Effects of pH and acetic acid on homoacetic fermentation of lactate by Clostridium formicoaceticum

Clostridium formicoaceticum homofermentatively converts lactate to acetate at 37 degrees C and pH 6.6-9.6. However, this fermentation is strongly inhibited by acetic acid at acidic pH. The specific growth rate of this organism decreased from a maximum at pH 7.6 to zero at pH 6.6. This inhibition effect was found to be attributed to both H(+) and undissociated acetic acid. At pH values below 7.6, the H(+) inhibited the fermentation following non-competitive inhibition kinetics. The acetic acid inhibition was found to be stronger at a lower medium pH. At pH 6.45-6.8, cell growth was found to be primarily limited by a maximum undissociated acetic acid concentration of 0.358 g/L (6mM). This indicates that the undissociated acid, not the dissociated acid, is the major acid inhibitor. At pH 7.6 or higher, this organism could tolerate acetate concentrations of higher than 0.8M, but salt (Na(+)) became a strong inhibitor at concentrations of higher than 0.4M. Acetic acid inhibition also can be represented by noncompetitive inhibition kinetics. A mathematical model for this homoacetic fermentation was also developed. This model can be used to simulate batch fermentation at any pH between 6.9 and 7.6.     

Aerobic Fermentation and the Depletion of the Amino Acid Pool in Yeast Cells

The amino acid pool of yeast cells, Saccharomyces cerevisiae, incubated with galactose remains at a constant level for 100 minutes. This is 30 minutes beyond the time at which the oxidative phase of the induced-enzyme formation begins. Washed yeast cells, the pools of which have been depleted 60 per cent by incubation with glucose, do not replenish their pools as do washed cells incubated without a substrate. These facts indicate that the induced enzymes are formed at least partially from pool-replenishing amino acids. The time of onset of pool depletion is the time at which the aerobic fermentation phase of induced-enzyme formation begins for cells incubated with galactose. With 0.1 per cent galactose the respiratory phase begins at 100 minutes but no aerobic fermentation nor pool depletion occurs. The rates of respiration and aerobic fermentation are constant for four glucose concentrations from 0.1 to 1.0 per cent. The amount of aerobicfermentation is proportional to the initial concentration of glucose. Amino acid pool depletion occurs for all concentrations but depletion ceases and is followed by pool replenishment after aerobic fermentation is complete. Ultraviolet radiations, which delay the appearance of the respiratory phase of induced-enzyme formation, completely eliminate both the appearance of aerobic fermentation and pool depletion. The results indicate an intimate association between aerobic fermentation and amino acid pool depletion.     

Propagated fixed-bed mixed-acid fermentation: Part I: Effect of volatile solid loading rate and agitation at high pH

Countercurrent fermentation is a high performing process design for mixed-acid fermentation. However, there are high operating costs associated with moving solids, which is an integral component of this configuration. This study investigated the effect of volatile solid loading rate (VSLR) and agitation in propagated fixed-bed fermentation, a configuration which may be more commercially viable. To evaluate the role of agitation on fixed-bed configuration performance, continuous mixing was compared with periodic mixing. VSLR was also varied and not found to affect acid yields. However, increased VSLR and liquid retention time did result in higher conversions, productivity, acid concentrations, but lower selectivities. Agitation was demonstrated to be important for this fermentor configuration, the periodically-mixed fermentation had the lowest conversion and yields. Operating at a high pH (～9) contributed to the high selectivity to acetic acid, which might be industrially desirable but at the cost of lower yield compared to a neutral pH.     

Whey fermentation by immobilized cells of Propionibacterium shermanii

Growth of Propionibacterium shermanii B-123 was faster on media containing lactate than on that containing lactose. Cheese whey was therefore fermented with Lactobacillus helveticus and neutralized with NaOH or Ca(OH)₂, before inoculation with B-123. Fermentation rate by immobilized propionibacteria was best in Ca(OH)₂-neutralized whey, and at lactate concentrations between 1 and 2%. Calcium propionate concentrations of 1 and 3% reduced fermentation rates by 40% and 55% respectively. Optimum temperature for propionate fermentation by immobilized cells was 37°C. Ratios of propionic acid to acetic acid increased as incubation temperature was increased. Agitation increased propionic acid fermentation rates but lowered the ratio of propionic acid to acetic acid. Beads containing immobilized propionibacteria were re-utilized for ten consecutive fermentations. Fermentation rates increased upon re-utilization. Escherichia coli and Staphylococcus aureus were inhibited by the propionic fermentation but did not die; they kept growing at a reduced rate.     

