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.     

Enhanced butanol production by optimization of medium parameters using Clostridium acetobutylicum YM1

A new isolate of the solvent-producing Clostridium acetobutylicum YM1 was used to produce butanol in batch culture fermentation. The effects of glucose concentration, butyric acid addition and C/N ratio were studied conventionally (one-factor-at-a-time). Moreover, the interactions between glucose concentration, butyric acid addition and C/N ratio were further investigated to optimize butanol production using response surface methodology (RSM). A central composite design was applied, and a polynomial regression model with a quadratic term was used to analyze the experimental data using analysis of variance (ANOVA). ANOVA revealed that the model was highly significant (p < 0.0001) and the effects of the glucose and butyric acid concentrations on butanol production were significant. The model validation experiment showed 13.82 g/L butanol was produced under optimum conditions. Scale up fermentation in optimized medium resulted in 17 g/L of butanol and 21.71 g/L of ABE. The experimental data of scale up in 5 L bioreactor and flask scale were fitted to kinetic mathematical models published in the literature to estimate the kinetic parameters of the fermentation. The models used gave the best fit for butanol production, biomass and glucose consumption for both flask scale and bioreactor scale up.     

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。     

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.     

Butanol production from agricultural residues: Impact of degradation products on Clostridium beijerinckii growth and butanol fermentation

During pretreatment and hydrolysis of fiber-rich agricultural biomass, compounds such as salts, furfural, hydroxymethyl furfural (HMF), acetic, ferulic, glucuronic, rho-coumaric acids, and phenolic compounds are produced. Clostridium beijerinckii BA101 can utilize the individual sugars present in lignocellulosic [e.g., corn fiber, distillers dry grain solubles (DDGS), etc] hydrolysates such as cellobiose, glucose, mannose, arabinose, and xylose. In these studies we investigated the effect of some of the lignocellulosic hydrolysate inhibitors associated with C. beijerinckii BA101 growth and acetone-butanol-ethanol (ABE) production. When 0.3 g/L rho-coumaric and ferulic acids were introduced into the fermentation medium, growth and ABE production by C. beijerinckii BA101 decreased significantly. Furfural and HMF are not inhibitory to C. beijerinckii BA101; rather they have stimulatory effect on the growth of the microorganism and ABE production.     

Soy molasses as fermentation substrate for production of butanol using Clostridium beijerinckii BA101

Spray-dried soy molasses (SDSM) contains the sugars dextrose, sucrose, fructose, pinitol, raffinose, verbascose, melibiose, and stachyose. Of the 746 g kg⁻¹ total sugars in SDSM, 434 g kg⁻¹ is fermentable using Clostridium beijerinckii BA101. SDSM was used to produce acetone, butanol, and ethanol (ABE) by C. beijerinckii BA101 in batch cultures. Using 80 g l⁻¹ SDSM, 10.7 g l⁻¹ ABE was produced in P2 medium. Higher concentrations of SDSM resulted in poor solvent production due to the presence of excessive salt and inhibitory components. C. beijerinckii BA101 in SDSM at 80 g l⁻¹ concentration produced 22.8 g l⁻¹ ABE when supplemented with 25.3 g l⁻¹ glucose. SDSM contains 57.4 g kg⁻¹ mineral ash and 2% tri-calcium phosphate. Tri-calcium phosphate up to 43.1 g l⁻¹ was not inhibitory and at a tri-calcium phosphate concentration of 28.8 g l⁻¹, the culture produced more solvents (30.1 g l⁻¹) than the control experiment (23.8 g l⁻¹). In contrast, sodium chloride was a strong inhibitor of C. beijerinckii BA101 cell growth. At a concentration of 10 g l⁻¹ sodium chloride, a maximum cell concentration of 0.6 g l⁻¹ was achieved compared to 1.7 g l⁻¹ in the control experiment. The effects of two salts on specific growth rate constant (μ) and specific rate of ABE production (ν) for C. beijerinckii BA101 were examined. Journal of Industrial Microbiology & Biotechnology (2001) 26, 290–295. Received 20 September 2000/ Accepted in revised form 16 February 2001     

Butanol production by Clostridium beijerinckii. Part I: use of acid and enzyme hydrolyzed corn fiber

