Single, chemically defined sporulation medium for Bacillus subtilis: growth, sporulation, and extracellular protease production.

The composition and application of a single, chemically defined medium or growth and sporulation of Bacillus subtilis is described. At 37 degrees C cells grew with a doubling time of about 40 min; cultures attained near-maximal spore formation (70 to 80% by 12 h after the end of exponential growth and produced 1 X 10(9) to 2 X 10(9) heat-resistant free spores at 24 h. Dipicolinic acid production was completed between 7 and 11 h. Cells grown in the single, chemically defined medium excreted levels of serine and neutral proteases comparable to those excreted in nutrient broth medium.     

Changes of Exponential Growth Rates in Relation to Differentiation of Geotrichum candidum in Submerged Culture

Growth and differentiation of the imperfect fungus Geotrichum candidum were followed in submerged cultures containing a simple synthetic glucose salt medium. Uptake of glucose, ammonium and oxygen from the medium were measured during the entire growth perod. In 0.1% glucose the fungus grows with one exponential growth phase until all the glucose has been consumed. The arthrospores are formed in the stationary phase. In 0.5% glucose the growth curve has two exponential growth phases, one with a doubling time of 1.8 h and a second one with a doubling time of 4.9 h. The second exponential growth phase, which starts when less than 15% of the glucose and less than 30% of the ammonium have been consumed, is shown to be the sporulation phase. During this growth phase the oxygen saturation in the culture remained constant at about 50%.     

Effects of pH shifts, bile salts, and glucose on sporulation of Clostridium perfringens NCTC 8798

The sporulation of Clostridium perfringens NCTC 8798 was studied after exposing vegetative cells to: pH values of 1.5 to 8.0 in fluid thioglycolate broth (for 2h) and then transferring them to Duncan-Strong (DS) sporulation medium; sodium cholate or sodium deoxycholate (0.3 to 6.5 mM) in DS medium; or Rhia-Solberg medium with 0.4% (wt/wt) starch, glucose, or both added at 0 to 55 mM. At pH 1.5, no culturable heat-resistant spores were formed. For cells exposed to pH 3.0, 4.0, 5.0, or 6.0, increases in heat-resistant spores were not seen until after a lag of 12 to 13 h, whereas the lag was only 2 to 3 h for cells exposed to pH 7.0 or 8.0. Maximal spore crops were produced after only 6 to 8 h for cells exposed to pH 7 or 8, but 16 to 18 h was required for production of maximal spore crops by cells exposed to the lower-pH media. The addition of sodium cholate (3.5 to 6.5 mM) to DS medium only slightly reduced the culturable heat-resistant spore count from 1.9 X 10(7) to 3 X 10(6)/ml. The addition of 1.8 mM or more sodium deoxycholate reduced the culturable heat-resistant spore count to less than 10/ ml. When either starch or glucose alone was added to Rhia-Solberg medium there was no production of culturable heat-resistant spores, but a combination of 0.4% (wt/wt) starch and 4.4 mM glucose yielded 6 X 10(5) spores/ml. The spore production remained at this level for glucose concentrations of 6 to 22 mM, but then declined to about 3 X 10(3) spores per ml at higher concentrations.     

Effects of pH shifts, bile salts, and glucose on sporulation of Clostridium perfringens NCTC 8798.

The sporulation of Clostridium perfringens NCTC 8798 was studied after exposing vegetative cells to: pH values of 1.5 to 8.0 in fluid thioglycolate broth (for 2h) and then transferring them to Duncan-Strong (DS) sporulation medium; sodium cholate or sodium deoxycholate (0.3 to 6.5 mM) in DS medium; or Rhia-Solberg medium with 0.4% (wt/wt) starch, glucose, or both added at 0 to 55 mM. At pH 1.5, no culturable heat-resistant spores were formed. For cells exposed to pH 3.0, 4.0, 5.0, or 6.0, increases in heat-resistant spores were not seen until after a lag of 12 to 13 h, whereas the lag was only 2 to 3 h for cells exposed to pH 7.0 or 8.0. Maximal spore crops were produced after only 6 to 8 h for cells exposed to pH 7 or 8, but 16 to 18 h was required for production of maximal spore crops by cells exposed to the lower-pH media. The addition of sodium cholate (3.5 to 6.5 mM) to DS medium only slightly reduced the culturable heat-resistant spore count from 1.9 X 10(7) to 3 X 10(6)/ml. The addition of 1.8 mM or more sodium deoxycholate reduced the culturable heat-resistant spore count to less than 10/ ml. When either starch or glucose alone was added to Rhia-Solberg medium there was no production of culturable heat-resistant spores, but a combination of 0.4% (wt/wt) starch and 4.4 mM glucose yielded 6 X 10(5) spores/ml. The spore production remained at this level for glucose concentrations of 6 to 22 mM, but then declined to about 3 X 10(3) spores per ml at higher concentrations.     

