Production of extracellular inulinase in high-cell-density fed-batch cultures of Kluyveromyces marxianus

The production of extracellular inulinase (\-1,2-d-fructan fructanohydrolase, EC 3.2.1.7) was studied in fed-batch cultures of the yeast Kluyveromyces marxianus CBS 6556 at 30 and at 40° C. At both temperatures, the final biomass concentration exceeded 100 g·l^–1 and more than 2 g enzyme. L^–1 of culture supernatant was produced. The biomass yield on O₂ at 40° C was substantially lower than at 30°C. Nevertheless, at 40° C a growth rate of 0.20 h^–1 could be maintained for a longer period than at 30° C. The unexpected higher O₂-transfer rate at 40°C is probably due to a lower viscosity of the culture broth. The 40°C fermentation took only 33 h as compared to 42 h at 30° C. These results indicate that K. marxianus is a promising host for the extracellular production of heterologous proteins under the control of the inulinase promoter.     

Effect of temperature on plasmid stability and expression of cloned cellulase gene in a recombinantBacillus megaterium

Summary The expression of carboxymethyl cellulase gene inBacillus megaterium (pCK108) was investigated with respect to temperature in batch culture. The suboptimal temperature supporting maximal cell growth rate was determined to be 30 °C at which stability of the plasmid pCK108 could be maintained stable. However, cellular plasmid contents, production rate of cellulase of the cell, and efficiency of the gene expression increased significantly with increase of the temperature from 30 °C to 44 °C, even though the plasmid stability decreased up to 60% level at the end of the culture.     

The effect of temperature,pH, and initial glucose concentration on the kinetics of ethanol production by Zymomonas mobilis in batch fermentation

Summary Zymomonas mobilis, strain ATCC 10988, was used to evaluate the effects of pH (5.0 to 8.0), temperature (30°C to 40°C), and initial glucose concentration (75 g/l to 150 g/l) on the kinetics of ethanol production from glucose using batch fermentation. Specific ethanol production rate was maximum and nearly constant over a pH range of 6.0 to 7.5. End-of-batch ethanol yield and specific growth rate were insensitive to pH in the range of 5.0 to 7.5. End-of-batch ethanol yield was maximum and nearly constant between 30°C and 37°C but decreased by 24% between 37°C and 40°C. All other kinetic parameters are greatest at 34°C. End-of-batch ethanol yield is maximum at an initial glucose concentration of 100 g/l. Specific growth rate reaches a maximum at 75 g/l, but specific ethanol production rate decreases throughout the range. The optimum initial glucose concentration of 100 g/l gives the highest ethanol yield at a specific ethanol production rate less than 10% below the maximum observed.     

Conversion of fat into yeast biomass in protein-containing waste-water

Summary Candida tropicalis S001 was grown on the lipid fraction of a protein-containing waste-water in order to (i) remove fat from the water, and (ii) produre yeast biomass for feed. The yeast cells were separated from the waste-water by sedimentation. Defatted waste-water was used for methane production and gave a yield of a 0.3 m³ methane/kg reduced chemical oxygen demand. The maximum specific growth rate (µ_max) of C. tropicalis growing on waste-water fat at pH 4.0 was 0.35 h^–1; the fat content was decreased from 8 g/l to about 0.1 g/l within 24 h. In continous culture a corresponding reduction was maintained at dilution rates up to 0.36 h^–1. The effect on growth of pH, temperature and CO₂ concentration was studied with triolein as the major carbon source. The µ_max was nearly constant (0.16 h^–1) in the pH and temperature range of 3.2–4.0 and 30°–38° C, respectively; 10% CO₂ was optimal for growth. Growth on triolein resulted in a biomass yield of 0.70 g dry weight/g fat. Offprint requests to: S. Rydin     

Effects of temperature shift on cell cycle, apoptosis and nucleotide pools in CHO cell batch cultues

Temperature reduction in CHO cell batch culture may be beneficial in the production of recombinant protein and in maintenance of viability. The effects on cell cycle, apoptosis and nucleotide pools were studied in cultures initiated at 37°C and temperature shifted to 30 °C after 48 hours. In control cultures maintained at 37 °C, viable cells continued to proliferate until the termination of the culture, however, temperature reduction caused a rapid decrease in the percent of cells in S phase and accumulation of cells in G-1. This was accompanied by a concurrent reduction in U ratio (UTO/UDP-GNAc), previously shown to be a sensitive indicator of growth rate. Culture viability was extended following temperature shift, as a result of delayed onset of apoptosis, however, once initiated, the rate and manner of cell death was similar to that observed at 37 °C. All nucleotide pools were similarly degraded at the time of apoptotic cell death. Temperature reduction to 30 °C did not decrease the energy charge of the cells, however, the overall rate of metabolism was reduced. The latter may be sufficient to extend culture viability via a reduction in toxic metabolites and/or limitation of nutrient deprivation. However, the possibility remains that the benefits of temperature reduction in terms of both viability and productivity are more directly associated with cultures spending extended time in G-1.     