Fermentation of sulfuric acid treated corn fiber hydrolysate (SACFH) inhibited cell growth and butanol production (1.7 ± 0.2 g/L acetone butanol ethanol or ABE) by Clostridium beijerinckii BA101. Treatment of SACFH with XAD-4 resin removed some of the inhibitors resulting in the production of 9.3 ± 0.5 g/L ABE and a yield of 0.39 ± 0.015. Fermentation of enzyme treated corn fiber hydrolysate (ETCFH) did not reveal any cell inhibition and resulted in the production of 8.6 ± 1.0 g/L ABE and used 24.6 g/L total sugars. ABE production from fermentation of 25 g/L glucose and 25 g/L xylose was 9.9 ± 0.4 and 9.6 ± 0.4 g/L, respectively, suggesting that the culture was able to utilize xylose as efficiently as glucose. Production of only 9.3 ± 0.5 g/L ABE (compared with 17.7 g/L ABE from fermentation of 55 g/L glucose-control) from the XAD-4 treated SACFH suggested that some fermentation inhibitors may still be present following treatment. It is suggested that inhibitory components be completely removed from the SACFH prior to fermentation with C. beijerinckii BA101. In our fermentations, an ABE yield ranging from 0.35 to 0.39 was obtained, which is higher than reported by the other investigators.     

Effect of growth supplements and whey pretreatment on butyric acid production by Clostridium butyricum

Improved production of butyrate (up to 19 g/l) from whey by Clostridium butyricum was achieved by adding either yeast extract (5 g/l) or biotin (50 g/l). Hydrolysed lactose and proteolysed whey were less effective even with added biotin.The authors are with the Department of Biochemical Technology, Faculty of Chemical Technology, Slovak Technical University, Radlinského 9, Bratislava 812 37, Slovakia     

3-羟基丙酸分批发酵过程中的pH控制策略研究

本文利用重组大肠杆菌以甘油为底物发酵合成3．羟基丙酸,考察了不同pH对3．羟基丙酸产量及菌体生长的影响,发现在pH6．5条件下,细胞比生长速率达到最大值,延迟期也相对较短;而pH7．0有利于3-羟基丙酸的合成,控制pH7．0可以使3-羟基丙酸产量达到7．39g／L。基于不同pH条件下对细胞比生长速率和3-羟基丙酸比生成速率的分析,提出3．羟基丙酸分批发酵过程中的pH控制策略,即在发酵过程前5h将pH控制在6．5,5h～15h控制pH为7．0,此时有利于细胞生长;而后在15h-25h控制pH为7．5,25h后控制pH为7．0,从而使细胞具有较高的3．羟基丙酸比合成速率。在此控制策略下经过34h发酵3-羟基丙酸的终产量达到8．76g／L,比pH7．0条件下的3-羟基丙酸产量提高了18．54％。     

Enhancement of butanol production and reducing power using a two-stage controlled-pH strategy in batch culture of Clostridium acetobutylicum XY16

The effects of pH control on the process of acetone/butanol/ethanol (ABE) production in batch cultures of Clostridium acetobutylicum XY16 have been investigated. Based on the specific acid- and solvent-forming rates in batch fermentation at different pH values (from 4.3 to 6.0), a two-stage controlled-pH strategy was developed in which the pH was shifted from 5.5 to 4.9 after a dry cell weight of 0.5 g L(-1) was achieved. By applying this strategy, the maximum ABE concentration and productivity reached 20.3 g L(-1) and 0.63 g L(-1) h (-1), and were significantly improved by 12.2 and 40.1 %, respectively, compared with the process with no pH control. In addition, reducing power capability was significantly enhanced by this strategy. The two-stage controlled-pH strategy was a convenient and rapid method for high intensity ABE production.     

Optimization of indole acetic acid production by isolated bacteria from Stevia rebaudiana rhizosphere and its effects on plant growth

The ability to synthesize Indole-3-acetic acid (IAA) is widely associated with the plant growth promoting rhizobacteria (PGPR). The present work deals with isolation and characterization of such bacteria from the rhizosphere of medicinal plant Stevia rebaudiana and optimization of IAA production from its isolates. The optimization of IAA production was carried out at different pH and temperature with varied carbon and nitrogen sources of culture media. Out of different isolates obtained, three of them were screened as efficient PGPRs on the basis of different plant growth promoting attributes. Isolates CA1001 and CA2004 showed better production of IAA at pH 9 (91.7?µg?ml^?1) and at temperature 37?°C (81.7?µg?ml^?1). Dextrose (1%) was found to be the best carbon source for isolate CA1001 with 104?µg?ml^?1 IAA production. Isolate CA 2004 showed best production of IAA 36?µg?ml^?1 and 34?µg?ml^?1 at 1.5% and 1% Beef extract as nitrogen source respectively. Isolate CA 1001 showed 32?µg?ml^?1 IAA production at 0.5% nicotinic acid concentration. From the current study, CA1001 and CA2004 emerged as noble alternatives for IAA production further which also resulted in root and shoot biomass generation in crop plants, hence can be further used as bio-inoculants for plant growth promotion.     

