Biotechnological production of l(+)-lactic acid from wood hydrolyzate by batch fermentation of Enterococcus faecalis

The inhibition of lactic acid fermentation by wood hydrolyzate was decreased (approx. 20%) by adaptation of Enterococcus faecalis RKY1 to wood hydrolyzate-based medium whereby lactic acid productivity and cell growth were enhanced by 0.5 g l(-1) h(-1) and 2.1 g l(-1), respectively. When the diluted or concentrated wood hydrolyzate (equivalent to 25-100 g glucose l(-1)) was supplemented with 15 g yeast extract l(-1), 24-93 g lactic acid l(-1) was produced at a rate between 1.7 g l(-1) h(-1) and 3.2 g l(-1) h(-1).     

Anaerobic fermentative production of lactic acid using cheese whey and corn steep liquor

Cheese whey was the most suitable substrate for production of lactic acid under anaerobic conditions by Entercoccus flavescens which, on supplementating with corn steep liquor (5% v/v) and 10 mM CaCO₃ at pH 5.5, 37°C, yielded 12.6 g lactic acid/l in 36 h. Production was scaled up to a 10 l bioreactor under controlled pH and continuous CO₂ supply and gave 28 g lactic acid/l in 30 h resulting in a net 8.7-fold increase in production as compared to unoptimized conditions.     

Improvement of glycerol production by Candida krusei in batch and continuous cultures using corn steep liquor

No fermentation parameter was affected at phosphate concentration above 0.4 g l^–1 when KH₂PO₄ was used as phosphate source and the glucose consumption rate was difficult to control when corn steep liquor (CSL) was adopted as the phosphate source. However, if CSL was supplemented as a source of growth factors instead of as the phosphate source, not only glucose uptake and glycerol was improved, but also fermentation became easy to control and a steady state of continuous culture was easily obtained.     

Fermentative production of succinic acid from glucose and corn steep liquor byAnaerobiospirillum succiniciproducens

Anaerobiospirillum succiniciproducens requires expensive complex nitrogen sources such as yeast extract and polypeptone for its growth and succinic acid production. It was found thatA. succiniciproducens was able to grow in a minimal medium containing glucose when supplemented with corn steep liquor (CSL) as the sole complex nitrogen source. The concentration of CSL had a significant effect on the glucose consumption byA. succiniciproducens. When 10–15 g/L of CSL was supplemented, cells were grown to an OD₆₆₀ of 3.5 and produced 17.8 g/L succinic acid with 20 g/L glucose. These results are similar to those obtained by supplementing yeast extract and polypeptone, thereby suggesting that succinic acid can be produced more economically using glucose and CSL.     

采用玉米秸秆水解糖和玉米浆发酵生产丁二酸

研究了以玉米秸秆水解糖为碳源,不同氮源条件下琥珀酸放线杆菌Actinobacillus succinogenesSF-9的丁二酸发酵产酸能力。结果表明玉米浆可以替代酵母膏作为丁二酸发酵的廉价氮源。厌氧摇瓶丁二酸发酵单因素试验,得到在初糖浓度50 g/L时,玉米浆的较佳用量为20 g/L。在5 L搅拌罐上,考察了不同初始玉米秸秆水解糖浓度对A.succinogenes SF-9发酵生产丁二酸的影响,结果显示高初始秸秆糖浓度对琥珀酸放线杆菌的生长有抑制作用。采用补料分批发酵,发酵60 h丁二酸的产量达到42.7g/L,丁二酸产率82.7%,生产强度0.81 g/(L·h)。丁二酸的产量和生产强度较分批发酵有明显提高。     

Batch and continuous cultures of<Emphasis Type="Italic"> Mannheimia succiniciproducens</Emphasis> MBEL55E for the production of succinic acid from whey and corn steep liquor