Influence of Carbohydrates on Growth and Sporulation of Clostridium perfringens Type A

Growth and sporulation of Clostridium perfringens type A in Duncan and Strong (DS) sporulation medium was investigated. A biphasic growth response was found to be dependent on starch concentration. Maximal levels of heat-resistant spores were formed at a starch concentration of 0.40%. Addition of glucose, maltose, or maltotriose to a sporulating culture resulted in an immediate turbidity increase, indicating that biphasic growth in DS medium may be due to such starch degradation products. Amylose and, to a lesser extent, amylopectin resulted in biphasic growth when each replaced starch in the sporulation medium. A levels of heat-resistant spores approximately equal to the control was produced with amylopectin but not amylose as the added carbohydrate. Addition of glucose or maltose to a DS medium without starch at stage II or III of sporulation did not alter the level of heat-resistant spores as compared with the level obtained in DS medium with starch. Omission of starch or glucose or maltose resulted in an approximately 100-fold decrease in the number of heat-resistant spores, although the percentage of sporulation (90%) was unaffected. The role of starch and amylopectin in the formation of heat-resistant spores probably involves the amyloytic production of utilizable short-chain glucose polymers that provide an energy source for the completion of sporulation.     

Optimal protease production condition for Prevotella ruminicola 23 and characterization of its extracellular crude protease

In this study, Prevotella ruminicola 23 (ATCC 19189), a ruminal proteolytic bacterium, was used as protease producer to examine the optimal condition for protease production. The best carbon and nitrogen sources for the maximum growth were glucose with peptone. Both sucrose and glucose could stimulate high protease production. Casein and peptone are better nitrogen sources for protease production than other choice in this study. The best enzyme production condition was 18-20 h incubation which was at late log phase in the broth of 5% glucose or sucrose as carbon source with 0.1% ammonium chloride and 0.2% peptone as nitrogen sources. Most of the protease activity was secreted into broth (65%) and on cell surface (18%). The optimal temperature and pH for protease reaction were 40 degrees C and pH 6.8, respectively. After incubation for 6h, the crude extract maintained 50% of original protease activity at 30 and 50 degrees C, and protease activity was stable between pH 6 and 8. The protease inhibitor test showed that serine, aspartic acid and metallo-protease inhibitors could cause inhibition of proteolysis. Protein feedstuff degradation experiments suggested that protease in crude extract had higher degradation ability on fish meal, whey, and feather meal (2.39, 2.60 and 1.76 micromol aminoacid/mg enzyme/h) in comparison to soybean meal and blood meal (1.11 and 1.09 micromol aminoacid/mg enzyme/h). The protease in the crude extract should have application potential in term of improving utilization of fish meal and feather meal for monogastric animals.     

Production and Purification of the Metalloprotease of Bacillus polymyxa

The nutritional and environmental factors relating to the production of an extracellular protease by Bacillus polymyxa were investigated. The enzyme was produced in all media that supported growth of the microorganism, irrespective of the carbon source used. Arabinose and hydrolyzed starch, however, gave highest yields. The nature of the peptone had a significant effect on the level of protease produced. Calcium and manganous ions exerted a beneficial effect on protease production. Highest enzyme levels were obtained when the initial pH of the medium was within the range 5.9 to 7.0. When the pH of the medium was not controlled during the fermentation, the accumulation of the enzyme paralleled the growth of the microorganism and reached a maximum towards the end of the exponential phase. With a fixed pH of 6.8, the level of protease was only one-fifteenth of that obtained when the culture was allowed to maintain its own pH. In addition, accumulation of the protease reached a maximum somewhat earlier, i.e., in the mid-log phase of growth. A 70-fold increase in the specific activity of the protease was obtained by ammonium sulfate and acetone fractionation followed by gel filtration on Sephadex G-100. The purified protease behaved as a homogenous entity when eluted by a sodium chloride gradient from CM-cellulose at pH 6.9. An overall enzyme recovery of 60% was obtained.     