Influence of dissolved oxygen concentration on intracellular pH for regulation of Aspergillus niger growth rate during citric acid fermentation in a stirred tank bioreactor

In this paper we report the regulation of Aspergillus niger growth rate during citric acid fermentation in a stirred tank bioreactor. For this, the influence of dissolved oxygen concentration in a medium on intracellular pH values and consequently on overall microbial metabolism was emphasized. Intracellular pH of mycelium grown under different concentrations of dissolved oxygen in the medium was determined. Sensitivity of proteins toward proton concentration is well recognized, therefore pH influences on the activities of key regulatory enzymes of Aspergillus niger were determined at pH values similar to those detected in the cells grown under lower dissolved oxygen concentrations. The results have shown significantly reduced specific activities of hexokinase, 6-phosphofructokinase and glucose-6-phosphate dehydrogenase in more acidic environment, while pyruvate kinase was found to be relatively insensitive towards higher proton concentration. As expected, due to the reduced specific activities of regulatory enzymes under more acidic conditions, overall metabolism should be hindered in the medium with lower dissolved oxygen concentration which was confirmed by detecting the reduced specific growth rates. From the studies, we conclude that dissolved oxygen concentration affects the intracellular pH and thus growth rate of Aspergillus niger during the fermentation process.     

Influence of calcium on fungal growth and citric acid production during fermentation of a sugarcane molasses-based medium by a strain of Aspergillus niger

The effect of CaCl₂ on the growth, morphology and citric acid production from sugarcane molasses by Aspergillus niger 419 was studied. The addition of 0.5g CaCl₂/l to the fermentation medium induced a loose pelleted form of growth, reduced the biomass concentration and increased the volumetric productivity (g citric acid/h) and the specific production (g citric acid/g biomass dw) from 0.02 and 0.37 to 0.13 and 3.72, respectively.     

The influence of pH on Staphylococcus saprophyticus iron metabolism and the production of siderophores

Staphylococcus saprophyticus is a gram-positive coagulase negative bacteria which shows clinical importance due to its capability of causing urinary tract infections (UTI), as well as its ability to persist in this environment. Little is known about how S. saprophyticus adapts to the pH shift that occurs during infection. Thus, in this study we aim to use a proteomic approach to analyze the metabolic adaptations which occur as a response by S. saprophyticus when exposed to acid (5.5) and alkaline (9.0) pH environments. Proteins related to iron storage are overexpressed in acid pH, whilst iron acquisition proteins are overexpressed in alkaline pH. It likely occurs because iron is soluble at acid pH and insoluble at alkaline pH. To evaluate if S. saprophyticus synthesizes siderophores, CAS assays were performed, and the results confirmed their production. The chemical characterization of siderophores demonstrates that S. saprophyticus produces carboxylates derived from citrate. Of special note is the fact that citrate synthase (CS) is down-regulated during incubation at acid pH, corroborating this result. This data was also confirmed by enzymatic assay. Our results demonstrate that iron metabolism regulation is influenced by different pH levels, and show, for the first time, the production of siderophores by S. saprophyticus. Enzymatic assays suggest that citrate from the tricarboxylic acid cycle (TCA) is used as substrate for siderophore production.     

Comparison of polysialic acid production in Escherichia coli K1 during batch cultivation and fed-batch cultivation applying two different control strategies

The polysialic acid (PSA) production in Escherichia coli (E. coli) K1 was studied using three different cultivation strategies. A batch cultivation, a fed-batch cultivation at a constant specific growth rate of 0.25 h⁻¹ and a fed-batch cultivation at a constant glucose concentration of 50 mg l⁻¹ was performed. PSA formation kinetics under different cultivation strategies were analyzed based on the Monod growth model and the Luedeking-Piret equation. The results revealed that PSA formation in E. coli K1 was completely growth associated, the highest specific PSA formation rate (0.0489 g g⁻¹ h⁻¹) was obtained in the batch cultivation. However, comparing biomass and PSA yields on the glucose consumed, both fed-batch cultivations provided higher yields than that of the batch cultivation and acetate formation was prevented. Moreover, PSA yield on glucose was also correlated to the specific growth rate of the cells. The optimal specific growth rate for PSA production was 0.32 h⁻¹ obtained in the fed-batch cultivation at a constant glucose concentration of 50 mg l⁻¹, with highest conversion efficiency of 43 mg g⁻¹.     

