Production of an extracellular proteinase and α-amylase byBacillus subtilis in chemostat

The formation of two extracellular enzymes (α-amylase and a proteinase) ofB. subtilis was investigated in batch and continuous cultures. Differences were observed in the production of both enzymes in batch culture when studied in flasks and in a fermentor. The values of proteinase activity from continuous cultivation never reached those obtained during batch cultivation. The optimal dilution rate for proteinase synthesis was 0.1 – 0.2/h. The optimal dilution rate for the production of α-amylase was 0.2 –0.3/h.     

Behavior of Bacillus thuringiensis var. kurstaki under continuous phased cultivation in a cyclone fermentor

Summary Growth, sporulation, insecticidal crystalline protein (ICP) production and plasmids of Bacillus thuringiensis var. kurstaki (HD-1) were investigated during batch and continuous phased cultivation using a laboratory scale cyclone fermentor. When grown in batch culture at 28°C, 93% of the cells sporulated and produced ICP within 10 h of commencement of stationary phase. The batch culture runs were completed within 50 h of inoculation. A predominantly sporogenous and crystalliferous cell population was also obtained by second, stage processing of culture harvested from the first 10 to 25 cycles of continuous phased cultivation. In contrast, after 25 or more cycles of cultivation the population in the continuous phased culture shifted towards a predominantly asporogenous and acrystalliferous one. Culture conditions in continuous phased cultivation did not affect the plasmid content of B. thuringiensis (HD-1), yet influenced sporulation and plasmid-coded ICP production.     

Acid in the first stage is a determinant factor for the solvent production in the two-stage continuous fermentation ofClostridium acetobutylicum

To maximise solvent production in a two-stage continuous culture ofClostridium acetobutylicum, a low concentration of solvents had to be maintained in the first vessel. A 19 g/l solvent concentration was achieved, if only 2 g/l acids were present in the first stage. The second stage was dependent on the metabolic state of the cells produced in the first fermentor.     

Calcium requirements of residual protease in Bacillus subtilis DB104

Summary Bacillus subtilis DB104, a double mutant which does not synthesize neutral or alkaline proteases, was shown to exhibit some residual proteolytic activity when grown in both batch and continuous cultures. A major protein component responsible for about 70% of extracellular residual protease activity was reversibly deactivated by removal of calcium.     

High-level production of recombinant glutamic acid-specific protease from Bacilllus licheniformis in Bacillus subtilis expression system

To obtain large quantities of glutamic acid-specific protease isolated originally from Bacillus licheniformis (BLase), an expression plasmid was constructed by inserting the BLase gene into a plasmid vector (pUB110) for Bacillus subtilis. B. subtilis strain ISW1214 harboring the resultant recombinant plasmid containing the coding and 5′-promoter and 3′-terminator regions of BLase gene secreted approximately 0.25 g/l of BLase in a culture medium contained in a 90-l jar fermentor, corresponding to nearly 10 times the natural production level and resulting in a stable large-scale production. The amount of BLase in the culture medium accounted for roughly 60% of the total extracellular proteins secreted from the recombinant strain, simplifying enzyme purification.     

Improved Succinic Acid Production in the Anaerobic Culture of an Escherichia coli pflB ldhA Double Mutant as a Result of Enhanced Anaplerotic Activities in the Preceding Aerobic Culture

Escherichia coli NZN111 is a pflB ldhA double mutant which loses its ability to ferment glucose anaerobically due to redox imbalance. In this study, two-stage culture of NZN111 was carried out for succinic acid production. It was found that when NZN111 was aerobically cultured on acetate, it regained the ability to ferment glucose with succinic acid as the major product in subsequent anaerobic culture. In two-stage culture carried out in flasks, succinic acid was produced at a level of 11.26 g/liter from 13.4 g/liter of glucose with a succinic acid yield of 1.28 mol/mol glucose and a productivity of 1.13 g/liter·h in the anaerobic stage. Analyses of key enzyme activities revealed that the activities of isocitrate lyase, malate dehydrogenase, malic enzyme, and phosphoenolpyruvate (PEP) carboxykinase were greatly enhanced while those of pyruvate kinase and PEP carboxylase were reduced in the acetate-grown cells. The two-stage culture was also performed in a 5-liter fermentor without separating the acetate-grown NZN111 cells from spent medium. The overall yield and concentration of succinic acid reached 1.13 mol/mol glucose and 28.2 g/liter, respectively, but the productivity of succinic acid in the anaerobic stage dropped to 0.7 g/liter·h due to cell autolysis and reduced anaplerotic activities. The results indicate the great potential to take advantage of cellular regulation mechanisms for improvement of succinic acid production by a metabolically engineered E. coli strain.     

