L-Lysine production by auxotrophic mutants of Arthrobacter globiformis

By mutagenesis with N-methyl N-nitro-N-nitrosoguanidine, in two steps, a number of methionine plus threonine double auxotrophs have been isolated from a glutamate producing Arthrobacter globiformis, excreting L-lysine in good amounts. For the three potent mutants tested the medium of WHITE was adjudged to be the best. Biotin, ammonium chloride and glucose was found to be optimum at 5 μg l^?1, 40 mM and 4% level, respectively. With such optimal C and N source, the strain MT 35 yielded 28.0 g lysine l^?1 of medium in flask culture.     

Tannase production by Bacillus licheniformis

Bacillus licheniformis KBR 6 produced maximum extracellular tannase activity at 0.21 U ml^–1 with 1.5% (w/v) tannic acid either in the absence or presence of glucose (1 g l^–1) after 18–21 h growth though the organism did not attain maximum growth until 36 h.     

Isolation of Bacillus licheniformis mutants for stable production profiles of alkaline protease

Summary A phenotypic requirement for cysteine was introduced inBacillus licheniformis producing alkaline protease to facilitate its isolation from poor or nonproducerBacillus species. This facilitated purification of the strain in cases of cross-contamination, preparation of good inocula for commercial production and stabilization of alkaline protease harvest values, alleviating economic losses incurred through cross-contamination.     

Bacteriocin-like substance production by Bacillus licheniformis strain P40

AIMS: To investigate the production of bacteriocin-like compounds by Bacillus spp. isolated from the Amazon basin. METHODS AND RESULTS: An antimicrobial substance produced by Bacillus licheniformis strain P40 was inhibitory to a broad range of indicator strains, such as Listeria monocytogenes, Bacillus cereus and clinical isolates of Streptococcus spp. The compound was stable at 100 degrees C, but lost its activity when treated at 121 degrees C/103.5 kPa for 15 min. It was resistant to the proteolytic action of trypsin and papain but sensitive to pronase E and was stable within a wide range of pH (3-11). The substance was bactericidal and bacteriolytic to L. monocytogenes. CONCLUSIONS: An antibacterial peptide produced by Bacillus licheniformis was characterized, presenting a broad spectrum of activity against pathogenic and spoilage organisms. SIGNIFICANCE AND IMPACT OF THE STUDY: The identification of a substance active against important pathogens addresses an important aspect of food safety.     

Improvement of acetoin reductase activity enhances bacitracin production by Bacillus licheniformis

Bacitracin fermentation by Bacillus licheniformis in this work showed three characteristics: (1) the extracellular propionate, butyrate, acetoin and 2,3-butanediol accumulates under conditions of low dissolved oxygen (zero after 4 h cultivation), reaching a total content of approximately 11.1 g/L; (2) cell growth occurs quickly subsequent to cell autolysis and the second growth; and (3) there is a low content of 2,3-butanediol, a reduced product of acetoin catalyzed by acetoin reductase, in the culture process. In this study, addition of MnCl₂ (0.3 mg/L) to the production medium increased the acetoin reductase activity, redirected the NADH oxidation partly from the propionate- and butyrate-production pathways to the 2,3-butanediol synthesis pathway, reduced the intracellular NADH/NAD⁺ ratio, and facilitated cell growth, ultimately achieving a 11.6% increase in bacitracin production (1076 U/mL) versus the control. The results provide useful information regarding large-scale bacitracin production by B. licheniformis.     

Mechanism of uridine production by Bacillus subtilis mutants

Summary Pyrimidine analogue-resistant mutants of Bacillus subtilis were found to produce a large amount of uridine. One of them accumulated 55 mg/ml of uridine in culture medium. The changes in enzymes involved in the metabolism of uridine 5-monophosphate (UMP) were examined with this mutant. All six enzymes of de novo UMP biosynthesis were completely free from regulation by uridine compounds, and the activities of these enzymes were 16- to 30-fold higher than those of the enzymes of the parental strain. In the mutant strain, the level of uridine phosphorylase, responsible for converting uridine to uracil, was extremely low, compared with that of the parental strain. No apparent change was observed between the strains in the activity of UMP dephosphorylation or uracil phosphoribosyltransferase. The implication of these findings is discussed in relation to the overproduction of uridine by the mutant.Microbial production of uridine. Part III     

