) to monitor 1,3-propanediol (1,3-PD) biosynthesis process by Klebsiella pneumoniae. In batch fermentation, cell growth, 1,3-propanediol production and by-products distribution were studied at four different ORP levels: 10, −140, −190 and −240 mV. From the results, the ORP level of −190 mV was preferable, which resulted in fast cell growth and high 1,3-propanediol concentration. The NAD⁺/NADH ratio was determined at different ORP levels, and a critical NAD⁺/NADH ratio of 4 was defined to divide fermentation environments into two categories: relatively oxidative environment (NAD⁺/NADH>4) and relatively reductive environment (NAD⁺/NADH<4). The former was correlative with high 1,3-propanediol productivity and high specific growth rate. The mechanism of ORP regulation was discussed. It is suggested that ORP regulation of fermentation might be due to its influence on the ratio of NAD⁺/NADH, which determined metabolic flux. Furthermore, a batch fermentation of modulating ORP following a profile in different levels corresponding to different fermentation stage was tested. The 1,3-PD concentration was 22.3% higher than that of constant ORP fermentation at −190 mV. Therefore, ORP is a valuable parameter to monitor and control anaerobic fermentation production.     

Studies on purification of 1,3-propanediol by molecular distillation

The separation of 1,3-propanediol using molecular distillation has been studied. The effects of operating temperature and feed flow rate through a sequential distillation strategy were investigated. The optimal experimental temperature was at 70°C for separating 1,3-propanediol and the by-product 2,3-butanediol. Meanwhile, the volume flow rate was 10 mL/min. As a result, the recovery of 1,3-propanediol and 2,3-butanediol were 87.6 and 87.5%, respectively. Furthermore, the integrated separation characteristic of 1,3-propanediol was evaluated through macrolevel and micro-level models. The separation factors of 1,3-propanediol versus 2,3-butanediol and glycerol were 0.11 and 1.07, respectively, affirming that the separation of 1,3-propanediol by molecular distillation was feasible.     

产1,3-丙二醇菌株的诱变和筛选

为提高克雷伯氏肺炎杆菌产1,3-丙二醇的能力,以离子束、紫外线和氯化锂为复合诱变法,建立了产酸圈和产物耐受相结合的平板筛选方法,获得可耐受高浓度1,3-丙二醇并且副产物中乙醇含量较少的优良突变菌株2株。与出发菌株相比,两株高产突变菌株Klebsiella pneumoniae LM 03和Klebsiella pneumoniae LM05的1,3-丙二醇产量分别提高了33% 和30% ,达到66.74 g/L和65.12 g/L;乙醇产量分别降低了38% 和24% ,降低为6.59 g/L和8.05 g/L。同时测定了诱变前后还原途径中甘油脱水酶（GDHt）和1,3-丙二醇氧化还原酶（PDOR）的酶活变化,研究表明诱变对GDHt有明显的促进作用,而对PDOR的影响不明显。该诱变和筛选方法目标明确、易操作、效率高,在1,3-PD工业规模的生物法生产中将具有良好的应用价值,而且对于其他具有工业应用价值的菌株筛选工作也具有一定的借鉴意义。     

Fermentation of glycerol to 1,3-propanediol: use of cosubstrates

Three fermentable substances, glucose, 1,2-ethanediol and 1,2-propanediol were checked as cosubstrates for the fermentation of glycerol by Clostridium butyricum and Citrobacter freundii with the aim of achieving a complete conversion of glycerol to 1,3-propanediol. Glucose was fermented by C. butyricum mainly to acetate, CO₂ and reducing equivalents in the presence of glycerol and contributed markedly to the 1,3-propanediol yield. However, because of relatively slow growth on glucose, complete conversion was not achieved. If the two glycols were used as cosubstrates for glycerol fermentation, the 1,3-propanediol yield did not increase but dimished considerably, as they were converted to more reduced products, i.e. alcohols instead of acids. From 1,2-propanediol 2-propanol was formed in addition to 1-propanol. The ratio of the propanols was dependent on the culture conditions.     

