A novel downstream process for 1,3-propanediol from glycerol-based fermentation

In this paper, a downstream process for purification of 1,3-propanediol from glycerol-based fermentation broth was investigated. The purification of 1,3-propanediol from fermentation broth was achieved by a process combining microfiltration, charcoal treatment, vacuum distillation, and silica gel chromatography. The broth was first filtered through hollow fiber cartridge, wherein 98.7% of biomass was removed. Soluble proteins and other color impurities in the broth were removed by the use of activated charcoal at optimal concentration of 30 g l⁻¹ where the soluble proteins in the broth decreased to 0.1 g l⁻¹ (96.0% protein loss). The obtained broth when concentrated by vacuum distillation resulted in the crystallization of inorganic salts. Subsequently, 1,3-propanediol was purified by gradient chromatography using silica gel as a stationary phase and mixture of chloroform and methanol as a mobile phase. Finally, with the optimal flow rate of 10 ml min⁻¹ and loading amount of 80 ml, the yield of 1,3-propanediol achieved was 89%. The overall yield of 1,3-propanediol using the proposed procedure was 75.47%. The developed method was found to be a simple, rapid, and efficient procedure for the purification of 1,3-propanediol from fermentation broth.     

Inactivation of <Emphasis Type="Italic">dhaD</Emphasis> and <Emphasis Type="Italic">dhaK</Emphasis> abolishes by-product accumulation during 1,3-propanediol production in <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

1,3-Propanediol (1,3-PD) can be used for the industrial synthesis of a variety of compounds, including polyesters, polyethers, and polyurethanes. 1,3-PD is generated from petrochemical and microbial sources. 1,3-Propanediol is a typical product of glycerol fermentation, while acetate, lactate, 2,3-butanediol, and ethanol also accumulate during the process. Substrate and product inhibition limit the final concentration of 1,3-propanediol in the fermentation broth. It is impossible to increase the yield of 1,3-propanediol by using the traditional whole-cell fermentation process. In this study, dhaD and dhaK, the genes for glycerol dehydrogenase and dihydroxyacetone kinase, respectively, were inactivated by homologous recombination in Klebsiella pneumoniae. The dhaD/dhaK double mutant (designated TC100), selected from 5,000 single or double cross homologous recombination mutants, was confirmed as a double cross by using polymerase chain reaction. Analysis of the cell-free supernatant with high-performance liquid chromatography revealed elimination of lactate and 2,3-butanediol, as well as ethanol accumulation in TC100, compared with the wild-type strain. Furthermore, 1,3-propanediol productivity was increased in the TC100 strain expressing glycerol dehydratase and 1,3-PDO dehydrogenase regulated by the arabinose P_BAD promoter. The genetic engineering and medium formulation approaches used here should aid in the separation of 1,3-propanediol from lactate, 2,3-butanediol, and ethanol and lead to increased production of 1,3-propanediol in Klebsiella pneumoniae.     

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.     

1,3-丙二醇产生茵基因组重排育种

[目的]本文以肺炎克雷伯氏杆菌为研究对象,利用基因组重排技术,提高其对发酵体系中主要产物的耐受性,获得1,3-丙二醇高产菌.[方法]以含预处理后的出发菌株的补料发酵终点液的96孔板为筛选方法,利用基因组重排技术育种.[结果]筛选到的5株高产菌株(LSG1,LSG2,LSG4,LSG5,LSG6),在3升罐批次发酵中的1...     

Decrease of 3-hydroxypropionaldehyde accumulation in 1,3-propanediol production by over-expressing <Emphasis Type="Italic">dha</Emphasis>T gene in <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> TUAC01