The influence of glucose, ammonium and magnesium availability on the production of protease and bacitracin by Bacillus licheniformis

Bacillus licheniformis was cultivated in a range of defined media varying in both the nature of the growth-limiting component and the concentration of excess nutrients. The compositions of the media were such as to ensure that the final absorbance (A430) of the culture was the same in each case. Samples taken during the stationary phase were assayed for their content of extracellular serine protease and bacitracin. The nature of the growth-limiting nutrient had a profound effect on the amounts of these products formed while those components which were present in excess also exerted an influence in proportion to their concentration. Thus, for example, a four-fold increase in serine protease production occurred when ammonium replaced glucose as the growth-limiting nutrient. Serine protease and bacitracin production responded differently to these varying cultural conditions suggesting they are subject to separate control mechanisms. The results are discussed in relation to the need for rigorously controlled cultural conditions during physiological studies of this nature.     

Physiological and genetic strategies for enhanced subtilisin production by Bacillus subtilis.

Defined minimal media conditions were used to assess and subsequently enhance the production of subtilisin by genetically characterized Bacillus subtilis strains. Subtilisin production was initiated by the exhaustion or limitation of ammonium in batch and fed-batch cultures. Expression of the subtilisin gene (aprE) was monitored with a chromosomal aprE::lacZ gene fusion. The beta-galactosidase production driven by this fusion reflected subtilisin accumulation in the culture medium. Subtilisin gene expression was temporally extended in sporulation-deficient strains (spoIIG), relative to co-genic sporogenous strains, resulting in enhanced subtilisin production. Ammonium exhaustion not only triggered subtilisin production in asporogenous spoIIG mutants but also shifted carbon metabolism from acetate production to acetate uptake and resulted in the formation of multiple septa in a significant fraction of the cell population. Fed-batch culture techniques, employing the spoIIG strain, were investigated as a means to further extend subtilisin production. The constant provision of ammonium resulted in linear growth, with doubling times of 11 and 36 h in each of two independent experiments. At the lower growth rate, the responses elicited (subtilisin production, glucose metabolism, and morphological changes) during the feeding regime closely approximated the ammonium starvation response, while at the higher growth rate a partial starvation response was observed.     

Repression of sporulation in Bacillus subtilis by L-malate.

L-Malate repressed sporulation in the wild-type strain of Bacillus subtilis. When 75 mM L-malate was added to the growth medium at the time of inoculation, the appearance of heat-resistant spores was delayed 6 to 8 h. The synthesis of extracellular serine protease, alkaline phosphatase, glucose dehydrogenase, and dipicolinic acid was similarly delayed. Sporulation was not repressed when malate was added to the culture at t4 or later. A mutant was selected for ability to sporulate in the presence of malate. This strain could also sporulate in the presence of glucose. The malate-resistant mutant grew poorly with malate as sole carbon source, although it possessed an intact citric acid cycle, and it showed increased levels of malic enzyme. This indicates a defect in the metabolism of malate in the mutant. A mutant lacking malate dehydrogenase activity was also able to sporulate in the presence of malate. A model for the regulation of sporulation by malate is presented and discussed. Citric acid cycle intermediates other than malate did not affect sporulation. In contrast to previous results, sporulation of certain citric acid cycle mutants could be greatly increased or completely restored by the addition of intermediates after the enzymatic block. The results indicate that the failure of citric acid cycle mutants to sporulate can be adequately explained by lack of energy and lack of glutamate.     

碳源对玫烟色虫草菌丝生长、芽生孢子产生及其耐热性的影响

提高虫生真菌孢子应对热胁迫的能力是生防菌应用研究的关键,为研究菌丝培养阶段碳源对玫烟色虫草Cordyceps fumosorosea IF-1106耐热性的影响,选择了麦芽糖、可溶性淀粉、蔗糖、葡萄糖、果糖、海藻糖为碳源的培养基对玫烟色虫草IF-1106进行液体培养,评估了不同碳源条件下菌丝的生长、产孢及所产芽生孢子的耐热性。结果表明,在菌株培养阶段,培养基中碳源的种类及浓度对菌丝产量、产孢量及所产芽生孢子的耐热性有显著影响,其中蔗糖为碳源时,所产芽生孢子的耐热性强,45 ℃热胁迫条件下LT₅₀为1.65 h;蔗糖浓度为40 g/L时,可产生大量耐热芽生孢子,液体培养3 d后产孢量可达3.43×10⁷个孢子/mL。为探索不同培养条件下所产芽生孢子耐热性不同的原因,提取了孢子内的海藻糖并采用离子色谱法对其进行了定量分析,发现耐热性高的芽生孢子胞内海藻糖含量普遍较低,可见海藻糖是与芽生孢子耐热性密切相关的内源物质。综上所述,选择适宜的培养基是调控孢子耐热性的有效途径,本研究为生产高耐热的玫烟色虫草生防制剂提供了有益的指导。     