Mannheimia succiniciproducens MBEL55E isolated from bovine rumen is able to produce a large amount of succinic acid in a medium containing glucose, peptone, and yeast extract. In order to reduce the cost of the medium, whey and corn steep liquor (CSL) were used as substrates for the production of succinic acid by M. succiniciproducens MBEL55E. Anaerobic batch cultures of M. succiniciproducens MBEL55E in a whey-based medium containing CSL resulted in the production of succinic acid with a yield of 71% and productivity of 1.18 g/l/h, which are similar to those obtained in a whey-based medium containing yeast extract (72% and 1.21 g/l/h). Anaerobic continuous culture of M. succiniciproducens MBEL55E in a whey-based medium containing CSL resulted in a succinic acid yield of 69% and a succinic acid productivity as high as 3.90 g/l/h. These results show that succinic acid can be produced efficiently and economically by M. succiniciproducens MBEL55E from whey and CSL.     

Acetate production byClostridium thermoaceticum in corn steep liquor media

A low-cost nutrient medium based on corn steep liquor (CSL) was developed for the production of acetates byClostridium thermoaceticum. Pre-treatment of CSL with dolime and vitamin supplementation increased the rate of acetate production. Adding excess nutrients in a fed-batch mode minimized by-product formation and increased final acetate concentration from 19 g L^–1 to 40 g L^–1 acetic acid. High yields of acetic acid (0.95 g g^–1 glucose in fed-batch mode) was probably due to the conversion of the lactic acid in CSL into acetic acid by the organism.     

Effects of corn steep liquor on production of 2,3-butanediol and acetoin by Bacillus subtilis

The initial concentration of corn steep liquor (CSL) have remarkable effects on not only 2,3-butanediol (2,3-BD) and acetoin (metabolic precursor) production, but also on the ratio of 2,3-BD to acetoin. When a high concentration of CSL was supplemented, cell growth was improved, acetoin reductase (ACR) was stimulated, the concentration of 2,3-BD increased by 78.6%, acetoin decreased by 61.9%, and the ratio of 2,3-BD to acetoin increased by 3.69-fold. The acr gene, encoding ACR, was over-expressed in Bacillus subtilis. Compared to the control (parent strain), low levels of CSL in the engineered strain increased 2,3-BD concentration and the ratio 2,3-BD to acetoin by 13.9% and 39.5%, respectively, and decreased acetoin titer by 18.3%. Acetoin became a major product under low levels of CSL. Also, a knockout strain carrying an acr::cat insertion mutation was constructed. As expected, the loss of ACR activity led to an accumulation of acetoin in the supernatants of acr:: cat mutant cultures. Additionally, the productivity of acetoin was improved by high concentration of CSL. The results above demonstrate the feasibility of using B. subtilis for the production of not only 2,3-BD but also acetoin as a major product.     

Ethanol production from syngas by Clostridium strain P11 using corn steep liquor as a nutrient replacement to yeast extract

The feasibility of replacing yeast extract (YE) by corn steep liquor (CSL), a low cost nutrient source, for syngas fermentation to produce ethanol using Clostridium strain P11 was investigated. About 32% more ethanol (1.7 g L⁻¹) was produced with 20 g L⁻¹ CSL media in 250-mL bottle fermentations compared to media with 1 g L⁻¹ YE after 360 h. Maximum ethanol concentrations after 360 h of fermentation in a 7.5-L fermentor with 10 and 20 g L⁻¹ CSL media were 8.6 and 9.6 g L⁻¹, respectively, which represent 57% and 60% of the theoretical ethanol yields from CO. Only about 6.1 g L⁻¹ of ethanol was obtained in the medium with 1 g L⁻¹ YE after 360 h, which represents 53% of the theoretical ethanol yield from CO. The use of CSL also enhanced butanol production by sevenfold compared to YE in bottle fermentations. These results demonstrate that CSL can replace YE as the primary medium component and significantly enhance ethanol production by Clostridium strain P11.     