Glycerol can be biologically converted to 1,3-propanediol, a key raw material required for the synthesis of polytrimethylene terephthalate and other polyester fibers. In 1,3-propanediol synthesis pathway, 3-hydroxypropionaldehyde (3-HPA) was an inhibitory intermediary metabolite. The accumulation of 3-HPA in broth would cause an irreversible cessation of the fermentation process. With the object of reducing 3-HPA level in the fermentation broth, dhaT gene which encodes 1,3-propanediol oxidoreductase (PDOR) was cloned and over expressed in 1,3-propanediol producing bacterium Klebsiella pneumoniae TUAC01. dhaT gene was linked downstream of the ptac promoter in an expressing vector pDK6 to form plasmid pDK-dhaT. The newly formed pDK-dhaT was transformed to K. pneumoniae TUAC01. Under the inducement of IPTG, PDOR was over-expressed when the constructed strain was cultured on an LB medium or a fermentation medium. A 5 L scale-up fermentation experiment was done to test the 3-HPA accumulation in broth, with the initial substrate glycerol 30 g/L; the peak levels of 3-HPA in broth were 7.55 and 1.49 mmol/L for control host strain and the constructed strain, respectively. In 50 g/L initial glycerol experiment, the peak level of 3-HPA in broth was 12.57 and 2.02 mmol/l for the control host strain and the constructed strain, respectively. Thus the fermentation cessation caused by the toxicity of 3-HPA was alleviated in the constructed strain.     

Sensitivity to pH, product inhibition, and inhibition by NAD+ of 1,3-propanediol dehydrogenase purified from Enterobacter agglomerans CNCM 1210

Because of its key role in the metabolism of glycerol during fermentation, 1,3-propanediol dehydrogenase (EC 1.1.1.202) of Enterobacter agglomerans CNCM 1210 was purified to homogeneity and studied with respect to its sensitivity to pH and to nucleotide and 1,3-propanediol concentrations. Enzyme activity was optimal at pH 7.8. The enzyme was competitively inhibited by NAD⁺ (K_i of 0.29 mM), and 1,3-propanediol exerted a strong inhibitory effect according to a mixed-type inhibition with a K_i of 13.7 mM and an a-factor of 9.0. It is proposed that these dehydrogenase properties be extended to the dehydrogenases of Citrobacter freundii and Klebsiella pneumoniae, which exhibited numerous similar physical properties. Received: 4 December 1996 / Accepted: 24 March 1997     

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.     

Pilot-scale production of 1,3-propanediol using Klebsiella pneumoniae

The conversion of glycerol to 1,3-propanediol (PDO) using Klebsiella pneumoniae M5al under anaerobic condition was scaled up from scale 5 to 5000 l in series. A simple strategy for scale-up was to transfer the optimized conditions of a lab scale bioreactor to pilot-scale fermentation. Multistage inocula were developed and their fermentation abilities were assessed in a small-scale fermenter. The experimental results showed that inoculum development in the early steps of a scale-up process could influence the outcomes of a large scale fermentation. Through three-stage liquid inoculum development and a pulse addition of (NH₄)₂SO₄ and yeast extract at 30 h of fermentation, the best results in a 5000 l fermentation were achieved leading to 58.8 g l⁻¹ 1,3-propanediol with a yield of 0.53 mol mol⁻¹ glycerol and productivity of 0.92 g l⁻¹ h⁻¹. This is the first report on pilot-scale 1,3-propanediol production using K. pneumoniae.     

Inhibition of Clostridium butyricum by 1,3-propanediol and diols during glycerol fermentation

1,3-Propanediol inhibition during glycerol fermentation to 1,3-propanediol by Clostridium butyricum CNCM 1211 has been studied. The initial concentration of the 1,3-propanediol affected the growth of the bacterium more than the glycerol fermentation. μ _max was inversely proportional to the initial concentration of 1,3-propanediol (0–65 g l⁻¹). For glycerol at 20 g l⁻¹, the growth and fermentation were completely stopped at an initial 1,3-propanediol concentration of 65 g l⁻¹. However, for an initial 1,3-propanediol concentration of 50 g l⁻¹ and glycerol at 70 g l⁻¹, the final concentration (initial and produced) of 1,3-propanediol reached 83.7 g l⁻¹(1.1 M), with complete consumption of the glycerol. Therefore, during the fermentation, the strain tolerated a 1,3-propanediol concentration higher than the initial inhibitory concentration (65 g l⁻¹). The addition of 1,2-propanediol or 2,3-butanediol (50 g l⁻¹) in the presence of glycerol (50–100 g l⁻¹), showed that 2-diols reduced the μ _max in a similar way to 1,3-propanediol. The measurement of the osmotic pressure of glycerol solutions, diols and diol/glycerol mixtures did not indicate any differences between these compounds. The hypothesis of diol inhibition was discussed. Taking into account the strain tolerance of highly concentrated 1,3-propanediol during fermentation, the fermentation processes for optimising production were considered. Received: 15 November 1999 / Revision received: 1 February 2000 / Accepted: 4 February 2000     