Production of extracellular enzymes in continuous culture

The production of bacterial enzymes in batch fermentations is compared with results obtained in continuous culture. When studying the production of α-amylase inBacillus subtilis it was found that instability of the enzyme synthesis was due to nonhomogeneity of the population rather than to “the culture’s history” (i.e. succession of several physiological states necessary for the enzyme production). The plasmid contained in the production clone was found to be the factor responsible for the α-amylase production. Predominance of the production clone or of the nonproduction one depends on the cultivation conditions used. As compared with batch cultivation the continuous production yields higher enzyme concentrations under optimal conditions and the fermentor productivity may be four to five times higher.     

Synthesis and release of proteases byBacteroides fragilis

Protease production byBacteroides fragilis ATCC 25285 was determined in batch and continuous cultures. During exponential growth in batch culture, the majority of proteolysis was cell associated. However, as the bacteria reached stationary phase, most of the intracellular proteases were released into the culture medium. Measurements of alkaline phosphatase and -galactosidase, which are respectively periplasmic and cytoplasmic marker enzymes inB. fragilis, showed that secretion of proteases in the stationary phase was a discrete event and was not associated with a general release of cytoplasmic contents. When the bacterium was grown in continuous culture, cell-associated protease activity increased concomitantly with dilution rate (D=0.03–0.23/h). The ratio of intracellular to whole cell protease activity also increased with growth rate (11 at D=0.03/h; 11.7 at D=0.23/h). Extracellular protease activity was detected only in trace amounts in continuous cultures at the lowest dilution rate. Determinations of the distribution of extracellular protease activity in batch culture after 48 h incubation showed that the majority of proteolysis (ca. 90%) was soluble. Nevertheless, a proportion was associated with particulate fractions, which had high specific activities.     

Cloning and expression of the gene for neutral protease of Bacillus amyloliquefaciens in Bacillus subtilis

A Bacillus amyloliquefaciens neutral protease gene was cloned and expressed in Bacillus subtilis.The chromosomal DNA of B. amyloliquefaciens strain F was partially digested with restriction endonuclease Sau3AI, and 2 to 9 kb fragments isolated were ligated into the BamHI site of plasmid pUB110. Then, B. subtilis strain 1A289 was transformed with the hybrid plasmids by the method of protoplast transformation and kanamycin-resistant transformants were screened for the formation of large halo on a casein plate. A transformant that produced a large amount of an extracellular neutral protease harbored a plasmid, designated as pNP150, which contained a 1.7 kb insert.The secreted neutral protease of the transformant was found to be indistinguishable from that of DNA donor strain B. amyloliquefaciens by double immunodiffusion test and SDS-polyacrylamide gel electrophoresis.The amount of the neutral protease activity excreted into culture medium by the B. subtilis transformed with pNP150 was about 50-fold higher than that secreted by B. amyloliquefaciens. The production of the neutral protease in the transformant was partially repressed by addition of glucose to the medium.     

A coupled two-stage continuous fermentation for solvent production by Clostridium acetobutylicum

The effects of nitrogen and phosphate in batch and continuous AEB fermentations were tested. Both nitrogen- and phosphate-limited fermentations favored acid formation but not solvent production. A coupled two-stage continuous fermentation was performed for 30 days with a nitrogen-limited first stage fermentation for enhanced acid production. The bacteria from the acidogenic phase (first stage) fermentation were continuously pumped into a 14-l second stage fermentor with supplemental glucose and nitrogen for solvent production. The second stage fermentor had a maximum butanol productivity of 0.4 g l⁻¹ h⁻¹ (total solvent production was 0.6 g l⁻¹ h⁻¹) at a dilution rate of 0.06 h⁻¹.     

Improved stability of the continuous production of acetone-butanol by Clostridium acetobutylicum in a two-stage process

A stable continuous culture has been maintained for 30 days at a high 20 g/l solvent concentration. This substantial increase in the stability of the continuous culture ofClostridium acetobutylicum at the maximal solvent level was achieved by using a two-stage process with a dilution rate of 0.1 h^–1 in the first fermentor and 0.04 h^–1 in the second fermentor. The two-stage continuous fermentation allows an optimal growth of cells and induction of solvent metabolism in the first stage, and a maximal production yield of solvents in the second stage.     

Antibiotic production by Streptomyces aureofaciens using self-cycling fermentation

The self-cycling frementation (;rSCF) technique was applied to culture of Streptomyces aureofaciens. SCF is a method of continuous fermentation in which the metabolism of a microorganism is monitored by a measurement such as dissolved oxygen. These data are sent to a computer to allow it to control the system. Tetracycline production was observed only at exceedingly low iron concentrations in the growth medium. Repeatability of cycles was found to be dependent upon the presence of tetracycline in the fermentation broth as well as the strain of microorganism grown in the fermentor. Tetracycline was produced by an improved specific rate when compared to results in the literature for this organism grown using the batch method. (c) 1994 John Wiley & Sons, Inc.     