A cost effective fermentative production of succinic acid from cane molasses and corn steep liquor by Escherichia coli

AIM: Development and optimization of an efficient and inexpensive medium for succinic acid production by Escherichia coli under anaerobic conditions. METHODS AND RESULTS: Initially, 0.8 gl(-1) of succinic acid was produced in 60 h in 300-ml medium. On optimization, glucose and peptone were replaced by cane molasses and corn steep liquor. Three hundred ml of this medium was inoculated with 4% (v/v) of seed inoculum, incubated at 39 degrees C for 72 h, resulted in 7.1 gl(-1) of succinic acid in 36 h. Scale up in a 10-l fermentor under conditions of controlled pH and continuous CO2 supply in this medium resulted in 17 gl(-1) of succinic acid in 30 h. CONCLUSIONS: A ninefold increase in succinic acid production was obtained in 500-ml anaerobic bottles with optimized medium having cane molasses and corn steep liquor as against initial medium containing glucose and peptone. However, a subsequent scale up in a 10-l fermentor resulted in a 2.5-fold increase in succinic acid production as against optimized medium used in 500-ml anaerobic bottles. SIGNIFICANCE AND IMPACT OF THE STUDY: Succinic acid production was enhanced in medium consisting of inexpensive carbon and nitrogen sources in a shorter span of time.     

Production of PHB by a Bacillus megaterium strain using sugarcane molasses and corn steep liquor as sole carbon and nitrogen sources

Poly(hydroxybutyric acid) (PHB) and other biodegradable polyesters are promising candidates for the development of environment-friendly, totally biodegradable plastics. The use of cane molasses and corn steep liquor, two of the cheapest substrates available in Egypt, may help to reduce the cost of producing such biopolyesters. In this work, the effect of different carbon sources was studied. Maximum production of PHB was obtained with cane molasses and glucose as sole carbon sources (40.8, 39.9 per mg cell dry matter, respectively). The best growth was obtained with 3% molasses, while maximum yield of PHB (46.2% per mg cell dry matter) was obtained with 2% molasses. Corn steep liquor was the best nitrogen source for PHB synthesis (32.7 mg per cell dry matter), on the other hand, best growth was observed when ammonium chloride, ammonium sulphate, ammonium oxalate or ammonium phosphate were used as nitrogen sources.     

Mathematical modeling of citric acid production by repeated batch culture

A mathematical model has been created for the process of citric acid biosynthesis by yeast (mutant strain Yarrowia lipolytica) cultivated by the repeated batch (RB) method on ethanol under conditions of nitrogen limitation. The model accounts for cell growth as a function of nitrogen concentration in the culture liquid; nitrogen uptake by growing cells; citric acid production; pH control in the fermentor by means of NaOH addition; and changes in system volume. The model represents a system of five nonlinear differential equations. Experimental measurements of cell concentration, citric acid concentration, and cultivation broth volume were used with the least squares method to determine the values of eight model parameters. The parameter values obtained were consistent with literature data and general concepts of cell growth and citric acid biosynthesis. The model has been used to predict optimum RB culture conditions.     

Studies on the production of extracellular protease by Alcaligenes faecalis

Alcaligenes faecalis produced extracellular protease when incubated in media containing protein substrates. Enzyme production was found to be influenced by various culture conditions. Enzyme production was growth-associated, expressed linearity with growth and reached a maximum at the end of the growth phase. Carbohydrates and inorganic nitrogen sources could not be utilized by the bacterium for its growth, and organic nitrogen appeared to be a primary determinant in protease production. Enzyme production reached its maximum level of 171.2 U/ml when the culture was incubated at 30 °C at pH 8.0. Ca²⁺ and Mg²⁺ enhanced the enzyme production. The crude enzyme powder was stable at high alkaline pH and stable upto 6 months at the storage temperature of 0–4 °C. This revised version was published online in July 2006 with corrections to the Cover Date.     

Sex pheromone plasmid pAD1-encoded surface exclusion protein of Enterococcus faecalis.