Production of 1,3-propanediol from Glycerol by Recombinant <Emphasis Type="Italic">E. coli</Emphasis> Using Incompatible Plasmids System

1,3-Propanediol (1,3-PD) has numerous applications in polymers, cosmetics, foods, lubricants, and medicines as a bifunctional organic compound. The genes for the production of 1,3-PD in Klebsiella pneumoniae, dhaB, which encodes glycerol dehydratase, and dhaT, which encodes 1,3-PD oxidoreductase, and gdrAB, which encodes glycerol dehydratase reactivating factor, are naturally under the control of different promoters and are transcribed in different directions. These genes were coexpressed in E. coli using two incompatible plasmids (pET28a and pET22b) in the presence of selective pressure. The recombinant E. coli coexpressed the glycerol dehydratase, 1,3-propanediol oxidoreductase and reactivating factor for the glycerol dehydratase at high levels. In a fed-batch fermentation of glycerol and glucose, the recombinant E. coli containing these two incompatible plasmids consumed 14.3 g/l glycerol and produced 8.6 g/l 1,3-propanediol. In the substitution case of yqhD (encoding alcohol dehydrogenase from E. coli) for dhaT, the final 1,3-propanediol concentration of the recombinant E. coli could reach 13.2 g/l.     

Microbial production of 1,3-propanediol: Recent developments and emerging opportunities

1,3-Propanediol, a valuable bifunctional molecule, can be produced from renewable resources using microorganisms. It has several promising properties for many synthetic reactions, particularly for polymer and cosmetic industries. By virtue of being a natural product, relevant biochemical pathways can be harnessed into fermentation processes to produce 1,3-propanediol. Various strategies for the microbial production of 1,3-propanediol are reviewed and compared in this article with their promises and constraints. Furthermore, genetic and metabolic engineering could significantly improve product yields and overcome the limitations of fermentation technology. Present review gives an overview on 1,3-propanediol production by wild and recombinant strains. It also attempts to encompass the various issues concerned in utilization of crude glycerol for 1,3-propanediol production, with particular emphasis laid on biodiesel industries. This review also summarizes the present state of strategies studied for the downstream processing and purification of biologically produced 1,3-propanediol. The future prospect of 1,3-propanediol and its potential as a major bulk chemical are discussed under the light of the current research.     

Overflow metabolism during anaerobic growth of Klebsiella aerogenes NCTC 418 on glycerol and dihydroxyacetone in chemostat culture

Klebsiella aerogenes NCTC 418 was grown anaerobically in chemostat culture with glycerol as source of carbon and energy. Glycerol-limited cultures did not ferment the carbon source with maximal efficiency but produced considerable amounts of 1,3-propanediol. The fraction of glycerol converted to this product depended on the growth rate and on the limitation: faster growing cells produced relatively more of this compound. Under glycerol excess conditions the energetic efficiency of fermentation was decreased due to the high 1,3-propanediol excretion rate. Evidence is presented that 1,3-propanediol accumulation exerts a profound effect on the cells' metabolic behaviour.When steady state glycerol-limited cultures were instantaneously relieved of the growth limitation a vastly enhanced glycerol uptake rate was observed, accompanied by a shift in the fermentation pattern towards 1,3-propanediol and acetate. This observation was consistent with the extremely high glycerol dehydrogenase activity that was measured in vitro. Some mechanisms that could be responsible for the energy dissipation during this response are discussed.     

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.     

Lipase catalysed synthesis of propanediol monoesters in biphasic aqueous medium

The 1,3-regiospecific lipase from Candida deformanscatalysed the esterification of oleic acid and propanediol in biphasic aqueous/lipid medium without organic solvent. The highest conversion of oleic acid into 1,2-propanediol ester was 74% in 24 h with 6.25 mol/l 1,2-propanediol and 0.08 mol/l oleic acid, and produced 100% monoester. The esterification of 1,3-propanediol converted up to 98% of oleic acid into esters in 24 h (with 7.5 mol/l 1,3-propanediol and 0.08 mol/l oleic acid) and formed 35-90% monoester depending on 1,3-propanediol initial concentration (2.5-10 mol/l).     

Glycerol fermentation of 1,3-propanediol by Clostridium butyricum. Measurement of product inhibition by use of a pH-auxostat

Summary The fermentation of glycerol to 1,3-propanediol, acetate, and butyrate by Clostridium butyricum was studied with respect to growth inhibition by the accumulating products. The clostridia were grown in a pH-auxostat culture at low cell density and product concentration and near maximum growth rate. The products were then added individually to the medium in increasing concentrations and the resulting depression of growth rate was used as a quantitative estimate of product inhibition. Under these conditions growth was totally inhibited at concentrations of 60 g/l for 1,3-propanediol, 27 g/l for acetic acid and 19 g/l for butyric acid at pH 6.5. Appreciable inhibition by glycerol was found only above a concentration of 80 g/l. In a pH-auxostat without added products but with high cell density as well as in batch cultures the product proportions were different. The 1,3-propanediol concentration may approach the value of complete inhibition while the concentrations of acetic and butyric acids remained below these values by at least one order of magnitude. It was therefore concluded that 1,3-propanediol is the first range inhibitor in this fermentation.     