木质纤维素酸解副产物对D-乳酸生产菌Sporolactobacillus sp.Y2-8生长及发酵的影响

选择乙酸根、糠醛、5-羟甲基糠醛、苯酚、香草酸和丁香醛等6种典型木质纤维素酸解副产物,考察它们对D-乳酸生产菌Sporolactobacillus sp.Y2-8生长及发酵的影响。实验结果表明:酚类物质抑制作用最强烈,0.25 g/L丁香醛已经完全抑制了菌体的生长和D-乳酸的发酵;苯酚和香草酸在低浓度(≤1.0 g/L)时抑制作用较小,但质量浓度达到3 g/L时对D-乳酸产量的抑制率分别为99%和70%;3 g/L糠醛和5-羟甲基糠醛对产物的抑制率分别为60%与20%,抑制作用小于酚类;乙酸根的影响最小,10 g/L的乙酸钠对菌体的生长和发酵几乎无抑制作用;当抑制物混合时,存在着相互促进作用,抑制作用更强烈。     

反相高效液相色谱法测定肠球菌FQ15发酵液中的有机酸

目的研究肠球菌FQ15发酵液中的有机酸在不同发酵时间的变化趋势。方法建立反相高效液相色谱法测定此株益生菌发酵液中有机酸的主要成分及其在发酵不同时间的变化趋势。结果丙酸、丙酮酸、乳酸、乙酸的浓度都是在菌体生长处于衰亡期时达到最大值,乳酸随发酵时间的延长浓度明显下降,而乙酸在发酵后期含量呈上升趋势。结论此方法重现性好,精密度高,为研究微生物合成中有机酸种类及变化趋势提供了一种可供参考的快捷分析手段。     

玉米秸秆酸解副产物对重组酿酒酵母6508-127发酵的影响

将木质纤维素类生物质如玉米秸秆等用稀酸水解预处理,在半纤维素水解为单糖的同时,水解液中还会产生一些可能对后续发酵有影响的副产物。本实验分别考查了在玉米秸秆稀酸水解液中检测出的乙酸、甲酸、香草醛、糠醛和羟甲基糠醛对重组木糖发酵菌株S. cerevisiae 6508-127生长和发酵的影响。结果表明,甲酸和乙酸对菌体生长的抑制强于乙醇生成,且甲酸的抑制程度远大于乙酸;2g/L香草醛可使菌体生长延滞期明显延长,而在较低浓度（≤1.2g/L）此现象不明显。糠醛在0.5-1.5g/L范围内对菌体生长有抑制作用,但使乙醇得率提高;羟甲基糠醛在0.2g/L浓度存在就使乙醇得率有明显降低,但使生物量得率提高;研究中还发现,糠醛、羟甲基糠醛和香草醛可被S. cerevisiae 6508-127代谢。     

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.     

Mechanism of action of benzoic acid on Zygosaccharomyces bailii: effects on glycolytic metabolite levels, energy production, and intracellular pH.

The effects of benzoic acid in the preservative-resistant yeast Zygosaccharomyces bailii were studied. At concentrations of benzoic acid up to 4 mM, fermentation was stimulated and only low levels of benzoate were accumulated. Near the MIC (10 mM), fermentation was inhibited, ATP levels declined, and benzoate was accumulated to relatively higher levels. Intracellular pH was reduced but not greatly. Changes in the levels of metabolites at different external benzoic acid levels showed that glycolysis was limited at pyruvate kinase and glyceraldehyde dehydrogenase-phosphoglycerate kinase steps. Inhibition of phosphofructokinase and several other glycolytic enzymes was not responsible for the inhibition of fermentation. Instead, the results suggest that the primary action of benzoic acid in Z. bailii is to cause a general energy loss, i.e., ATP depletion.     

Mechanism of action of benzoic acid on Zygosaccharomyces bailii: effects on glycolytic metabolite levels, energy production, and intracellular pH.

The effects of benzoic acid in the preservative-resistant yeast Zygosaccharomyces bailii were studied. At concentrations of benzoic acid up to 4 mM, fermentation was stimulated and only low levels of benzoate were accumulated. Near the MIC (10 mM), fermentation was inhibited, ATP levels declined, and benzoate was accumulated to relatively higher levels. Intracellular pH was reduced but not greatly. Changes in the levels of metabolites at different external benzoic acid levels showed that glycolysis was limited at pyruvate kinase and glyceraldehyde dehydrogenase-phosphoglycerate kinase steps. Inhibition of phosphofructokinase and several other glycolytic enzymes was not responsible for the inhibition of fermentation. Instead, the results suggest that the primary action of benzoic acid in Z. bailii is to cause a general energy loss, i.e., ATP depletion.     

