Buffering as a means for increasing growth and butanol production byClostridium acetobutylicum

Summary The objective of this work was to optimize butanol formation in the acetone-butanol-ethanol (ABE) fermentation by examining the level of buffering as it affects the dissociation of butyric acid to the less toxic butyrate anion. Experiments were carried out in batch culture using chemically defined (P2) or complex media containing various buffering agents. These included salts of acetate, citrate, phosphate, nitrate, or bicarbonate, representing a range of pK _a values and buffering capacities. Growth in highly buffered medium was found to increase the stationary phase cell density, carbohydrate utilization, and the final butanol concentration. At higher levels of buffering, increased growth and elevated concentrations of butyric acid were required to initiate solventogenesis, suggesting the involvement of a critical threshold level of undissociated butyric acid.     

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.     

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     

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.     

Fermentation of raw glycerol to 1,3-propanediol by new strains ofClostridium butyricum

Industrial glycerol obtained through the transesterification process using rapeseed oil did not support growth of several strains ofClostridium butyricum obtained from bacterial culture collections. Ten new strains ofC. butyricum were obtained from mud samples from a river, a stagnant pond, and a dry canal. These new isolates fermented the commercial glycerol and produced 1,3-propanediol as a major fermentation product with concomitant production of acetic and butyric acids. Four of the ten isolates were able to grow on industrial glycerol obtained from rapeseed oil. One strain,C. butyricum E5, was very resistant to high levels of glycerol and 1,3-propanediol. Using fed-batch fermentation, 109 g L^–1 of industrial glycerol were converted into 58 g of 1,3-propanediol, 2.2 g of acetate and 6.1 g of butyrate per liter.     

Growth and survival ofAzospirillum brasilense andArthrobacter giacomelloi in binary continuous culture

Summary Azospirillum brasilense andArthrobacter giacomelloi were grown in single and mixed succinate-limited continuous cultures at a partial oxygen pressure of 0.01atm. Growth, viability and survival during nutrient starvation were examined at various dilution rates. At D=0.05 h^–1, K_s values for succinate consumed were calculated.Arthrobacter giacomelloi viability was inversely related to dilution rate whereasAzo. brasilense was directly related. Slightly lower values of viability were obtained in mixed culture, but the ratio between the microorganisms was constant. The survival ofArth. giacomelloi in single culture decreased with increasing growth rate while survival ofAzo. brasilense was directly related to dilution rate. Acetylene reduction activity was generally very low in both single and mixed cultures. Respiration rate was also determined and the mixed culture showed an oxygen uptake rate higher than that of single cultures.Research work supported by CNR, Italy. Special grant I.P.R.A. Sub-project 1. Paper N. 317.     

Organic acids and water-soluble phenolics produced by Paxillus sp. 60/92 together show antifungal activity against Pythium vexans under acidic culture conditions

Ectomycorrhizal fungi can produce antifungal compounds in vitro as well as in symbiosis with the host plant that can reduce root diseases. The objective of this study was to isolate antifungal compounds from culture filtrate of Paxillus sp. 60/92, which can form mycorrhizas with Picea glehnii seedlings. Culture filtrate of Paxillus sp. 60/92 showed antifungal activity against Pythium vexans at pH 3–4 but not at pH 5–10, although sterile MMN-b liquid medium (pH 3–10) did not show antifungal activity. Upon separation of antifungal compounds in the culture filtrate, antifungal activity was detected in the organic acid and water-soluble phenolics fractions adjusted to pH 3. Although antifungal activity of individual fractions was lower than that of the culture filtrate, a mixture of these fractions showed antifungal activity similar to that of the culture filtrate. Furthermore, antifungal activity of oxalic acid, which is known to be produced by Paxillus involutus, was increased by mixing with the water-soluble phenolic fraction. Our findings indicate that Paxillus sp. 60/92 produces organic acids and water-soluble phenolics that together show antifungal activity at pH 3–4 against P. vexans.     

Enzymatic properties of lipase and characteristics production byLactobacillus delbrueckii subsp.bulgaricus

Some properties of an extracellular lipase produced byLactobacillus delbrueckii subsp.bulgaricus were studied. Maximum enzyme activity was found against olive and butter oil as enzyme substrates. Addition of 9% acacia gum, 0.1% Na-deoxycholate and 0.01 M CaCl₂ to the enzyme reaction mixture increased-lipase activity from 5.3 to 14.5 (FFA/mg protein/minute) at pH 6.0 and at 40° C. Maximum lipase production was reached in the presence of glucose as a sole source of carbon, wheat bran as nitrogen source, olive oil as a sole lipid source and butyric acid as fatty acid supporting the growth medium. An initial pH value of the culture medium of 6.0 and a temperature of 35° C gave the highest lipolytic activity.     