Isolation of microorganisms able to produce 1,3-propanediol and optimization of medium constituents for Klebsiella pneumoniae AJ4

Microbial fermentation under anaerobic and microaerobic conditions has been used for the production of 1,3-propanediol (1,3-PD), a monomer used to produce polymers such as polytrimethylene terephthalate. In this study, we screened microorganisms using the high throughput screening method and isolated the Klebsiella pneumoniae AJ4 strain, which is able to produce 1,3-PD under aerobic conditions. To obtain the maximum 1,3-PD concentration from glycerol, the response surface methodology based on a central composite design was chosen to show the statistical significance of the effects of glycerol, peptone, and (NH₄)₂SO₄ on 1,3-PD production by K. pneumoniae AJ4. The optimal culture medium factors for achieving maximum concentrations of 1,3-PD included glycerol, 108.5 g/L; peptone, 2.72 g/L; and (NH₄)₂SO_4, 4.38 g/L. Under this optimum condition, the maximum concentration of 1,3-PD, 54.76 g/L, was predicted. A concentration of about 52.59 g/L 1,3-PD was obtained using the optimized medium during 26-h batch fermentation, a finding that agreed well with the predicted value.     

Production of 1,3-Propanediol from Glycerol by Clostridium acetobutylicum and Other Clostridium Species

Glycerol was fermented with the production of 1,3-propanediol as the major fermentation product by four strains of Clostridium acetobutylicum, six of C. butylicum, two of C. beijerinckii, one of C. kainantoi, and three of C. butyricum. 1,3-Propanediol was identified by its retention times in gas chromatography and high-pressure liquid chromatography and by its mass spectrum. During growth of C. butylicum B593 in a chemostat culture at pH 6.5, 61% of the glycerol fermented was converted to 1,3-propanediol. When the pH was decreased to 4.9, growth and 1,3-propanediol production were substantially reduced.     

High production of 1,3-propanediol from glycerol by Clostridium butyricum VPI 3266 in a simply controlled fed-batch system

Summary A simple fed-batch system which controls substrate feeding by measuring the CO₂ produced during the fermentation, was developped. This Fed-batch approach allowed high production of 1,3-propanediol from glycerol by Clostridium butyricum by avoiding substrate inhibition phenomena. 65 g/l of 1,3-propanediol was produced with a productivity of 1.21 g/l.h and a yield of 0.56. The concentration of 1,3-propanediol obtained and the productivity were significantly higher than those reached in batch culture.     

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.     

Enhanced 1,3-propanediol production in recombinant <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> carrying the gene <Emphasis Type="Italic">yqh</Emphasis>D encoding 1,3-propanediol oxidoreductase isoenzyme

The yqhD gene from Escherichia coli encoding 1,3-propanediol oxidoreductase isoenzyme (PDORI) and the tetracycline resistant gene (tetR) from plasmid pHY300PLK were amplified by PCR. They were inserted into vector pUC18, yielding the recombinant expression vector pUC18-yqhD-tetR. The recombinant vector was then cloned into Klebsiella pneumoniae ME-308. The overexpression of PDORI in K. pneumoniae surprisingly led to higher 1,3-propanediol production. The final 1,3-propanediol concentration of recombinant K. pneumoniae reached 67.6 g/l, which was 125.33% of that of the original strain. The maximum activity of recombinant PDORI converting 3-HPA to 1,3-PD reached 110 IU/mg after induction by IPTG at 31°C during the fermentation, while it was only 11 IU/mg under the same conditions for the wild type strain. The K _m values of the purified PDORI for 1,3-propanediol and NADP were 12.1 mM and 0.15 mM, respectively. Compared with the original strains, the concentration of the toxic intermediate 3-hydroxypropionaldehyde during the fermentation was also reduced by 22.4%. Both the increased production of 1,3-propanediol and the reduction of toxic intermediate confirmed the significant role of 1,3-propanediol oxidoreductase isoenzyme from E. coli in converting 3-hydroxypropionaldehyde to 1,3-propanediol for 1,3-PD production.     

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.     