Growth and development kinetics of Bacillus thuringiensis in batch culture

The kinetics of Bacillus thuringiensis growth and its assimilation of nutrient substances were studied under the conditions of batch cultivation in a complex medium containing yeast extract and in a chemically defined medium with amino acids. The growth of B. thuringiensis can be divided into five phases: exponential growth; decelerated growth; stationary phase when protein crystals are formed; stationary phase when spores are formed; lysis of sporangia releasing spores. The first phase may in turn be subdivided into three stages according to changes in the specific growth rate and substrate assimilation: a high specific growth rate and no glucose assimilation; an abrupt drop in mu and the beginning of intensive glucose assimilation from the medium; a new rise in the specific growth rate. As follows from the results of studying the kinetics of B. thuringiensis growth in a chemically defined medium, the above changes in the exponential growth phase are due to the fact that the culture assimilates yeast extract components in the complex medium or amino acids in the chemically defined medium during this phase, and then starts to assimilate glucose and ammonium in the following phases of growth.     

Rupture of bacterial spores with ammonium bicarbonate subsequently removed by sublimation

A new method for dry rupture of bacterial spores was developed. Ammonium bicarbonate crystals, used in place of sodium chloride or glass beads, are vigorously shaken with spores. The ammonium bicarbonate is removed subsequently by sublimation, yielding uncontaminated, disrupted spores. Increased recovery of glucose dehydrogenase and protease activity from Bacillus cereus spores was obtained with the new method.     

Influence of carbon source on production of a heat stable protease from Thermomonospora fusca YX

Summary Thermomonospora fusca YX produced a very active heat stable protease when incubated in media containing cellulose as the substrate. Cultures grown on Solka-floc generated the highest amount of protease whereas the protease was produced at significantly lower levels when T. fusca YX was grown on cellobiose or glucose. Negligible growth or protease production was observed when protein was used as a carbon source. The production of the protease did not appear to be constitutive. While rapid growth was observed on either cellobiose or glucose, protease levels were at least two to fourfold lower than for the T. fusca YX cultures grown on Solka-floc wich generated 33% less cell mass. Protease production was four times lower in cultures which employed casein hydrolysate (tryptone) or xylan as carbon sources than for cellulose.     

Growth Rates of Sulfolobus acidocaldarius in Nature

Turnover times for water passing through several Sulfolobus acidocaldarius-containing springs were determined by measuring the dilution rates of small amounts of sodium chloride that were added to the springs. Chloride was diluted out exponentially, while concentrations of the bacteria remained constant. Additionally, temperature, pH, and chemical composition of the springs also remained constant during the time that the chloride was being diluted. The springs are thus steady-state systems, and since the rates of bacterial growth must be at least equal to the chloride dilution rates, minimal doubling times for the bacterial populations can be calculated. Half-times for chloride dilution, equivalent to bacterial doubling times, were on the order of 10 to 20 h for springs ranging in volume from about 20 to 2,000 liters, but approximately 30 days for two larger springs of about 1 million liters. Formaldehyde-fixed cells of a serologically distinguishable strain of S. acidocaldarius were also added as markers to four of the smaller springs, and the dilution rates of these bacteria were compared with the chloride dilution rates. The rates agreed reasonably well, thus verifying the growth rates obtained from the chloride dilution rates. In three springs, exponential growth was studied by draining the springs and allowing them to refill with bacteria-free water. Exponential doubling times were on the order of a few hours, much more rapid than steady-state doubling times. The methods used in this work may have wider utility in aquatic environments.     

Biosynthesis of Poly-beta-Hydroxyalkanoates from Pentoses by Pseudomonas pseudoflava

The potential of Pseudomonas pseudoflava to produce poly-beta-hydroxyalkanoates (PHAs) from pentoses was studied. This organism was able to use a hydrolysate from the hemicellulosic fraction of poplar wood as a carbon and energy source for its growth. However, in batch cultures, growth was inhibited completely at hydrolysate concentrations higher than 30% (vol/vol). When P. pseudoflava was grown on the major sugars present in hemicelluloses in batch cultures, poly-beta-hydroxybutyric acid (PHB) accumulated when glucose, xylose, or arabinose was the sole carbon source, with the final PHB content varying from 17% (wt/wt) of the biomass dry weight on arabinose to 22% (wt/wt) of the biomass dry weight on glucose and xylose. Specific growth rates were 0.58 h on glucose, 0.13 h on xylose, and 0.10 h on arabinose, while the specific PHB production rates based on total biomass ranged from 0.02 g g h on arabinose to 0.11 g g h on glucose. PHB weight-average molecular weights were 640,000 on arabinose and 1,100,000 on glucose and xylose. The absolute amount of PHB in the cells decreased markedly when nitrogen limitation was relaxed by feeding ammonium sulfate at the end of the PHB accumulation stage of the arabinose and xylose fermentations. Copolymers of beta-hydroxybutyric and beta-hydroxyvaleric acids were produced when propionic acid was added to shake flasks containing 10 g of glucose liter. The beta-hydroxyvaleric acid monomer content attained a maximum of 45 mol% when the initial propionic acid concentration was 2 g liter.     