The Influence of Ammonium Nitrate,pH and Indole Butyric Acid on Root Induction and Survival in Soil of Micropropagated <Emphasis Type="Italic">Eucalyptus globulus</Emphasis>

Rooting of Eucalyptus globulus shoots was influenced by the concentration of the indole butyric acid (IBA) and NH₄ ⁺ in the root-induction medium. Optimum plantlet vigor and survival were achieved using low concentrations (1 – 2.5 μM) of IBA and when NH₄NO₃ was removed. Removal of NH₄ ⁺ also had a significant effect on medium pH, its presence caused a decrease in pH as the culture period proceeded. When different nitrate compounds (excluding NH₄NO₃) were used as the nitrogen source, the medium pH was more stable and this was associated with higher root production. The higher root production, in association with appropriate IBA concentrations, produced plantlets with higher survival and better growth on transfer to soil. This revised version was published online in July 2006 with corrections to the Cover Date.     

Influence of short chain fatty acids and lysine on Salmonella typhimurium cadA expression

In Salmonella typhimurium, cadA has a role in virulence expression and is an inducible gene that responds to external lysine concentration. In this study, a strain of S. typhimurium carrying a cadA: lacZ fusion was used to determine if the induction of cadA occurred under different lysine concentrations and mildly acid conditions in the presence of short chain fatty acids. Aliquots of an 18-h culture of S. typhimurium were placed on fresh media containing different lysine concentrations at pH 5.8 adjusted by addition of HCl or by 1 M short chain fatty acids (SCFA, acetic, propionic and butyric acid) stock solution. After an induction period of 2 h, -galactosidase activities were assayed. Expression of cadA in rich medium was significantly higher than that of minimal medium at neutral pH and different lysine concentrations. In contrast, at pH 5.8, there was a significant increase in cadA expression, particularly when pH was adjusted using HCl at all lysine levels. Addition of a mixture of organic acids yielded an overall lower cadA expression at all lysine levels studied when compared to HCl. However, each SCFA challenge (individual or as a mixture) caused a high level of expression, both at neutral and acidic pH. Based on these results it is apparent that in the presence of external lysine, SCFA and nutrient availability can influence cadA expression in S. typhimurium.     

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.     

Optimum conditions for the biological production of lactic acid by a newly isolated lactic acid bacterium,Lactobacillus sp. RKY2

Lactic acid is a green chemical that can be used as a raw material for biodegradable polymer. To produce lactic acid through microbial fermentation, we previously screened a novel lactic acid bacterium. In this work, we optimized lactic acid fermentation using a newly isolated and homofermentative lactic acid bacterium. The optimum medium components were found to be glucose, yeast extract, (NH₄)₂HPO₄, and MnSO₄. The optimum pH and temperature for a batch culture ofLactobacillus sp. RKY2 was found to be 6.0 and 36°C, respectively. Under the optimized culture conditions, the maximum lactic acid concentration (153.9 g/L) was obtained from 200 g/L of glucose and 15 g/L of yeast extract, and maximum lactic acid productivity (6.21 gL⁻¹h⁻¹) was obtained from 100 g/L of glucose and 20 g/L of yeast extract. In all cases, the lactic acid yields were found to be above 0.91 g/g. This article provides the optimized conditions for a batch culture ofLactobacillus sp. RKY2, which resulted in highest productivity of lactic acid.     

Directed metabolic flow with high butanol yield and selectivity in continuous cultures ofClostridium acetobutylicum

Summary This work addresses the problem of stable butanol formation byClostridium acetobutylicum in continuous culture. Sustained altered electron flow was observed in the presence of benzyl viologen which serves to redirect carbon flow towards primarily butanol formation. A yield of butanol of over 0.28 g.g^–1 glucose was obtained and butanol comprised over 90% of the total solvents formed. Additionally, acid formation decreased significantly with butyric acid as the dominant acid end product.     

Significance of an extracellular polymer for the energy metabolism in Clostridium acetobutylicum: A hypothesis

Summary An extracellular polymeric substance was produced by Clostridium acetobutylicum during the growth and acid production phase, and also when butanol was produced simultaneously from glucose and reassimilated butyric acid. When butanol and butyric acid were produced at the same time, reutilization of previously produced polymer occurred. These phenomena were revealed by investigating material balances during different phases of batch cultures. The same scheme of polymer production and uptake could also be identified in batch cultures published in the literature. Resting cells produced a polymer, likely a polysaccharide, with a significantly high degree of acetylation when butanol was formed from glucose and reassimilated butyric acid. It is suggested that the acetylated polymer is produced when the organism requires extensive amounts of reducing power and the conditions for production of non-reduced end products are not favourable. The polymer (of unknown composition) produced during the growth phase has no obvious relation to the energy metabolism, but it is suggested that previously produced polymer can be used as a reserve carbon source when sugar is needed at high rate. In batch culture, where the pH was controlled at 6.0 the simultaneous production of acids and butanol was also observed.     

Effect of temperature and pH onCandida blankii in chemostat culture

The growth characteristics ofCandida blankii as a function of temperature and pH in a simulated bagasse hemicellulose hydrolysate were determined in chemostat culture. The highest maximum specific growth rate of 0.44h^–1 was reached at 38°C and at pH 5.5, with a sharp decrease in growth rate on either side of this temperature. Growth occurred at 46°C but not at 48°C. The protein and cell yields varied little below 40°C and the respective values were 0.22 and 0.5 g/g at 38°C. At the lower pH values, a severe linear decrease in cell and protein yields occurred, whereas a small increase in these yields at decreasing pH values was found when acetic acid was omitted from the medium. In the presence of acetic acid, a very sharp decrease in the growth rate at pH values below pH 4.5 was noted, despite the very low residual acetic acid concentrations, of less than 50 mg/l, in the culture.     

