Acetone, butanol and ethanol production from domestic organic waste by solventogenic clostridia

Domestic organic waste (DOW) was washed and dried to 85 % dryness by VAM (The Netherlands). This material contained 25.1 g glucose, 8.4 g xylose and 5.8 g other monosaccharides/100 g dry matter. Using Mansonite steam explosion and enzymatic hydrolysis, a hydrolysate containing 15.4 g glucose, 2.2 g xylose and 0.8 g other monosaccharides per l was made. Clostridium acetobutylicum DSM 1731 produced 1.5 and C. beijerinckii B-592 0.9 g/l ABE and Clostridium LMD 84.48 1.9 g/l IBE, respectively, from this hydrolysate without further supplementation. Incubation with 2 fold concentrated hydrolysate completely impaired ABE production. After removal of unspecific inhibiting components, the yield of ABE production by Clostridium acetobutylicum DSM 1731 increased about 3 fold as compared to the nontreated hydrolysate. From 4 fold concentrated, partially purified, hydrolysate containing 34.2 g glucose/l, ABE production was 9.3 g/l after 120 h as compared to 3.2 g ABE/I from non-concentrated hydrolysate which contained 12.0 g glucose/l after elution over the same column. The concentration of butyric acid in the fermented hydrolysates was 2.2 and 0.4 g/l, respectively. This reasonably low amount of butyric acid showed that the fermentation had proceeded quite well.     

The cause of "acid-crash" and "acidogenic fermentations" during the batch acetone-butanol-ethanol (ABE-) fermentation process

Experiments were performed to determine the cause of "acid crash", a phenomenon which occasionally occurs in pH-uncontrolled batch fermentations resulting in premature cessation of ABE (acetone butanol) production. The results indicate that "acid crash" occurs when the concentration of undissociated acids in the broth exceeds 57 - 60 mmol/l. Prevention can be achieved by introducing some limited pH control to minimize the concentration of undissociated acids or by slowing the metabolic rate, and thus the rate of acid production, by, for example, lowering the fermentation temperature. "Acidogenic fermentations", which occur when batch fermentations are performed at pH values close to neutrality, are due to rapid production of acids followed by inhibition of solventogenesis when the total acid concentration reaches 240 - 250 mmol/l. Solventogenesis can be achieved at these pH values by lowering the glucose uptake rate / acid production rate by use of e.g. elevated glucose or lowered yeast extract concentrations in the growth medium.     

Effects of butyric and acetic acids on acetone-butanol formation by Clostridium acetobutylicum

The actions of butyric and acetic acids on acetone-butanol fermentation are investigated. Production of butyric and acetic acids are controlled by the extracellular concentrations of both acids: acetic acid added to the medium inhibits its own formation but has no effect on butyric acid formation, and added butyric acid inhibits its own formation but not that of acetic acid. The ratio of end metabolites depends upon acetic and butyric acid quantities excreted during the fermentation. In contrast to acetic acid, which specifically increases acetone formation, butyric acid increases both acetone and butanol formations. Acetate and butyrate kinase activities were also examined. Both increase at the start of fermentation and decrease when solvents appear in the medium. Coenzyme A transferase activity is weak in the acidogenic phase and markedly increases in the solvent phase. Acetic and butyric acids appear to be co-substrates. On the basis of these results, a mechanism of acetic and butyric acid pathways, coupled to solvent formation by C. acetobutylicum glucose fermentation is proposed.     

THE PRODUCTION OF VOLATILE FATTY ACIDS BY BACTERIA OF THE DYSENTERY GROUP

These studies show: 1. A close agreement exists among all the organisms studied in the total quantity of volatile fatty acids produced and in the ratio of formic to acetic, under aerobic conditions, and in the presence of 1 per cent of glucose. 2. When grown upon peptone alone, with free access of air to the cultures, volatile fatty acids are produced in appreciable quantities, although the reaction of the solution has gone more alkaline as shown by colorimetric pH tests. Formic acid is not found, but in its place we obtain propionic acid. 3. Upon exhaustion of air from the non-sugar medium the bacteria again produce formic acid, and in addition some butyric. This is true for both Shiga and non-Shiga cultures. The reaction is distinctly more acid. 4. The presence of glucose in the medium from which the air has been pumped furnishes a condition which provokes about the same type and degree of fermentation that operates in the glucose medium bathed in air at atmospheric pressure. 5. The enormous quantity of formic acid produced by these bacteria may play a significant part in the digestive disturbances and toxic symptoms accompanying their infection of the human intestinal tract.     

