Production of butanol by Clostridium puniceum in batch and continuous culture

Summary The pink-pigmented, amylolytic and pectinolytic bacterium Clostridium puniceum in anaerobic batch culture at pH 5.5 and 25–30°C produced butan-1-ol as the major product of fermentation of glucose or starch. The alcohol was formed throughout the exponential phase of growth and surprisingly little acetone was simultaneously produced. Furthermore, acetic and butyric acids were only accumulated in low concentrations, and under optimal conditions were completely re-utilised before the fermentation ceased. Thus, in a minimal medium containing 4% w/v glucose as sole source of carbon and energy, after 65 h at 25°C, pH 5.5 all of the glucose had been consumed to yield (g product/100 g glucose utilised) butanol 32, acetone 3 and ethanol 2. Butanol was again the major product of glucose fermentation during phosphate-limited chemostat culture wherein, although the organism eventually lost its capacity to sporulate and to synthesize granulose, production of butanol continued for at least 100 volume changes. Under no growth condition was the organism capable of producing more than 13.3 g l^-1 of butanol. At pH 5.5, growth on pectin was slow and yielded a markedly lesser biomass concentration than when growth was on glucose or starch; acetic acid was the major fermentation product with lower concentrations of methanol, acetone, butanol and butyric acid. At pH 7, growth on all substrates produced virtually no solvents but high concentrations of both acetic and butyric acids.     

The acetone butanol fermentation on glucose and xylose. II. Regulation and kinetics in fed-batch cultures

The kinetics in fed-batch cultures of acetone butanol fermentation by Clostridium acetobutylicum is compared on glucose, xylose, and mixtures of both sugars. The final conversion yield of sugars into solvents always increases with the sugar feeding rate. At low feeding rates, the sugar concentration in the medium becomes limiting, which results in a slower cellular growth, a slower metabolic transition from an acid to a solvent fermentation and, thus, a higher accumulation of acids. It is only at sufficiently high feeding rates that fed-batch fermentations yield kinetic results comparable to those of batch fermentations. With mixtures of glucose and xylose, because of a maintained low glucose level, both sugars are taken up at the same rate during a first fermentation period. An earlier accumulation of xylose when the fermentation becomes inhibited suggest that xylose utilization is inhibited when the catabolic flux of glucose alone can satisfy the metabolic activity of the cell. Kinetic results with batch and fed-batch fermentations indicate several important features of the regulation of C. acetobutylicum metabolism: an early inhibition by the produced acids; an initiation of solvent formation between 4 and 6 g/L acetic and butyric acid depending on the metabolic activity of the cell; a metabolic transition from acids to solvents production at a rate closely related to the rate of sugar uptake; during solvent production, a reassimilation of acids above a minimal rate of sugar consumption of 0.2 h(-1); a final inhibition of the fermentation at a total butanol and acids concentration of ca. 20 g/L.     

Effect of pyruvate on glucose metabolism in Clostridium acetobutylicum

Pyruvate effects on the metabolism of Clostridium acetobutylicum during glucose fermentation were studied. After addition to the culture medium, the pyruvate was rapidly used, provoking several changes in the metabolic pattern of the bacteria. When pyruvate addition occurred early in the fermentation, the glucose utilization decreased and the solventogenic phase was not induced. When pyruvate was added during solventogenesis, glucose consumption was slightly affected and the cells fermented both substrates simultaneously: however, the acidogenic phase started again to the detriment of solvent formation. Usually, during the solvent phase, the cells remetabolized acetic and butyric acids into solvents, but when pyruvate was added, the utilization of acids was stopped and the specific rates of acetate and butyrate formation increased immediately. The acidogenic growth phase was characterized by high levels of acetate and butyrate kinase which dropped during the solvent phase. Addition of pyruvate limited the down shift of these two enzymes and the levels of the activities remained constant during the course of the fermentation. Conversely, the acetoacetate decarboxylase, which is characteristic of the solvent phase, decreased sharply in the presence of pyruvate. The fact that the specific rate of glucose consumption was not decreased by the pyruvate metabolism, a cosubstrate, proves that the phosphoroclastic reaction is not a limiting step. Furthermore, the pyruvate utilization represented a promising approach to obtain useful data on the intracellular compounds implicated in the mechanism for switching from the acidogenic to the solventogenic phase.     