Effect of glucose on sporulation and extracellular amylase production byClostridium perfringens type A in a defined medium

The effect of glucose and other sugars on sporulation and extracellular amylase production byClostridium perfringens NCTC 8679 type A in a defined medium was studied. Cells grown in the presence of glucose and mannose yielded the highest levels of amylase activity, while disaccharides such as lactose, maltose, and sucrose resulted in moderate amylase production. Little amylase activity was detected in the medium in the presence of ribose or galactose. The concentration of each sugar resulting in highest amylase production was between 6 and 10mm except for fructose (25mm). Levels of heat-resistant spores decreased as sugar concentrations increased. The addition of even small amounts of glucose to the medium before exponential growth suppressed sporulation but maximized amylase activity. The addition of glucose after the initiation of sporulation did not inhibit spore formation. However, its addition to 3-h amylase-producing cells did inhibit subsequent sporulation but promoted the continued excretion of amylase. The different response to glucose between sporulating cells and amylase-producing cells suggests that the mechanisms of catabolite repression of extracellular amylase production and sporulation are distinct in this strain ofC. perfringens.     

Growth, pigment production and protease activity of Monascus purpureus as affected by salt, sodium nitrite, polyphosphate and various sugars

The effect of different levels of salt, sodium nitrite, polyphosphate and various sugars on growth, pigment production, protease activity and culture pH caused by Monascus purpureus was studied in broth medium and ground meat. The addition of sodium chloride (> 50.0 g l(-1)) and polyphosphate (> 3.0g l(-1)) to broth medium decreased mycelial growth, pigment production and protease activity of M. purpureus, whereas low concentrations of sodium nitrite (< 0.2 g l(-1)) promoted mycelial growth and pigment production. When the basal medium and ground meat contained salt, 150.0 g l(-1), the mould growth was stopped. The medium with fructose as carbon source proved to be the most suitable for mycelium growth and pigment production, with maltose and glucose being the second most productive. When sucrose and lactose were used as carbon sources, mycelium growth and pigment production were inhibited but the protease activity increased significantly. The mould showed more tolerance to salt and polyphosphate in ground meat than in broth medium and used sucrose as a carbon source as well as glucose for growth and pigment production in the meat mixture.     

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.     

Some observations on protease production in continuous suspension cultures of Bacillus firmus

Invariance of culture conditions in steady state continuous cultures make these a very valuable tool to study the influence of various culture parameters on cell growth and synthesis of primary and secondary metabolites. The result of a parametric study on production of protease in continuous suspension cultures of Bacillus firmus NRS 783 are reported in this article. This strain is a superior producer of an alkaline protease with major application in the detergent industry. The parameters investigated include dilution rate and concentrations of yeast extract, ammonium, and inorganic phosphate in the bioreactor feed, glucose being the principal carbon source in all experiments. The regulatory effects of the key culture parameters on cell growth, synthesis and secretion of protease, and production of acetic acid are investigated. The relations among the specific cell growth rate, specific utilization rates of the principal carbon, nitrogen, and phosphorous sources, and specific production rates of two nonbiomass products, viz., acetic acid and protease, are examined, and the effects of the manipulated culture parameters on these relations, specific protease activity, and yields of cell mass, protease, and acetic acid on the basis of the principal carbon, nitrogen, and phosphorous sources are studied. An increase in dilution rate led to increases in specific utilization rates of the principal carbon, nitrogen, and phosphorous sources and specific production rates of acetic acid and protease and decreases in bulk activities/concentrations of the three products (acetic acid, cell mass, and protease). As a result, the productivities of the three species were maximized at an intermediate dilution rate. Increased supply of yeast extract (a rich source of amino acids, proteins, and vitamins, besides being an additional source of carbon, nitrogen, and phosphorus) promoted cell mass formation but reduced protease production per unit cell mass. Increased supply of nitrogen and phosphorous sources stimulated protease synthesis up to certain threshold levels and repressed the enzyme synthesis beyond the threshold levels. With increased supply of the nitrogen source, the phosphorous source was more efficiently utilized for cell growth and protease synthesis. Stable maintenance of continuous cultures of B. firmus over prolonged period is demonstrated in this study. (c) 1993 John Wiley & Sons, Inc.