Summary During conjugative transfer of sex pheromone plasmids ofEnterococcus faecalis a so-called surface exclusion protein reduces the frequency with which these plasmids are transferred to cells already possessing the same plasmid. We report here the DNA sequence of a 3 .8 kb fragment of the sex pheromone plasmid pAD1 containing the structural genesea1 for surface exclusion protein and a small open reading frame (ORF) upstream ofsea1. Surface exclusion protein Seal was found to be highly homologous to the surface exclusion protein Sec10 encoded by the sex pheromone plasmid pCF10. Hybridization studies with DNA probes derived from the structural gene seal demonstrated that, with the exception of pAM373, all known sex pheromone plasmids carry a homologous gene. These studies also indicated that the genetic organization is similar in these plasmids, with the structural gene for surface exclusion protein being located 5 to that for aggregation substance.     

Enterococcus faecalis cytolysin and lactocin S of Lactobacillus sake

Strains of Enterococcus faecalis and Lactobacillus sake have been found to express lantibiotics with unusual properties. The enterococcal lantibiotic is unusual in that it consists of two dissimilar subunits, both putatively containing modifications consistent with those found in other lantibiotics. The enterococal lantibiotic is also unusual in the number of proteolytic steps involved in secretion signal removal and activation. Moreover, it has been observed to contribute to enterococcal disease in humans and in animal models. Structrural studies of lactocin S, expressed by a strain of L. sake highlight unique properties including the presence of D-alanine within its structure, and a protease putatively responsible for lactocin S secretion signal peptide removal which, itself, lacks a signal or propeptide sequence. Despite the unusual properties of each of these lantibiotics, the operons encoding each, and accompanying auxiliary functions, are collinear suggeting a common ancestry. The accretion of interdigitating DNA sequences between genes encoded within the lactocin S determinant are unique to that determinant, however, and are of unknown function.     

Identification of aggregation substances of Enterococcus faecalis cells after induction by sex pheromones

The sex pheromone system of Enterococcus faecalis is responsible for the clumping response of a plasmid carrying donor strain with a corresponding plasmid free recipient strain due to the production of sex pheromones by the recipient strain. The clumping response is mediated by a surface material (called aggregation substance) which is synthesized upon addition of sex pheromones to the cultures. Here we show that after induction a dense layer of hairlike structures is formed on the cell wall of the bacteria. These hairlike structures are responsible for the cell-cell contact which leads to the aggregation of cells. Formation of these structures was specific, only occurring after the addition of homologous sex pheromone.Abbreviations cAD1 sex pheromone specific for plasmid pAD1 - cPD1 sex pheromone specific for plasmid pPD1 - CW cell wall - pAD1 conjugative plasmid specifically transferred in the presence of cAD1 - pPD1 conjugative plasmid specifically transferred in the presence of cPD1 - PBS 10 mM Na-phosphate pH 7.5, 0.85% NaCl     

Experimental design to enhance the production of l-(+)-lactic acid from steam-exploded wood hydrolysate using Rhizopus oryzae in a mixed-acid fermentation

The fermentation of hemicellulosic hydrolysate from Pinus taeda chips, using the fungal culture Rhizopus oryzae, was carried out to produce l-(+)-lactic acid and to optimize and enhance the biological conversion of reducing sugar into l-(+)-lactic acid using the experimental design to evaluate the culture conditions. The first factorial design based on surface response with five factors (agitation level, substrate concentration, CaCO₃ concentration, C/N and C/P ratios) at low levels and one medium point was performed to optimize culture conditions. The second study tested two factors (substrate concentration and C/N ratio) at three levels. The statistical analysis of the data obtained from the factorial study showed that a C/N ratio of 35 and substrate concentration of 90 g/litre were the best conditions to produce l-(+)-lactic acid with R. oryzae on P. taeda hydrolysate, but in this case the statistical projection was not correct and the real optimized conditions were C/N ratio of 55 and substrate concentration of 75 g/litre of reducing sugar.     