Levan-type FOS production using a Bacillus licheniformis endolevanase

In the present work we describe an enzymatic production method to obtain β2-6 fructose oligosaccharides (levan-type FOS) through a sequential reaction in which a bacterial endolevanase is applied to levan produced from sucrose by bacterial levansucrases. A putative gene encoding an endolevanase, designated as LevBl, was identified through a bioinformatics search, isolated from a strain of Bacillus licheniformis IBt1 from our own collection and expressed in Escherichia coli. LevB1 showed a specific activity of 1.8 U/mg protein at 35 °C in 50 mM phosphate buffer pH 6.0. A first order kinetic behavior was found when up to 150 g/L of low molecular weight levan (8.3 kDa) was used as the substrate. The product profile was determined by HPAEC-PAD and consisted of levan-type FOS with a polymerization degree between 2 and 8, with levanbiose as the major product after long reaction times. Yields of 97% of levan-type FOS were obtained when 1.0 U/mL of LevB1 reacted with 100 g/L of levan produced by the levansucrase from Bacillus subtilis. Finally, it was observed that levan-type FOS are efficiently fermented by probiotic lactic acid bacteria.     

Heat-stable toxin production by strains of Bacillus cereus, Bacillus firmus, Bacillus megaterium, Bacillus simplex and Bacillus licheniformis

Strains of Bacillus cereus can produce a heat-stable toxin (cereulide). In this study, 101 Bacillus strains representing 7 Bacillus species were tested for production of heat-stable toxins. Strains of B. megaterium, B. firmus and B. simplex were found to produce novel heat-stable toxins, which showed varying levels of toxicity. B. cereus strains (18 out of 54) were positive for toxin production. Thirteen were of serovar H1, and it was of interest that some were of clinical origin. Two were of serovars 17B and 20, which are not usually implicated in the emetic syndrome. Partial purification of the novel B. megaterium, B. simplex and B. firmus toxins showed they had similar physical characteristics to the B. cereus emetic toxin, cereulide.     

Effect of oilseed cakes on alpha-amylase production by Bacillus licheniformis CUMC305

The effects of oilseed cakes on extracellular thermostable alpha-amylase production by Bacillus licheniformis CUMC305 was investigated. Each oilseed cake was made of groundnut, mustard, sesame, linseed, coconut copra, madhuca, or cotton. alpha-Amylase production was considerably improved in all instances and varied with the oilseed cake concentration in basal medium containing peptone and beef extract. Maximum increases were effected by a low concentration (0.5 to 1.0%) of groundnut or coconut, a high concentration (3%) of linseed or mustard, and an Rintermediate concentration (2%) of cotton, madhuca, or sesame. The oilseed cakes made of groundnut or mustard could completely replace the conventional peptone-beef extract medium as the fermentation base for the production of alpha-amylase by B. licheniformis. The addition of corn steep liquor to cotton, linseed, sesame, or madhuca cake in the medium improved alpha-amylase production.     

The production of polyhydroxyalkanoate by Bacillus licheniformis using sequential mutagenesis and optimization

The purpose of this study was to enhance the production of polyhydroxyalkanoate (PHA) by sequential mutation of Bacillus licheniformis PHAs-007, using UV and N-methyl-N′-nitro-N-nitrosoguanidine (NTG). In addition, the effect of nutrient additions and environmental conditions were optimized to increase the production of PHA. Bacillus licheniformis PHAs-007 produced high amounts of PHA (64.09 ～ 68.80% of DCW) under both synthetic and renewable substrates. After mutagenesis treatment, mutant M2-12 was selected from 380 strains, based on its high biomass and PHA concentration. The mutant M2-12 gave the highest value of specific growth rate (0.09/h), biomass (22.24 g/L) and PHA content (19.55 g/L) under optimal conditions, consisting of 3% palm oil mill effluent, with no additional trace elements, at 45oC and pH 7. The mutant strain showed higher resistance to substrate concentrations, as well as pH and temperature, than the wild type. The accumulation of PHA was increased by 3.18-fold compared to the wild type, and the production of PHA by the mutant M2-12 was constantly retained over 12 times of cultivation. The mutation and optimization strategy appear to be suitable for producing high density PHA, reducing the medium cost and consequently lowering the production cost. Interestingly, the mutant strain could synthesize the novel PHA copolymers such as 3-hydroxyvalerate and 3-hydroxyhexanoate, which were not produced by the wild type.     

Pearl millet, a source of alpha amylase production by Bacillus licheniformis

The present study is concerned with the selection of economically available agricultural starchy substrate for the production of alpha amylase by Bacillus licheniformis. Different agricultural starchy substrates such as soluble starch, hordium, pearl millet, rice, corn, gram and wheat starch were tested for the production of alpha amylase by parental and its mutant derivatives. The production of alpha amylase was 10-folds better by the mutant strain B. licheniformis GCUCM-30 than the parental strain when pearl millet starch at 1.5% level and nutrient broth concentrations at the level of 0.25% was supplemented to the fermentation medium.     