Kinetics and mathematical modeling of homoacetic fermentation of lactate by Clostridium formicoaceticum

Fermentation kinetics of Clostridium formicoaceticum grown on lactate at pH 7.0 and 35 degrees C was studied. Acetate was the only fermentation product and its production was growth associated. The growth of this bacterium was insensitive to the lactate concentrations studied, but was inhibited by acetic acid. A Monod-type expression with product inhibition similar to the noncompetitive inhibition of enzyme kinetics was used to model the batch fermentation. An integrated equation was developed and used to help estimating the kinetic parameters in the model. This mathematical model can be used to simulate the homoacetic fermentation of lactate by C. formicoaceticum at pH 7.0 and 35 degrees C.     

Effect of Benzoic Acid on Growth Yield of Yeasts Differing in Their Resistance to Preservatives

Yeasts grown in the presence of benzoic acid tolerated 40 to 100% higher benzoic acid concentrations than did those grown in the absence of weak-acid-type preservatives. They also accumulated less benzoate in the presence of glucose. In chemostat cultures, benzoic acid reduced growth yield and the rate of cell production but increased specific fermentation rates. Benzoate contents were lower than those required for equilibrium when cells were impermeable to benzoate anion. Intracellular pHs were maintained near neutrality. Between species, stimulation of fermentation was inversely related to preservation resistance but was unrelated to the maximum rate of fermentation. The results show that a major effect of benzoic acid on yeasts in the presence of an energy source is the energy requirement for the reduction in cytoplasmic benzoate concentration and maintenance of pH. This energy source is unavailable for growth, resulting in lower growth yields and rates. Resistant species may be less permeable to undissociated benzoic acid.     

Liquid–liquid extraction of fermentation inhibiting compounds in lignocellulose hydrolysate

Several compounds that are formed or released during hydrolysis of lignocellulosic biomass inhibit the fermentation of the hydrolysate. The use of a liquid extractive agent is suggested as a method for removal of these fermentation inhibitors. The method can be applied before or during the fermentation. For a series of alkanes and alcohols, partition coefficients were measured at low concentrations of the inhibiting compounds furfural, hydroxymethyl furfural, vanillin, syringaldehyde, coniferyl aldehyde, acetic acid, as well as for ethanol as the fermentation product. Carbon dioxide production was measured during fermentation in the presence of each organic solvent to indicate its biocompatibility. The feasibility of extractive fermentation of hydrolysate was investigated by ethanolic glucose fermentation in synthetic medium containing several concentrations of furfural and vanillin and in the presence of decanol, oleyl alcohol and oleic acid. Volumetric ethanol productivity with 6 g/L vanillin in the medium increased twofold with 30% volume oleyl alcohol. Decanol showed interesting extractive properties for most fermentation inhibiting compounds, but it is not suitable for in situ application due to its poor biocompatibility. Biotechnol. Bioeng. 2009;102: 1354–1360. © 2008 Wiley Periodicals, Inc.     

Influence of valine and other amino acids on total diacetyl and 2,3-pentanedione levels during fermentation of brewer’s wort

Undesirable butter-tasting vicinal diketones are produced as by-products of valine and isoleucine biosynthesis during wort fermentation. One promising method of decreasing diacetyl production is through control of wort valine content since valine is involved in feedback inhibition of enzymes controlling the formation of diacetyl precursors. Here, the influence of valine supplementation, wort amino acid profile and free amino nitrogen content on diacetyl formation during wort fermentation with the lager yeast Saccharomyces pastorianus was investigated. Valine supplementation (100 to 300 mg L^?1) resulted in decreased maximum diacetyl concentrations (up to 37 % lower) and diacetyl concentrations at the end of fermentation (up to 33 % lower) in all trials. Composition of the amino acid spectrum of the wort also had an impact on diacetyl and 2,3-pentanedione production during fermentation. No direct correlation between the wort amino acid concentrations and diacetyl production was found, but rather a negative correlation between the uptake rate of valine (and also other branched-chain amino acids) and diacetyl production. Fermentation performance and yeast growth were unaffected by supplementations. Amino acid addition had a minor effect on higher alcohol and ester composition, suggesting that high levels of supplementation could affect the flavour profile of the beer. Modifying amino acid profile of wort, especially with respect to valine and the other branched-chain amino acids, may be an effective way of decreasing the amount of diacetyl formed during fermentation.     