Improvements of metabolites tolerance in <Emphasis Type="Italic">Clostridium acetobutylicum</Emphasis> by micronutrient zinc supplementation

Micronutrient zinc is of great importance for acetone-butanol-ethanol (ABE) fermentation by Clostridium acetobutylicum. The effect of zinc supplementation on toxic metabolites (formic, acetic, butyric acid and butanol) tolerance during ABE fermentation was investigated under various stress-shock conditions without pH control. Great improvements on cell growth, glucose utilization and butanol production were achieved. In the presence of 0.45 g/L formic acid, zinc contributed to 11.28 g/L butanol produced from 55.24 g/L glucose compared to only 5.27 g/L butanol from 29.49 g/L glucose in the control without zinc supplementation. More importantly, relatively higher levels of 7.5 g/L acetic acid, 5.5 g/L butyric acid and 18 g/L butanol could be tolerated by C. acetobutylicum with zinc supplementation while no fermentation was observed under the same stress-shock condition respectively, suggesting that the acids and butanol tolerance in C. acetobutylicum could be significantly facilitated by pleiotropic regulation of micronutrient zinc. Thus, this paper provides an efficient bioprocess engineering strategy for improving stress tolerance in Clostridium species.     

Engineering the robustness of Clostridium acetobutylicum by introducing glutathione biosynthetic capability

To improve the aero- and solvent tolerance of the solvent-producing Clostridium acetobutylicum, glutathione biosynthetic capability was introduced into C. acetobutylicum DSM1731 by cloning and over-expressing the gshAB genes from Escherichia coli. Strain DSM1731(pITAB) produces glutathione, and shows a significantly improved survival upon aeration and butanol challenge, as compared with the control. In addition, strain DSM1731(pITAB) exhibited an improved butanol tolerance and an increased butanol production capability, as compared with the recombinant strains with only gshA or gshB gene. These results illustrated that introducing glutathione biosynthetic pathway, which is redundant for the metabolism of C. acetobutylicum, can increase the robustness of the host to achieve a better solvent production.     

Physiological adaptations of anaerobic bacteria to low pH: metabolic control of proton motive force in Sarcina ventriculi.

Detailed physiological studies were done to compare the influence of environmental pH and fermentation end product formation on metabolism, growth, and proton motive force in Sarcina ventriculi. The kinetics of end product formation during glucose fermentation in unbuffered batch cultures shifted from hydrogen-acetate production to ethanol production as the medium pH dropped from 7.0 to 3.3. At a constant pH of 3.0, the production of acetate ceased when the accumulation of acetate in the medium reached 40 mmol/liter. At a constant pH of 7.0, acetate production continued throughout the entire growth time course. The in vivo hydrogenase activity was much higher in cells grown at pH 7.0 than at pH 3.0. The magnitude of the proton motive force increased in relation to a decrease of the medium pH from 7.5 to 3.0. When the organism was grown at pH 3.0, the cytoplasmic pH was 4.25 and the organism was unable to exclude acetic acid or butyric acid from the cytoplasm. Addition of acetic acid, but not hydrogen or ethanol, inhibited growth and resulted in proton motive force dissipation and the accumulation of acetic acid in the cytoplasm. The results indicate that S. ventriculi is an acidophile that can continue to produce ethanol at low cytoplasmic pH values. Both the ability to shift to ethanol production and the ability to continue to ferment glucose while cytoplasmic pH values are low adapt S. ventriculi for growth at low pH.     