Fermentation of glycerol by Clostridium pasteurianum--batch and continuous culture studies

The fermentation of glycerol by Clostridium pasteurianum was studied with respect to product formation as influenced by the culture conditions. In the majority of batch cultures, butanol was the main fermentation product, but a varying fraction of glycerol was also converted to 1,3-propanediol, butyric and acetic acids and ethanol. More than 60 g/l glycerol was utilized, and up to 17 g/l butanol was produced. Fed-batch cultures did not offer an advantage. When molecular nitrogen was used as a nitrogen source, the fermentation time was prolonged by a factor of 1.5. Fermentations at constant pH values between 4.5 and 7.5 did not reveal significant differences in product formation except for an increase in the ethanol content starting at pH 6.5. Chemostat cultures also yielded predominantly n-butanol, but in some fermentations, the 1,3-propanediol fraction was relatively high. The pH auxostat cultures, which were operated at a glycerol excess, contained 1,3-propanediol as the main product. As a whole, the fermentations were characterized by a certain variability in product formation under seemingly equal or slightly varied conditions. It appears that the regulation of the numerous fermentation pathways occurring in this organism is not very strict. Journal of Industrial Microbiology & Biotechnology (2001) 27, 18–26. Received 25 September 2000/ Accepted in revised form 07 April 2001     

Glycerol and propanediols degradation by Desulfovibrio alcoholovorans in pure culture in the presence of sulfate, or in syntrophic association with Methanospirillum hungatei

Abstract In a mineral medium containing sulfate as terminal electron acceptor, the sulfate-reducing bacterium Desulfovibrio alcoholovorans oxidized stoichiometrically 1 mol glycerol to 1 mol acetate and 1 mol 1,3-propanediol to 1 mol acetate with the concomitant reduction of 0.75 and 1 mol sulfate, respectively; 1 mol 1,2-propanediol was degraded to 0.8 mol acetate and 0.1 mol proprionate, with the reduction of approximately 1 mol sulfate. The maximum specific growth rates (μ_max in h⁻¹) were 0.22, 0.086 and 0.09 with glycerol, 1,3-propanediol and 1,2-propanediol, respectively. The growth yields were 12.7 g, 11.1 g and 7.2 g dry weight/mol 1,3-propanediol, glycerol and 1,2-propanediol degraded, respectively. The growth yields and maximum specific growth rates of the H₂-transferring associations were also calculated. In the absense of sulfate, all these reduced substrates were degraded to acids and methane when D. alcoholovorans was cocultured with Methanospirillum hungatei . Changes in the metabolic pathway were observed in the degradation of 1,2- and 1,3-propanediol. The metabolic efficiency of D. alcoholovorans to degrade glycerol, 1.2- and 1,3-propanediol is discussed.     

Cell physiology and metabolic flux response of Klebsiella pneumoniae to aerobic conditions

Cell physiology and metabolic flux distribution of Klebsiella pneumoniae under anaerobic, micro-aerobic and sufficient aerobic conditions were compared. Comparing with the anaerobic condition, the carbon flux flowed from glycerol to biomass increased 10.1% and 389.9%, while the flux flowed to 1,3-propanediol decreased 10.3% and 92.9% under micro-aerobic and sufficient aerobic conditions, respectively. Furthermore, the carbon flux flowed to TCA cycle increased 5.9% and 31.0% under such two conditions. The energy analysis results revealed that the oxygen was favorable for the NADH₂ synthesis, but excessive oxygen was disadvantage for the NADH₂ utilization in 1,3-propanediol synthesis process. So, the aeration control is significant for the aerobic 1,3-propanediol fermentation. This work is considered helpful for the further understanding of the glycerol metabolism by Klebsiella pneumoniae under aerobic condition and to establish a rational aeration control strategy for 1,3-propanediol aerobic fermentation in a large-scale bioreactor.