Discovery of 2-(1H-imidazo-2-yl)piperazines as a new class of potent and non-cytotoxic inhibitors of Trypanosoma brucei growth in vitro

The identification of a new series of growth inhibitors of Trypanosoma brucei rhodesiense, causative agent of Human African Trypanosomiasis (HAT), is described. A selection of compounds from our in-house compound collection was screened in vitro against the parasite leading to the identification of compounds with nanomolar inhibition of T. brucei growth. Preliminary SAR on the hit compound led to the identification of compound 34 that shows low nanomolar parasite growth inhibition (T. brucei EC₅₀ 5?nM), is not cytotoxic (HeLa CC₅₀?>?25,000?nM) and is selective over other parasites, such as Trypanosoma cruzi and Plasmodium falciparum (T. cruzi EC₅₀ 8120?nM, P. falciparum EC₅₀ 3624?nM).     

一株耐受低pH、高浓度硒菌株的筛选鉴定及两阶段pH调控高效除硒的研究

通过酸性含硒平板和摇瓶筛选出一株对低pH、高浓度硒有很好耐受性的菌株Y1,通过菌落形态特征分析和26S rDNA测序,鉴定该菌株为Pichia kudriavzevii,多抗性实验结果显示该菌是一株多重耐受性毕赤酵母。通过摇瓶实验研究了温度、接种量、摇床转速、pH对菌株除硒性能的影响,结果显示当温度为25℃,接种量为12%(v/v),摇床转速为250 r/min,pH为3.0时,菌株对硒的去除率最高为58.3%。基于不同pH发酵过程中菌体生物量及富硒量的不同表现:pH 3.0时生物量最高,pH 5.0时富硒量最高,提出两阶段pH调控策略:发酵0 h~14 h将pH控制在3.0,14 h~28 h将pH控制在5.0,最终除硒率可达78.6%,分别比pH恒定在3.0及5.0条件下提高了15.4%和21.7%。     

Treatability of cheese whey for single-cell protein production in nonsterile systems: Part I. Optimal condition for lactic acid fermentation using a microaerobic sequencing batch reactor (microaerobic SBR) with immobilized Lactobacillus plantarum TISTR 2265 and microbial communities

Cheese whey contains a high organic content and causes serious problems if it is released into the environment when untreated. This study aimed to investigate the optimum condition of lactic acid production using the microaerobic sequencing batch reactor (microaerobic SBR) in a nonsterile system. The high production of lactic acid was achieved by immobilized Lactobacillus plantarum TISTR 2265 to generate an acidic pH condition below 4.5 and then to support single-cell protein (SCP) production in the second aerobic sequencing batch reactor (aerobic SBR). A hydraulic retention time (HRT) of 4 days and a whey concentration of 80% feeding gave a high lactic acid yield of 12.58 g/L, chemical oxygen demand (COD) removal of 62.38%, and lactose utilization of 61.54%. The microbial communities in the nonsterile system were dominated by members of lactic acid bacteria, and it was shown that the inoculum remained in the system up to 330 days.     

Inhibitory effects in vitro of S-[2-carboxy-1-(1H-imidazol-4-yl)ethyl]-glutathione,a proposed metabolite of l-histidine,on γ-glutamyltransferase activity

A transfer of the γ-glutamyl moiety of S-[2-carboxy-1-(1H-imidazol-4-yl)ethyl]glutathione (I), an adduct of glutathione and l-histidine metabolite urocanic acid, has been investigated by using γ-glutamyltransferase preparation from bovine kidney. When an equimolar mixture of two diastereomers of compound I in a phosphate buffer was allowed to react with glycylglycine in the presence of the transferase, two diastereomers of N-{S-[2-carboxy-1-(1H-imidazol-4-yl)ethyl]-l-cysteinyl}glycine (II) were formed in the same yield with each other and this was accompanied by a formation of γ-glutamylglycylglycine. Kinetics of compound I with the transferase indicated high affinity between the two materials, while the maximal reaction velocity of the γ-glutamyl transfer was low. Effects of compound I in vitro on the transfer of γ-glutamyl moiety of γ-glutamyl-p-nitroanilide to glycylglycine with the transferase were also studied, and the results indicated that the transfer was suppressed by compound I based on its competitive and non-competitive inhibitions. These results suggest that little variation in reactivities of two diastereomers of compound I as the substrate is given by the difference in stereomerism of their asymmetric carbon atoms and that inhibitory effects of compound I on the catalytic action of the transferase is of sufficient physiological importance to decrease the degradation of natural γ-glutamyl compounds, such as glutathione and its analogs.