Influence of amino acid supplements on the metabolism of Clostridium acetobutylicum

The effects of organic nitrogen on the metabolism of Clostridium acetobutylicum were investigated in batch fermentations. For this study, amino acids were added to a chemically defined medium in groups from the same biosynthetic pathways. In all cases the addition of amino acids shifted the solvent ratio to higher butanol production at the expense of that of acetone (except for the glutamic acid group) and ethanol (except for histidine). Highest biomass production was obtained from media containing aromatic amino acids and histidine (4.57 g · l⁻¹ and 5.4 g · l⁻¹, respectively). However, the solvent production (ca. 20 g · l⁻¹) and the solvent yield (ca. 33%) in both cases, were similar to those obtained from the synthetic medium. Lower values were obtained from fermentations carried out with other families of amino acids. The strongest inhibition of cell growth (1.13 g · l⁻¹) which related to the lowest solvent production (3.15 g · l⁻¹) was observed on a medium complemented with amino acids of the pyruvic acid group. During the second phase of fermentation, amino acids-complemented media caused a less efficient remetabolization of acetic and butyric acids. Highest production of acids was obtained with the aspartic acid group (7.4 g · l⁻¹). These observations suggest that amino acids can be used as a competitive nitrogen source and also modify the level of enzyme activities involved in acid and solvent production.     

Regulation of acetate kinase and butyrate kinase by acids in Clostridium acetobutylicum

Abstract The effects of acetic acid and butyric acid on acetate kinase, butyrate kinase and acetoacetate decarboxylase levels are studied. It is shown that acetate kinase biosynthesis is regulated by acetic acid whereas butyric acid has no effect. Acetate kinase specific activity is found to be maximal at the beginning of the fermentation, and decreases as acetic acid concentration increases in the medium. Butyrate kinase is not regulated by the end-product acids; its specific activity is constant during the fermentation. In the presence of acetic acid, acetoacetate decarboxylase biosynthesis represents a 4-fold increase in activity over a culture without acetate and a 1.7-fold increase over that obtained in presence of butyrate. The technique of fermentation used allows us to show that bacterial growth and solventogenesis may occur simultaneously.     

Improvements of GC and HPLC analyses in solvent (acetone-butanol-ethanol) fermentation byClostridium saccharobutylicum using a mixture of starch and glycerol as carbon source

A study on the feasibility of using improved computer-controlled HPLC and GC systems was carried out to shorten the time needed for measuring levels of the substrates (glucose, maltose, and glycerol) and products (acetone, butanol ethanol, acetic acid, and butyric acid) produced byClostridium saccharobutylicum DSM 13864 during direct fermentation of sago starch to solvent. The use of HPLC system with a single injection to analyse the composition of culture broth (substrates and products) during solvent fermentation was achieved by raising the column temperature to 80°C. Although good separation of the components in the mixture was achieved, a slight overlap was observed in the peaks for butyric acid and acetone. The shape of the peak obtained and the analysis time of 26.66 min were satisfactory at a fixed flow rate of 0.8 mL/min. An improved GC system was developed, that was able to measure the products of solvent fermentation (acetone, butanol, ethanol, acetic acid, and butyric acid) within 19.28 min. Excellent resolution for each peak was achieved by adjusting the oven temperature to 65°C.     