Growth and butyric acid production by Clostridium populeti

The growth of Clostridium populeti in 2% (w/v) glucose medium containing 0.2% (w/v) yeast extract was optimal with 10 mM NH₄Cl as the nitrogen source. Although the maximum specific growth rate (=0.32 h^-1) with 5 mM NH₄Cl was similar, the biomass yield was about 30% lower than that at the optimum. Either sodium sulphide or cysteine-HCl at an optimum concentration of 0.33 mM and 5.0 mM respectively, could serve as the sole sulphur source for growth. The growth rate was unaffected by initial glucose concentrations of up to 10% (w/v), but in the presence of 15% glucose it declined by about 35%. The molar yield of butyric acid (mol/mol glucose) declined from 0.70 in 1% (w/v) initial glucose medium to 0.39 in 10% glucose medium. In 5.7% initial glucose medium, butyric acid levels of 6.3 g/l were obtained (0.56 mol butyrate/mol glucose) after 72 h of incubation in 2.5 l batch cultures. A decrease of about 50% in the maximum specific growth rate of C. populeti was observed in the presence of an initial concentration of either 1.2 g/l of butyric acid or 18.9 g/l of acetic acid.This paper is issued as NRCC No. 29032     

Clostridial strain degeneration

Abstract: Strain degeneration, the loss of the capacity to produce solvents and form spores, typically occurs when Clostridium acetobutylicum and related clostridia are repeatedly subcultured in batch culture or grown in continuous culture, as opposed to being grown from germinated, heat-treated spores. Several mechanisms for degeneration have been identified thus far. (i) Degeneration can be caused by excessive acidification of the culture during exponential growth. We present data interpreted to mean that C. beijerinckii (formerly C. acetobutylicum ) NCIMB 8052 cells ferment glucose to acetic and butyric acids at an uncontrolled rate, so that, during rapid growth, the rate of acid production can exceed the rate of induction of the solventogenic pathway enzymes. As a result, the medium pH drops to bactericical levels, and the cells cannot switch to solventogenesis and sporulation. The clostridia seem to be poised either to produce excess acids, or to initiate solventogenesis, depending on small differences in the rates of growth. (ii) We have isolated transposon-insertion mutants of C. beijerinckii NCIMB 8052 that are resistant to degeneration, suggesting the involvement of a regulatory region of the clostridial chromosome. (iii) Involvement of a global regulatory gene has been inferred in C. beijerinckii NCIMB 8052 which degenerates irreversibly in chemostat culture. (iv) Impairment of butanol formation due to a defect in NADH generation has been reported in an oligosporogenous strain which can revert to the non-degenerate phenotype. (v) In continuous culture, degenerate cells may be selected because they continue to divide, while the non-degenerate cells stop dividing and start differentiating.     

Extracellular glycosyl hydrolase activity of the clostridia producing acetone, butanol, and ethanol

Production of acetone, butanol, ethanol, acetic acid, and butyric acid by three strains of anaerobic bacteria, which we identified as Clostridium acetobutylicum, was studied. The yield of acetone and alcohols in 6% flour medium amounted to 12.7-15 g/l with butanol constituting 51.0-55.6%. Activities of these strains towards xylan, beta-glucan, carboxymethylcellulose, and crystalline and amorphous celluloses were studied. C. acertobutylicum 6, C. acetoburylicum 7, and C. acertobutylicum VKPM B-4786 produced larger amounts of acetone and alcohols and displayed higher cellulase and hemicellulase activities than the type strain C. acetobutylicum ATCC 824. It was demonstrated that starch in the medium could be partially substituted with plant biomass.     

Transport of acetic acid in Zygosaccharomyces bailii: effects of ethanol and their implications on the resistance of the yeast to acidic environments.