Accelerated process development for protease production in continuous multi-stage cultures

A fermentation process was developed and optimized for the production of a specific protease from Bacillus licheniformis PWD-1. Media formulations were constructed and crucial environmental parameters were optimized to enhance growth and product formation. Process dynamics of substrate consumption, biomass-, product-, as well as by-product formation were determined under controlled conditions in a bioreactor. Using kinetic data from batch- and continuous-culture experiments, a fed-batch process was developed producing proteolytic activities 10 times those found during regular batch culture. In one stage continuous stirred tank culture protease formation was completely decoupled from sporulation. Shift experiments in one-stage continuous cultures led to the development of a two-stage continuous stirred tank fermentation process using optimized conditions for growth in the first stage and protease formation in the second stage. Accordingly, the basis for a continuous production of the enzyme on a pilot scale was accomplished.     

Effect of simple and complex carbon sources,low temperature culture and complex carbon feeding policies on poly-3-hydroxybutyric acid (PHB) content and molecular weight (Mw) from Azotobacter chroococcum 6B

The molecular weight (M _w) of poly-3-hydroxybutyrate (PHB), produced by shake-flask culture of Azotobacter chroococcum showed little variation with increasing glucose concentration as carbon source (being in the range of 400–500 kDa), while M _w increased from 300–400 to 640 kDa when grown with increasing concentration of sugar cane molasses. Molecular weight increased nearly 30% from 48 to 72 h culture time when 5% molasses as carbon source was used, while with glucose the highest M _w was reached at 48 h. Under fermentor cultivation A. chroococcum produced PHB with a relatively high M _w of 1590 kDa at 53 h culture time when grown in modified Burk's medium with glucose as carbon source at an initial C/N ratio (molar basis) of 69 under fermentor cultivation. A batch glucose-grown ammonium-limited fermentor culture was repeatedly fed with sugar cane molasses (initial C/N ratio 69) and it was observed that PHB content curve decreased at a slower rate than in the fed-batch culture in which glucose and sucrose were not consumed in the culture medium after the feed.     

Screening fungi for the production of an inhibitor of HMG CoA reductase: Production of mevinolin by the fungi of the genus Pleurotus

Abstract Two thermophilic archaea belonging to the genus Sulfolobus , grown on glucose, produced an extracellular polysaccharide (EPS). The production of EPS conducted both in 90 1 fermentor and in batch culture reached the maximum during the stationary phase of growth. The chemical analysis (FT-IR, HPAE-PAD, UV, Optical Rotation) of the biopolymer and of its acid hydrolizate suggested glucose, mannose, glucosamine and galactose as major components of the sulfated heteropolysaccharide.     

Glucose repression of enterotoxins A, B and C and other extracellular proteins in staphlyococci in batch and continuous culture.

The production of enterotoxins, lipase and total extracellular protein by four strains of Staphylococcus aureus grown in batch culture at a controlled pH of 6.5 in a completely defined medium was markedly reduced by glucose or glycerol constantly maintained at 0.I M. A concomitant increase in the production of deoxyribonuclease, up to 13-fold, showed however that not all extracellular proteins are under the same control mechanism. The presence of glucose and glycerol in the medium also resulted in a rapid increase in the specific growth rate. However, growth of S. aureus s6 in Mgilimited continuous culture showed that glucose repression of enterotoxin B when the growth rate was held constant was more than twice that in batch culture. Therefore glucose repression can occur independently of an increase in growth rate. The specific rate of production of enterotoxin B, lipase, deoxyribonuclease, beta-haemolysin and total extracellular protein by S. aureus s6 increased as the growth rate increased from 0.07 to 0.24 h-1. Non-replicating cells grown in the absence of glucose produced considerable amounts of enterotoxin, and production was not repressed by the presence of glucose in the resuspension medium. In contrast, no enterotoxin B or C was obtained from nonreplicating cells grown in the presence of glucose. Chloramphenicol completely inhibited enterotoxin production by non-replicating cells, indicating that synthesis of new protein was required.     