Influence of the glycolytic rate on production of citric acid and oxalic acid by Aspergillus niger in solid state fermentation

A study was performed to understand the physiology and biochemical mechanism of citric acid accumulation during solid state fermentation of sweet potato using Aspergillus niger Yang No.2. A low citrate-producing mutant was isolated followed by a comparative study of the fermentation process and selected physiological and biochemical parameters. In contrast with the parent strain, the mutant strain displayed lower concentrations, yields and production rates of citric acid, accompanied by higher concentrations, yields and production rates of oxalic acid. In addition, the mutant utilized starch at a lower rate although higher concentrations of free glucose accumulated in the cultures. Biochemical analyses revealed lower rates of glucose uptake and hexokinase activity of the mutant strain in comparison with the parent strain. It is proposed that, in common with submerged fermentation, over-production of citric acid in solid state fermentation is related to an increased glucose flux through glycolysis. At low glucose fluxes, oxalic acid is accumulated.     

Production of butyric acid by batch fermentation of cheese whey withClostridium beijerinckii

Summary The effect of pH on the fermentation of butyric acid byClostridium beijerinckii using cheese whey as a substrate was studied. Maximum concentrations of the acid were produced when the pH was controlled at 5.5. Raising or lowering of pH was found to reduce the total acid formation. This particular strain ofC. beijerinckii produced insignificant amounts of butanol in all the pure culture cases investigated. A comparative study of the fermentation in a synthetic glucose medium and in cheese whey showed the whey to produce more butyric acid.     

Biochemical changes during the fermentation of Prosopis africana seeds for ogiri-okpei production

Biochemical changes during fermentation of seeds of Prosopis africana for production of ogiri-okpei, a food condiment popular among people of West Africa were studied. Fermentation resulted in a net increase in concentrations of total soluble sugars and free amino acids, both reaching a peak after 72 h of fermentation but declining thereafter. Corresponding increases were observed in amylase and protease activities, respectively. Lipase activity was observed to be very strong, increasing throughout the duration of fermentation. Analyses of amino and fatty acid composition using an amino acid analyzer and gas liquid chromatography, respectively, revealed a wide variety of amino acids including glutamine > cystine > arginine and the fatty acids stearic > Arachidic > linolenic > linoleic in the unfermented seed in the highest concentrations. Fluctuations in the concentrations of these compounds were observed during the fermentation. At the end of 96 h fermentation, glutamine > cystine > lysine and an unidentified fatty acid > arachidic > linolenic acids were found in the highest concentrations. Marked increases in composition with increasing period of fermentation were observed for Ca, P, K, Mn, and Z. Transformations of amino acids, fatty acids, and minerals during the fermentation of this seed revealed during this study will contribute towards the development of an industrial process for ogiri-okpei as well as an understanding of its contribution to the nutrition of its consumers.     

Effects of propionate and acetate additions on solvent production in batch cultures of Clostridium acetobutylicum

Addition of acetate or propionate to uncontrolled-pH batch cultures does not affect the initiation of solventogenesis but does enhance final solvent concentrations compared with those of unchallenged cultures. This observation can be explained in terms of the increased buffering capacity of the medium brought about by the added acids, resulting in protection against premature growth inhibition due to low culture pH values at the end of the fermentation. The uptake of propionic acid from the medium does not proceed solely via the coenzyme A-transferase pathway, since less acetone than propanol is formed. Therefore, at least 50% of the propionic acid is taken up through the reversed kinase-phosphotransbutyrylase reaction pathway.     

Effects of propionate and acetate additions on solvent production in batch cultures of Clostridium acetobutylicum.

Addition of acetate or propionate to uncontrolled-pH batch cultures does not affect the initiation of solventogenesis but does enhance final solvent concentrations compared with those of unchallenged cultures. This observation can be explained in terms of the increased buffering capacity of the medium brought about by the added acids, resulting in protection against premature growth inhibition due to low culture pH values at the end of the fermentation. The uptake of propionic acid from the medium does not proceed solely via the coenzyme A-transferase pathway, since less acetone than propanol is formed. Therefore, at least 50% of the propionic acid is taken up through the reversed kinase-phosphotransbutyrylase reaction pathway.     

Utilization of Molasses Sugar for Lactic Acid Production by Lactobacillus delbrueckii subsp. delbrueckii Mutant Uc-3 in Batch Fermentation

Efficient lactic acid production from cane sugar molasses by Lactobacillus delbrueckii mutant Uc-3 in batch fermentation process is demonstrated. Lactic acid fermentation using molasses was not significantly affected by yeast extract concentrations. The final lactic acid concentration increased with increases of molasses sugar concentrations up to 190 g/liter. The maximum lactic acid concentration of 166 g/liter was obtained at a molasses sugar concentration of 190 g/liter with a productivity of 4.15 g/liter/h. Such a high concentration of lactic acid with high productivity from molasses has not been reported previously, and hence mutant Uc-3 could be a potential candidate for economical production of lactic acid from molasses at a commercial scale.