添加有机酸对Clostridium acetobutylicum合成丙酮和丁醇的影响

为提高丙酮-丁醇梭菌厌氧发酵生产丙酮和丁醇的能力,在发酵过程中添加有机酸（乙酸和丁酸）,考察其对菌体生长、溶剂合成影响。实验表明：当添加1.5 g/L乙酸时能够促进菌体的生长,促进丙酮的合成,在600 nm处的最大OD值比参照值高出18.4%,丙酮的最终质量分数提高了21.05%,但不能促进丁醇的合成;当添加1.0g/L丁酸时能够促进菌体生长,促进丁醇的合成,在600 nm处的最大OD比参照值高22.29%,丁醇的最终质量分数比对照组提高了24.32%,但不能促进丙酮的合成。     

Role of Chemotaxis in Solvent Production by Clostridium acetobutylicum

The motility of Clostridium acetobutylicum has been investigated during a typical batch fermentation process for solvent production. The motility is characterized by “runs” during the early phase of sugar utilization and acid production, but this changes to “tumbles” during the onset of solventogenesis. Sugars and undissociated acetic and butyric acids have been shown to be attractants for the bacterium, while acetone, butanol, ethanol, and dissociated acetate and butyrate are repellents. It is suggested that chemotactic responses explain why highly motile cells are strongly solventogenic.     

Solvent production byClostridium pasteurianum in media of high sugar content

Summary The fermentation end products ofClostridium pasteurianum ATCC 6013 are normally acetic and butyric acids. When grown in media of high sugar content however, significant quantities of solvents (acetone, butanol and ethanol) were produced. Solvent production was not stimulated by added acetic and butyric acids, nor was the effect due to a low water activity of the mediumper se.     

Intracellular Conditions Required for Initiation of Solvent Production by Clostridium acetobutylicum

We investigated the intracellular physiological conditions associated with the induction of butanol-producing enzymes in Clostridium acetobutylicum. During the acidogenic phase of growth, the internal pH decreased in parallel with the decrease in the external pH, but the internal pH did not go below 5.5 throughout batch growth. Butanol was found to dissipate the proton motive force of fermenting C. acetobutylicum cells by decreasing the transmembrane pH gradient, whereas the membrane potential was affected only slightly. In growing cells, the switch from acid to solvent production occurred when the internal undissociated butyric acid concentration reached 13 mM and the total intracellular undissociated acid concentration (acetic plus butyric acids) was at least 40 to 45 mM. Similar values were obtained when cultures were supplemented with 50 mM butyric acid initially or when a phosphate-buffered medium was used instead of an acetate-buffered medium. To measure the induction of the enzymes involved in solvent synthesis, we determined the rates of conversion of butyrate to butanol in growing cells. The rate of butanol formation reached a maximum in the mid-solvent phase, when the butanol concentration was 50 mM. Although more solvent accumulated later, de novo enzyme synthesis decreased and then ceased.     

Modulation of Acetone-Butanol-Ethanol Fermentation by Carbon Monoxide and Organic Acids

Metabolic modulation of acetone-butanol-ethanol fermentation by Clostridium acetobutylicum with carbon monoxide (CO) and organic acids is described. CO, which is a known inhibitor of hydrogenase, was found to be effective in the concentration range of dissolved CO corresponding to a CO partial pressure of 0.1 to 0.2 atm. Metabolic modulation by CO was particularly effective when organic acids such as acetic and butyric acids were added to the fermentation as electron sinks. The uptake of organic acids was enhanced, and increases in butyric acid uptake by 50 to 200% over control were observed. Hydrogen production could be reduced by 50% and the ratio of solvents could be controlled by CO modulation and organic acid addition. Acetone production could be eliminated if desired. Butanol yield could be increased by 10 to 15%. Total solvent yield could be increased 1 to 3% and the electron efficiency to acetone-butanol-ethanol solvents could be increased from 73 to 78% for controls to 80 to 85% for CO- and organic acid-modulated fermentations. Based on these results, the dynamic nature of electron flow in this fermentation has been elucidated and mechanisms for metabolic control have been hypothesized.     

Influence of pH and undissociated butyric acid on the production of acetone and butanol in batch cultures of Clostridium acetobutylicum

Summary The kinetics of growth and acid and solvent production are examined in batch fermentation of Clostridium acetobutylicum at pH between 4.5 and 6.0. At the lower pH, growth occurs in two consecutive phases and solvents are the main excreted metabolites. At the higher pH, there is a single growth phase with only acid formation. The influence of the pH can be correlated with a critical role of the concentration of undissociated butyric acid in the medium: cellular growth is inhibited above 0.5 g/l and solvent production starts at an undissociated acid level of 1.5 g/l. Reducing the intracellular acid dissociation by lowering the intracellular pH also favours the production of acetone and butanol.     