Construction of a novel recombinant Escherichia coli strain capable of producing 1,3–propanediol and optimization of fermentation parameters by statistical design

Summary The structural gene yqhD from a wild-type Escherichia coli encoding 1,3-propanediol oxidoreductase isoenzyme and the structural gene dhaB from Citrobacter freundii encoding glycerol dehydratase were amplified by using the PCR method. The temperature control expression vector pHsh harboring the yqhD and dhaB genes was transformed into E. coli JM109 to yield the recombinant strain E. coli JM109 (pHsh-dhaB-yqhD). The response surface method (RSM) was then applied to further optimize the fermentation condition of the recombinant strain. A mathematical model was then developed to show the effect of each medium composition and their interactions on the production of 1,3-propanediol by recombinant strain E. coli JM109. The model estimated that a maximal yield of 1,3-propanediol (43.86 g/l) could be obtained when the concentrations of glycerol, yeast extract and vitamin B₁₂ were set at 61.8 g/l, 6.2 g/l and 49 mg/l, respectively; and the fermentation time was 30 h. These predicted values were also verified by validation experiments. Compared with the values obtained by other runs in the experimental design, the optimized medium resulted in a significant increase in the yield of 1,3-propanediol. The yield and productivity under the optimal parameters and process can reach 43.1 g/l and 1.54 g/l/h. Maximum 1,3-propanediol yield of 41.1 g/l was achieved in a 5-l fermenter using the optimized medium. This makes the engineered strain have potential application in the conversion of glycerol to 1,3-propanediol on an industrial scale.     

The fermentation of glycerol byClostridium butyricum LMG 1212t2 and 1213t1 andC. pasteurianum LMG 3285

Summary In batch culture on reiinforced clostridial medium strain-dependent product profiles from glycerol revealed unusual fermentation products such as propionate and n-propanol with Clostridium butyricum LMG 1213t₁, and 1,3-propanediol with C. butyricum LMG 1212t₂ and C. pasteurianium LMG 3285. Only the latter two strains were able to grow on glycerol in a minimal medium. Nicotinamide adenine dinucleotide (NAD⁺)-dependent dehydrogenase activities were detected with 1,3-propanediol and n-butanol as substrate (the latter only after a lag period) in cell-free extracts of C. butyricum LMG 1212t₂ and with 1,3-propanediol, n-butanol and ethanol in cell-free extracts of C. pasteurianum LMG 3285. The data indicated the existance of a specific 1,3-propanediol dehydrogenase in both organisms. In a chemostat, C. butyricum LMG 1212t₂ converted 65% of the glycerol supplied as sole carbon and energy source to 1,3-propanediol without H₂ production. Increasing concentration of acetate in the inflow medium resulted in less 1,3-propanediol and more butyrate and H₂ production. C. pasteurianum LMG 3285 converted somewhat more than half of the glycerol supplied as sole energy and carbon source to n-butanol with significant concomitant H₂ production. This fermentation pattern was hardly affected by acetate as co-substrate. Offprint requests to: P. De Vos     

Production of 1,3-propanediol, 2,3-butanediol and ethanol by a newly isolated Klebsiella oxytoca strain growing on biodiesel-derived glycerol based media

The production of 1,3-propanediol, 2,3-butanediol and ethanol was studied, during cultivations of strain Klebsiella oxytoca FMCC-197 on biodiesel-derived glycerol based media. Different kinds of glycerol feedstocks and experimental conditions had an important impact upon the distribution of metabolic products; production of 1,3-propanediol was positively influenced by stable pH conditions and by the absence of N₂ gas infusions throughout the fermentation. Thus, during batch bioreactor fermentations conducted at increasing glycerol concentrations, 1,3-propanediol at 41.3 g/L and yield ～47% (w/w) was achieved at initial glycerol concentration ～120 g/L. At even higher initial glycerol media (150 and 170 g/L), growth was not ceased, but 1,3-propanediol production declined. During fed-batch fermentation under optimal experimental conditions, 126 g/L of glycerol were converted into 50.1 g/L of 1,3-propanediol. In this experiment, also 25.2 g/L of ethanol (conversion yield ～20%, w/w) were formed. A batch-bioreactor culture was performed under non-sterilized conditions and the 1,3-propanediol production was almost equivalent to the sterilized process. Concerning 2,3-butanediol formation, the most detrimental parameter was the absence of N₂ sparging and as a result, no 2,3-butanediol was produced. The presence of glucose as co-substrate seriously enhanced 2,3-butanediol production; when commercial glucose was employed as sole substrate, 32.1 g/L of 2,3-butanediol were formed.     

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.