Localization of aggregation substances of Enterococcus faecalis after induction by sex pheromones

The distribution of sex pheromone induced aggregation substance was studied on the cell surface of various Enterococcus faecalis strains. In the accompanying paper we have shown that the aggregation substance appears as a layer of hairlike structures. Using direct and indirect immunogold technique, transmission electron microscopy and high resolution scanning electron microscopy we investigated the appearance and distribution of the aggregation substance. The hairs increase in number with increasing exposure to sex pheromones (maximum density: 1300/m²). We show that these structures are unequally distributed over the cell surface, even if the cells were induced by sex pheromones for a long period of time. Statistical analysis of the unequal distribution indicates that aggregation substance is incorporated into pre-existing old cell-walls and that this incorporation shows a saturation ca. 40 min after addition of sex pheromones.Abbreviations cAD1 sex pheromone specific for plasmid pAD1 - cPD1 sex pheromone specific for plasmid pPD1 - FESEM field emission scanning electron microscope - pAD1 conjugative plasmid specifically transferred in the presence of cAD1 - pPD1 conjugative plasmid specifically transferred in the presence of cPD1 - TEM transmission electron microscope     

Molecular cloning, overexpression, purification, and characterization of an aerobic FMN-dependent azoreductase from Enterococcus faecalis

Azo dyes represent a major class of synthetic colorants that are ubiquitous in foods and consumer products. Enterococcus faecalis is a predominant member of the human gastrointestinal microflora. Strain ATCC 19433 grew in the presence of azo dyes and metabolized them to colorless products. A gene encoding a putative FMN-dependent aerobic azoreductase that shares 34% identity with azoreductase (AcpD) of Escherichia coli has been identified in this strain. The gene in E. faecalis, designated as azoA, encoded a protein of 208 amino acids with a calculated isoelectric point of 4.8. AzoA was heterologously overexpressed in E. coli with a strong band of 23 kDa on SDS-PAGE. The purified recombinant enzyme was a homodimer with a molecular weight of 43 kDa, probably containing one molecule of FMN per dimer. AzoA required FMN and NADH, but not NADPH, as a preferred electron donor for its activity. The apparent Km values for both NADH and 2-[4-(dimethylamino)phenylazo]benzoic acid (Methyl red) substrates were 0.14 and 0.024 mM, respectively. The apparent Vmax was 86.2 microM/min/mg protein. The enzyme was not only able to decolorize Methyl red, but was also able to convert sulfonated azo dyes Orange II, Amaranth, Ponceau BS, and Ponceau S. AzoA is the first aerobic azoreductase to be identified and characterized from human intestinal gram-positive bacteria.     

Optimization of polyhydroxybutyrate production by <Emphasis Type="Italic">Bacillus</Emphasis> sp. CFR 256 with corn steep liquor as a nitrogen source

Polyhydroxyalkanotes (PHAs), the eco-friendly biopolymers produced by many bacteria, are gaining importance in curtailing the environmental pollution by replacing the non-biodegradable plastics derived from petroleum. The present study was carried out to economize the polyhydroxybutyrate (PHB) production by optimizing the fermentation medium using corn steep liquor (CSL), a by-product of starch processing industry, as a cheap nitrogen source, by Bacillus sp. CFR 256. Response surface methodology (RSM) was used to optimize the fermentation medium using the variables such as corn steep liquor (5–25 g l⁻¹), Na₂HPO₄ 2H₂O (2.2–6.2 g l⁻¹), KH₂PO₄ (0.5–2.5 g l⁻¹), sucrose (5–55 g l⁻¹) and inoculum concentration (1–25 ml l⁻¹). Central composite rotatable design (CCRD) experiments were carried out to study the complex interactions of the variables. The optimum conditions for maximum PHB production were (g l⁻¹): CSL-25, Na₂HPO₄ 2H₂O-2.2, KH₂PO₄ − 0.5, sucrose − 55 and inoculum − 10 (ml l⁻¹). After 72 h of fermentation, the amount of PHA produced was 8.20 g l⁻¹ (51.20% of dry cell biomass). It is the first report on optimization of fermentation medium using CSL as a nitrogen source, for PHB production by Bacillus sp.