Transformation ofo-xylene too-methyl benzoic acid by a denitrifying enrichment culture using toluene as the primary substrate

A highly enriched denitrifying mixed culture transformedo-xylene cometabolically along with toluene by methyl group oxidation.o-Methyl benzaldehyde ando-methyl benzoic acid accumulated transiently as metabolic products ofo-xylene transformation. Transformation ofo-methyl benzyl alcohol ando-methyl benzaldehyde occurred independently of toluene degradation and resulted in the formation of a compound coeluting witho-methyl benzoic acid on a gas chromatograph. The cometabolic relationship between toluene ando-xylene could be attributed to a mechanism linked to the initial oxidation of the methyl group.     

Detoxification of model phenolic compounds in lignocellulosic hydrolysates with peroxidase for butanol production from <Emphasis Type="Italic">Clostridium beijerinckii</Emphasis>

In the present study, we investigated the peroxidase-catalyzed detoxification of model phenolic compounds and evaluated the inhibitory effects of the detoxified solution on butanol production by Clostridium beijerinckii National Collection of Industrial and Marine Bacteria Ltd. 8052. The six phenolic compounds, p-coumaric acid, ferulic acid, 4-hydroxybenzoic acid, vanillic acid, syringaldehyde, and vanillin, were selected as model fermentation inhibitors generated during pretreatment and hydrolysis of lignocellulose. The enzyme reaction was optimized as a function of the reaction conditions of pH, peroxidase concentration, and hydrogen peroxide to substrate ratio. Most of the tested phenolics have a broad optimum pH range of 6.0 to 9. Removal efficiency increased with the molar ratio of H₂O₂ to each compound up to 0.5–1.25. In the case of p-coumaric acid, ferulic acid, vanillic acid, and vanillin, the removal efficiency was almost 100% with only 0.01 μM of enzyme. The tested phenolic compounds (1 g/L) inhibited cell growth by 64–74%, while completely inhibiting the production of butanol. Although syringaldehyde and vanillin were less toxic on cell growth, the level of inhibition on the butanol production was quite different. The detoxified solution remarkably improved cell growth and surprisingly increased butanol production to the level of the control. Hence, our present study, using peroxidase for the removal of model phenolic compounds, could be applied towards the detoxification of lignocellulosic hydrolysates for butanol fermentation.     

酒色着色菌利用产酸克雷伯氏菌发酵废液产氢

研究了酒色着色菌(Chromatium vinosum DSM185)利用产酸克雷伯氏菌（Klebsiella oxytoca HP1）发酵产氢废液进行光发酵和暗发酵产氢的可行性,以达到对产氢底物的充分利用和对产氢废液的进一步处理。研究结果表明C.vinosum可以利用K.oxytoca的发酵废液进行光发酵产氢和暗发酵产氢。C.vinosum发酵产氢后废液中残余还原糖和主要有机酸（丁酸）的含量明显降低,发酵产氢的最佳pH为6.5,添加0.1%(W/W)NH₄Cl能促进产氢。在光照条件下丁酸利用率可达54.38%,产氢量达36.97 mL/mg;在黑暗条件下丁酸利用率可达36.01%,产氢量达37.50mL/mg。     

Effect of carbon source and dissolved oxygen level on cell growth and pullulanase production byBacillus stearothermophilus G-82

Cell growth and extracellular pullulanase production ofBacillus stearothermophilus G-82 were investigated in batch culture using a defined medium with glucose, maltose, pullulan or amylopectin as carbon source. Maximum enzyme activity was with pullulan or amylopectin. Cell growth in batch culture was better under oxygen unlimited conditions, while higher total and specific enzyme activities, using pullulan or amylopectin, were obtained in oxygen-limited conditions. Enzyme accumulation took place in the late growth phase. The highest enzyme production of 300 U/I was reached when pullulan was used as carbon source in conditions of oxygen limitation.     

Hydrogen production conditions from food waste by dark fermentation with Clostridium beijerinckii KCTC 1785

The optimum conditions for biological hydrogen production from food waste by Clostridium beijerinckii KCTC 1875 were investigated. The optimum initial pH and fermentation temperature were 7.0 and 40°C, respectively. When the pH of fermentation was controlled to 5.5, a maximum amount of hydrogen could be obtained. Under these conditions, about 2,737 mL of hydrogen was produced from 50 g COD/L of food waste for 24 h, and the hydrogen content in the biogas was 38%. Hydrogen production rate and yield were about 108 mL/L·h and 128 mL/g COD_degraded, respectively. High concentrations of acetic (< 5,000 mg/L) or butyric acid (< 3,000 mg/L) significantly inhibited hydrogen production.