Effects of extractive fermentation on butyric acid production byClostridium acetobutylicum

Summary The addition of an oleyl alcohol extractant to a batch fermentation of glucose byClostridium acetobutylicum resulted in a concentration profile that was distinctly different from the non-extractive control fermentation. The concentration of butyric acid increased and subsequently decreased in the control fermentation. The concentration of butyric acid increased but did not subsequently decrease in the oleyl alcohol extractive fermentation. The production of butyric acid was found to have been prolonged into the solventogenic phase in the oleyl alcohol extractive fermentation. Butyric acid was continually replenished from glucose while it was being converted to butanol. Supplementation of exogenous acetic and butyric acids, the metabolic uncoupler carbonyl cyanide 3-chlorophenylhydrazone, or decanol to the oleyl alcohol extractive fermentation helped to reinstate the normal butyric acid concentration profile. These findings are discussed with respect to the effects of these additives on the pH ofC. acetobutylicum and its importance with regard to the production of butyric acid.     

Comparative investigations of growth and solvent formation in ‘Clostridium saccharoperbutylacetonicum’ DSM 2152 and Clostridium acetobutylicum DSM 792

The butanol and acetone-producing strain DSM 2152, invalidly described as ‘Clostridium saccharoperbutylacetonicum’ is compared with the type strain C. acetobutylicum, DSM 792, with respect to solvent and acid formation at varying pH values and growth rates. Batch cultures, product-limited chemostat and pH-auxostat cultures were used for characterization. Under all conditions strain DSM 2152 produced much lower amounts of butyric and acetic acids than the type strain. The pH optimum for solvent formation was higher, ie 5.5 instead of 4.5. Solvent formation occurred at higher dilution rates, but below 0.1 h⁻¹ a lower solvent concentration was obtained, indicating that acid production was too low to provide a sufficient amount for acetone formation. The results are discussed in the light of recent publications on the taxonomy of butanol-acetone producing clostridia using 16S rRNA sequence analysis and other nucleic acid data. The presently suggested ‘phylogenetic’ classification of the collective species, C. acetobutylicum, is also reflected in the fermentation characteristics. Received 21 December 1998/ Accepted in revised form 22 January 1999     

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.     

Ethanol production from glucose byClostridium thermosaccharolyticum strains: Effect of pH and temperature

Summary The fermentation of glucose byClostridium thermosaccharolyticum strains IMG 2811^T, 6544 and 6564 was studied in batch culture in a complex medium at different temperatures in defined and free-floating pH conditions. All the strains ferment 5 g glucose.l^–1 completely. The yield of the fermentation products turned out to be independent of the incubation temperature for strain IMG 2811^T. Strain IMG 6544 produced at 60°C significantly more ethanol and less acetic acid, butyric acid, hydrogen gas and biomass than at lower temperatures. With strain IMG 6564, the opposite effect occurred: ethanol appeared to be the main fermentation product at 45°C; at 60°C less ethanol and more acetic acid, butyric acid and hydrogen gas was formed.Experiments, carried out with strain IMG 6564, at defined pH conditions (between 5.5 and 7) and different temperatures (45, 55 and 60°C) revealed no effect of the incubation temperature, but an important effect of the pH on the product formation. At pH 7, ethanol was the main fermentation product while minor amounts of hydrogen gas, acetic and butyric acid were produced. Lowering the pH gradually to 5.5 resulted in a decrease of ethanol and an increase of biomass, hydrogen gas, acetic, butyric and lactic acids. At pH higher than 7 no growth occurred. Similar conclusions could be drawn for strains IMG 2811^T and 6544.     