Production of cyclomaltodextrin glucanotransferase of Bacillus circulans var. alkalophilus ATCC21783 in B. subtilis

Summary The cyclomaltodextrin glucanotransferase (CGTase, E.C. 2.4.1.19) gene from an alkalophilic Bacillus circulans var. alkalophilus ATCC21783 was cloned into Escherichia coli and B. subtilis. When cloned from E. coli to B. subtilis, the entire insert containing the CGTase gene was, depending on the plasmid construction, either unstable or the recombinant B. subtilis did not secrete the enzyme in significant amounts. To achieve efficient enzyme production in B. subtilis, the gene was placed under the control of the B. amyloliquefaciens -amylase promoter. In one of the constructions, both the promoter and the signal sequence of the gene were replaced with those of B. amyloliquefaciens, whereas in another construction only the promoter area was exchanged. The recombinant B. subtilis clones transformed with these plasmid constructions secreted CGTase into the culture medium 14 times as much as did the parental strain in shake flask cultures. In fermentor cultures in an industrially feasible medium the enzyme production was substantially higher, yielding 1.2 g/l of CGTase, which is about 33 times the amount of the enzyme produced by the parental strain in corresponding fermentations. Both of the plasmid constructions were stable when grown over 50 generations without antibiotic selection.     

Production of alkaline serine protease subtilisin Carlsberg by Bacillus licheniformis on complex medium in a stirred tank reactor

Bacillus licheniformis (DSM 641) was cultivated on complex medium in batch and fed-batch operations in a 20-l working volume stirred tank reactor. The medium composition (maltose, glucose, sucrose, fructose, ammonia, phosphate) and O₂ and CO₂ in the off-gas were monitored on-line; pH, pO₂, turbidity, culture fluorescence were monitored in situ; optical density, concentrations of sugars, amino acids, phosphate, proteins, DNA, protease activity and total solids content were monitored off-line. Problems of on-line sampling, cell concentration monitoring, and culture fluorescence measurements and the influence of medium components on the enzyme productivity are discussed. Close relationships between variations of pH, pO₂, O₂ transfer rate and CO₂ production rate on the one hand and cell mass and fluorescence intensity on the other were demonstrated in batch and in fed-batch cultures. Using suitable cultivation conditions, alkaline protease with high volume activity [15300 units (U)/ml] and specific activity (510 U/mg) was produced. By replacing the complex medium with a semisynthetic one, the volumetric activity was reduced by a factor of ten (to 1650 U/ml), but the specific productivity by a factor of only two (to 210 U/ml). Correspondence to: K. Schügerl     

Characteristics of Protease Production by Cephalosporium sp

We investigated protease formation by Cephalosporium sp. strain KM388, which produced trypsin inhibitor in the same cultures, in medium containing polypeptone, meat extract, and glucose (natural medium) and in medium containing NaNO₃, glucose, and yeast extract (semisynthetic medium). In natural medium, protease was secreted into the culture broth after cessation of growth caused by consumption of the polypeptone, the growth-limiting substrate. Enzyme formation in the stationary growth phase was due to de novo and so-called preferential synthesis, because cycloheximide immediately inhibited enzyme formation. In semisynthetic medium, protease was produced in parallel with mycelial growth, but production was repressed by the addition of polypeptone to the medium; protease production began after the added polypeptone was consumed. On the other hand, if glucose was eliminated from natural medium, the lag period of initiation of enzyme production was reduced until the late exponential phase. The addition of phosphate up to a concentration of 1.0% to natural medium also shortened the lag period and damped the pH change of the broth during cultivation.     

Effects of yeast extract and glucose on xanthan production and cell growth in batch culture of Xanthomonas campestris

Although available kinetic data provide a useful insight into the effects of medium composition on xanthan production by Xanthomonas campestris, they cannot account for the synergetic effects of carbon (glucose) and nitrogen (yeast extract) substrates on cell growth and xanthan production. In this work, we studied the effects of the glucose/yeast-extract ratio (G/YE) in the medium on cell growth and xanthan production in various operating modes, including batch, two-stage batch, and fed-batch fermentations. In general, both the xanthan yield and specific production rate increased with increasing G/YE in the medium, but the cell yield and specific growth rate decreased as G/YE increased. A two-stage batch fermentation with a G/YE shift from an initial low level (2.5% glucose/0.3% yeast extract) to a high level (5.0% glucose/0.3% yeast extract) at the end of the exponential growth phase was found to be preferable for xanthan production. This two-stage fermentation design both provided fast cell growth and gave a high xanthan yield and xanthan production rate. In contrast, fed-batch fermentation with intermittent additions of glucose to the fermentor during the stationary phase was not favorable for xanthan production because of the relatively low G/YE resulting in low xanthan production rate and yield. It is also important to use a moderately high yeast extract concentration in the medium in order to reach a high cell density before the culture enters the stationary phase. A high cell density is also important to the overall xanthan production rate. Received: 30 September 1996 / Received revision: 21 January 1997 / Accepted: 10 February 1997