Cells of Zygosaccharomyces bailii ISA 1307 grown in a medium with acetic acid, ethanol, or glycerol as the sole carbon and energy source transported acetic acid by a saturable transport system. This system accepted propionic and formic acids but not lactic, sorbic, and benzoic acids. When the carbon source was glucose or fructose, the cells displayed activity of a mediated transport system specific for acetic acid, apparently not being able to recognize other monocarboxylic acids. In both types of cells, ethanol inhibited the transport of labelled acetic acid. The inhibition was noncompetitive, and the dependence of the maximum transport rate on the ethanol concentration was found to be exponential. These results reinforced the belief that, under the referenced growth conditions, the acid entered the cells mainly through a transporter protein. The simple diffusion of the undissociated acid appeared to contribute, with a relatively low weight, to the overall acid uptake. It was concluded that in Z. bailii, ethanol plays a protective role against the possible negative effects of acetic acid by inhibiting its transport and accumulation. Thus, the intracellular concentration of the acid could be maintained at levels lower than those expected if the acid entered the cells only by simple diffusion.     

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 Organic Acids on Shrimp Pathogen, <Emphasis Type="Italic">Vibrio harveyi</Emphasis>

Shrimp farming accounts for more than 40% of the world shrimp production. Luminous vibriosis is a shrimp disease that causes major economic losses in the shrimp industry as a result of massive shrimp kills due to infection. Some farms in the South Asia use antibiotics to control Vibrio harveyi, a responsible pathogen for luminous vibriosis. However, the antibiotic-resistant strain was found recently in many shrimp farms, which makes it necessary to develop alternative pathogen control methods. Short-chain fatty acids are metabolic products of organisms, and they have been used as food preservatives for a long time. Organic acids are also commonly added in feeds in animal husbandry, but not in aquaculture. In this study, growth inhibitory effects of short-chain fatty acids, namely formic acid, acetic acid, propionic acid, and butyric acid, on V. harveyi were investigated. Among four acids, formic acid showed the strongest inhibitory effect followed by acetic acid, propionic acid, and butyric acid. The minimum inhibitory concentration (MIC) of 0.035% formic acid suppressed growth of V. harveyi. The major inhibitory mechanism seems to be the pH effect of organic acids. The effective concentration 50 (EC₅₀) values at 96 h inoculation for all organic acids were determined to be 0.023, 0.041, 0.03, and 0.066% for formic, acetic, propionic, and butyric acid, respectively. The laboratory study results are encouraging to formulate shrimp feeds with organic acids to control vibrio infection in shrimp aquaculture farms.     

Characteristics of butanol fermentation by a low-acid-producing Clostridium acetobutylicum B18

Fermentation characteristics of Clostridium acetobutylicum B18 were studied in batch experiments with and without pH control. This strain is shown to be potentially useful in simultaneous acetone-butanol-ethanol fermentation-separation systems because of its low acid production. In a pH-uncontrolled batch culture this strain produced mostly solvents, including 15 g/l of butanol. Ethanol production was low. Strain B18 recycled organic acids more efficiently than other strains. In particular, butyric acid was completely recycled when glucose was not limiting. Yield of liquid products (solvents plus organic acids) and carbon recovery in total products (gas plus liquid) were 33.1–36.4 wt% and 90–91 mol%, respectively, for 20–80 g/l of initial glucose. Glucose consumption and the percentage of butanol among solvents were higher at 32°C than at 37°C. Strain B18 required approximately 0.4 g/l of undissociated butyric acid at the onset of solvent production in pH-uncontrolled batch culture. The low undissociated butyric acid requirement enabled this strain to produce 13.8 g/l of butanol at a controlled pH of 6.0.Contribution no. 19998 of the Minnesota Agricultural Experiment Station Correspondence to: C.-H. Park     

Evaluation of clastogenicity of formic acid, acetic acid and lactic acid on cultured mammalian cells