Formic acid triggers the "Acid Crash" of acetone-butanol-ethanol fermentation by Clostridium acetobutylicum

Solvent production by Clostridium acetobutylicum collapses when cells are grown in pH-uncontrolled glucose medium, the so-called "acid crash" phenomenon. It is generally accepted that the fast accumulation of acetic acid and butyric acid triggers the acid crash. We found that addition of 1 mM formic acid into corn mash medium could trigger acid crash, suggesting that formic acid might be related to acid crash. When it was grown in pH-uncontrolled glucose medium or glucose-rich medium, C. acetobutylicum DSM 1731 containing the empty plasmid pIMP1 failed to produce solvents and was found to accumulate 0.5 to 1.24 mM formic acid intracellularly. In contrast, recombinant strain DSM 1731 with formate dehydrogenase activity did not accumulate formic acid intracellularly and could produce solvent as usual. We therefore conclude that the accumulation of formic acid, rather than acetic acid and butyric acid, is responsible for the acid crash of acetone-butanol-ethanol fermentation.     

Enhanced Butanol Production by Clostridium beijerinckii BA101 Grown in Semidefined P2 Medium Containing 6 Percent Maltodextrin or Glucose

Dramatically elevated levels of butanol and acetone resulted in higher butanol and total solvent yields for hyperamylolytic Clostridium beijerinckii BA101 relative to the NCIMB 8052 parent strain grown in semidefined P2 medium containing either 6% glucose or STAR-DRI 5 maltodextrin. C. beijerinckii BA101 consistently produced on the order of 19 g of butanol per liter in 20-liter batch fermentations. This represents a greater than 100% increase in butanol concentration by the BA101 strain compared to the parent NCIMB 8052 strain. The kinetics of butanol production over time also indicate a more rapid rate of butanol production by BA101 in semidefined P2 medium containing glucose or maltodextrin. The lower levels of butyric and acetic acids produced over the course of the fermentation carried out by BA101 are consistent with an enhanced capacity for uptake and recycling of these acids. C. beijerinckii BA101 appears to more completely utilize carbohydrate compared to the 8052 strain. Carbon balance following fermentation by C. beijerinckii 8052 and BA101 indicates that sufficient carbon is available for the twofold increase in butanol concentration observed during BA101 fermentations. C. beijerinckii BA101 also has superior solvent production capacity during continuous culture fermentation in P2 medium containing 6% glucose. Volumetric solvent yields of 0.78 and 1.74 g/liter/h for BA101 and 0.34 and 1.17 g/liter/h for NCIMB 8052 were obtained at dilution rates of 0.05 and 0.20 h(sup-1), respectively. No drift towards acid synthesis (strain degeneration) was observed for up to 200 h (d = 0.05 h(sup-1)) and 100 h (d = 0.20 h(sup-1)).     

酪丁酸梭菌代谢工程菌的构建及其发酵特性

酪丁酸梭菌Clostridium tyrobutyricum可以利用葡萄糖、木糖、纤维二糖、阿拉伯糖等多种底物进行产酸发酵,主要发酵产物为丁酸和乙酸,是一种适合于木质纤维素同步糖化发酵生产丁酸的菌种。将酪丁酸梭菌乙酸发酵关键基因取代为丁酸发酵关键基因来构建突变株,可使突变株丁酸发酵量增多,乙酸发酵量减少。分别获得来源于丙酮丁醇梭菌的丁酸代谢关键酶基因——乙酰乙酰辅酶A转移酶基因(thl)、来源于酪丁酸梭菌本身的乙酸代谢关键酶基因片段——磷酸转乙酰基酶基因片段(pta)和来源于质粒pIMP1的红霉素抗性基因(em)。将它们与质粒pUC19相连构建为非复制性质粒pUC19-EPT。通过电转化将其导入酪丁酸梭菌中。利用红霉素抗性平板筛选获得转化子,通过PCR验证发现,获得的突变株染色体上pta被thl替换。在以葡萄糖为底物的发酵中,突变株丁酸得率为0.47,较野生型增大了34%,乙酸得率为0.05,较野生型下降了29%。