Phosphate enrichment and fed-batch operation for prolonged beta-lactamase production by Bacillus licheniformis

AIMS: Investigation of the phosphate effect and feeding strategy, i.e. linear and exponential feeding, to improve beta-lactamase production by Bacillus licheniformis considering the viability of the cells. METHODS AND RESULTS: Effect of phosphate enrichment on beta-lactamase production was investigated and resulted in 1.2-fold increase in beta-lactamase activity. Thereafter, exponential and linear feed profiles were established, after an initial batch phase for t = 0-7.5 h. The highest beta-lactamase activity was obtained at fed-batch operation with exponential feeding (FBO1) condition as A = 106 U cm(-3), which is c. 1.7-fold higher than that of the phosphate-enriched batch operation (PE-BO). CONCLUSIONS: Biphasic variations in beta-lactamase production was enhanced to monophasic variation with the exponential feeding strategy where the activity was obtained as A = 106 U cm(-3) at t = 16 h. SIGNIFICANCE AND IMPACT OF THE STUDY: Phosphate enrichment decreases the intracellular ammonium concentration and organic acid excretion, but increrases beta-lactamase production. When batch operation (BO) and PE-BO are compared, it is seen that succinic acid formation decreased with the phosphate enrichment as a result of smooth operation of the tricarboxylic acid cycle. At FBO1 despite the increased lactic and acetic acid formation, beta-lactamase production increased 1.7-fold, and 92% of the cells were alive at the end of the fermentation.     

l-Ribulose production by an Escherichia coli harboring l-arabinose isomerase from Bacillus licheniformis

Recombinant Escherichia coli harboring the l-arabinose isomerase (BLAI) from Bacillus licheniformis was used as a biocatalyst to produce l-ribulose in the presence of borate. Effects of substrate concentration, the borate to l-arabinose ratio, pH, and temperature on the conversion of l-arabinose to l-ribulose were investigated. l-Ribulose production was efficient when pH was higher than 9 and temperature was higher than 50 °C. Borate addition to the reaction mixture was essential for high conversion of l-arabinose to l-ribulose as it resulted in an equilibrium shift in favor of the product. Under the optimal conditions determined by response surface methodology, the E. coli harboring BLAI produced 375 g l⁻¹ L-ribulose from 500 g l⁻¹ l-arabinose at a reaction time of 60 min, corresponding to a conversion yield of 75% and productivity of 375 g l⁻¹ h⁻¹. When the resting recombinant E. coli cells were recycled, 85% of the yield was obtained even after seven cycles of reuse. The productivity and final concentration of l-ribulose obtained in the present study were the highest yet reported.     

Substrate and energy costs of the production of exocellular enzymes by Bacillus licheniformis

Substrate and energy costs of the production of exocellular enzymes from glucose and citrate by B. Iicheniformis S1684 as well as molar growth yields corrected for these costs of product formation were calculated using data from chemostat experiments. The calculations showed that 1.46-1.73 mol glucose and 2.31-2.77 mol citrate are needed for formation and excretion of 1 mol protein. Consequently, the values of the maximal product yield from substrate (Y(psm') g/mol) are 80 < Y(psm) < 95 when product is formed from glucose and 50 < Y(psm) < 60 when product is formed from citrate. The higher substrate costs for product formation from citrate are due to a higher level of CO(2) production during protein formation and a higher substrate requirement for the energy supply of product formation and excretion than when product is formed from glucose. The theoretical ATP requirement for protein synthesis could be determined reasonably well, but the energy costs of protein excretion could not be determined exactly. The energy costs of protein formation are higher than those of biomass formation or protein excretion. Molar growth yields corrected for the substrate costs of product formation were high, indicating a high efficiency of growth.Growth and production parameters were determined as well from experimental data of recycling fermentor experiments using a parameter optimization procedure based on a mathematical model describing biomass growth as a linear function of the substrate consumption rate and the rate of product formation as a linear function of biomass growth rate. The fitting procedure yielded two growth and production domains during glucose limitation. In the first domain the values for the maximal growth yield and maintenance coefficient were in agreement with those found in chemostat experiments at corresponding values of Y(spm). Domain 2 could be described best with linear growth and product formation. In domain 2 the rate of product formation decreased and more substrate became available for biomass formation. As a consequence the specific growth rate increased in the shift from domain 1 to 2. Domain 2 behavior most probably is caused by the rel-status of B. Iicheniformis S1684.