Using Chinese hamster ovary K1 cells, chromosomal aberration tests were carried out with formic acid, acetic acid and lactic acid, and the relationship between the pH of the medium and the clastogenic activity was examined. The medium used was Ham's F12 supplemented with 17 mM NaHCO3 and 10% fetal calf serum. All of these acids induced chromosomal aberrations at the initial pH of ca. 6.0 or below (about 10-14 mM of each acid) both with and without S9 mix. Exposure of cells to about pH 5.7 or below (about 12-16 mM of each acid) was found to be toxic. When the culture medium was first acidified with each of these acids and then neutralized to pH 6.4 or pH 7.2 with NaOH, no clastogenic activity was observed. Using F12 medium supplemented with 34 mM NaHCO3 as a buffer, no clastogenic activity was observed at doses up to 25 mM of these acids (initial pH 5.8-6.0). However, it was found that about 10% of the cells had aberrations at pH 5.7 or below (27.5-32.5 mM of each acid). Furthermore, when 30 mM HEPES was used as a buffer, chromosomal aberrations were not induced at doses up to 20 mM formic acid and acetic acid (initial pH 7.0-7.1), and at doses up to 30 mM lactic acid (initial pH 6.6). In the initial pH range of 6.4-6.7 (25-32.5 mM of each acid), chromosomal aberrations were observed. The above results show that these acids themselves are non-clastogenic, and the pseudo-positive reactions attributable to non-physiological pH could be eliminated by either neutralization of the treatment medium or enhancement of the buffering ability.     

Cellulose: Energy source for microbial protein

Mixed cultures of bacteria anaerobically attacking cellulosic materials produce sufficient acetic, butyric, lactic and formic acids and ethanol and glucose to account for most of the original carbon. These products contain 60 to 90% of the free energy of the cellulose and are all usable as carbon sources for the aerobic growth of yeast.     

Anaerobic l-lactate degradation by Lactobacillus plantarum

Abstract Lactobacillus plantarum strains used as silage inoculants were investigated for their ability to metabolize lactic acid anaerobically after prolonged incubation (7–30 days) when glucose was absent from the medium. When citrate was present in the medium together with glucose during the initial fermentation, the lactic acid produced was degraded. Citrate was concomitantly degraded, resulting in accumulation of formic, acetic and succinic acids along with CO₂. The anaerobic degradation was confirmed by the use of l ¹⁴C(U) labelled lactate. The existence of pyruvate formate lyase in L. plantarum was indicated by using ¹⁴C-labelled pyruvate and HPLC identification of end-products. The 1-¹⁴C-carboxylic acid group of pyruvate was converted to formic acid, and the 3-¹⁴C was found in acetic acid. The key enzyme(s) in this metabolic pathway appears to require anaerobic conditions and induction by citrate.     

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%。     

Phenotypic and genotypic differences between certain strains of Clostridium acetobutylicum

Abstract It has become evident that several of the strains of Clostridium acetobutylicum that have been employed in physiological studies of the acetone-butanol fermentation, are heterogeneous. Studies of the phenotypic and genotypic characteristics of several of these strains (involving inter alia both pyrolysis mass spectrometry and 16S rRNA sequence determinations) demonstrated that the type strain obtained from ATCC was not identical with that supplied by NCIMB, and that NCIMB 8052T is in fact Clostridium beijerinckii . We therefore suggest that the name Clostridium acetobutylicum should be restricted to those strains that are genetically closely related to ATCC 824T (which include strains DSM 792 and DSM 1731 but not strain P262).     

Isolation and characterization of a cyanide-utilizing Burkholderia cepacia strain

A bacterium that utilizes cyanide as a nitrogen source was isolated from soil after enrichment in a liquid medium containing potassium cyanide (10mM) and glucose (1.0%, w/v). The strain could tolerate and grow in potassium cyanide at concentrations of up to 25mM. It could also utilize potassium cyanate, potassium thiocyanate, linamarin and a range of aliphatic and aromatic nitriles. The isolate was tentatively identified as Burkholderia cepacia strain C-3. Ammonia and formic acid were found in the culture supernatant of the strain grown on fructose and potassium cyanide, no formamide was detected, suggesting a hydrolytic pathway for the degradation of cyanide. The cyanide-degrading activity was higher in early and the stationary phase cells. Crude cell extracts of strain C-3 grown on nutrient broth exhibited cyanide-degrading activity. The characteristics of strain C-3 suggest that it would be useful in the bioremediation of cyanide-containing waste.