Mass production of lipase by fed-batch culture of Pseudomonas fluorescens

Summary High concentration production of an extracellular enzyme, lipase, was achieved by a fed-batch culture of Pseudomonas fluorescens. During the cultivation, temperature, pH and dissolved oxygen concentration wwre maintained at 23°C, 6.5 and 2–5 ppm, respectively. Olive oil was used as a carbon source for microbial growth. To produce lipase effectively the specific feed rate of olive oil had to be maintained in a range of 0.04–0.06 (g oil) · (g dry cell)^-1 · h^-1. The CO₂ evolution rate was monitored to estimate the requirement of olive oil. The ratio of feed rate of olive oil to the CO₂ evolution rate was varied in the range of 20–60 g oil/mol CO₂. The higher value of the ratio accelerated microbial growth, but did not favour lipase production. Once the high cell concentration of 60 g/l had been achieved, the ratio was changed from 50 to 30 g oil/mol CO₂ to accelerate the lipase production. By this CO₂-dependent method a very high activity of lipase, 1980 units/ml, was obtained. Both the productivity and yield of lipase were prominently increased compared with a conventional batch culture.     

A new control strategy for yeast production based on the L/A* approach

Summary We studied the effect of temperature on the production of an extracellular neutral metalloproteinase of Bacillus megaterium in a laboratory fermentor under constant aeration and pH. The optimal temperature for growth (35–38° C) was higher than that for the synthesis of proteinase during exponential growth (below 31° C). The critical biomass concentration at which the exponential growth terminated decreased with increase in cultivation temperature. The specific rate of proteinase synthesis decreased when the critical biomass concentration was achieved. The observed decrease in proteinase synthesis was related to the cultivation temperature. The temperature also influenced the level of mRNA coding for proteinase. We formulated a mathematical model of cultivation describing the dependence of growth and proteinase synthesis on dissolved oxygen and temperature. The parameters of the model were identified for temperature intervals from 21 to 41° C using a computer. The optimum temperature for the enzyme production was 21° C. The productivity (enzyme activity/time) was maximal at 24–28° C. When optimizing the temperature profile of cultivation, we designed a suboptimal solution represented by a linear temperature profile. We have found that under conditions of continuous decrease in temperature, the maximal production of the proteinase was achieved at a broad range of temperature (26–34° C) when the rate of temperature decrease was 0.2–0.8° C/h. The initial optimal temperature for the enzyme productivity was in the range of 32–34° C. The optimum temperature decrease was 0.8° C/h. Offprint requests to: J. Chaloupka     

Effects of dissolved oxygen concentration and DO-stat feeding strategy on CoQ10 production with Rhizobium radiobacter

The cell growth and CoQ₁₀ (coenzyme Q₁₀) formation of Rhizobium radiobacter WSH2601 were investigated in a 7-1 bioreactor under different dissolved oxygen (DO) concentrations. A maximal CoQ₁₀ content (C/B) of 1.91 mg/g dry cell weight (DCW) and CoQ₁₀ concentration of 32.1 mg/l were obtained at the appropriate DO concentration of 40% (of air saturation). High DO concentration was favourable to the cell growth of Rhizobium radiobacter WSH2601. In order to achieve the maximal yield of CoQ₁₀ production, a new DO-stat feeding strategy was proposed, which significantly improved cell growth and CoQ₁₀ formation. With this strategy, the maximal CoQ₁₀ concentration and DCW reached 51.1 mg/l and 23.9 g/l, respectively, which were 67 and 44.8% higher than those obtained in the batch culture with DO concentration controlled.     

Staphylococcal Enterotoxin B and Nuclease Production Under Controlled Dissolved Oxygen Conditions

Enterotoxin B, nuclease, and total exoprotein production by Staphylococcus aureus strain S-6 was studied in a 0.5-liter fermentor system. While these extracellular products were elaborated over a wide range of aeration rates, maximal production occurred within the very narrow range of 125 to 150 cm(3) of air per min. The levels attained at the optimal aeration rate were not increased by maintaining a constant pH, although yield of enterotoxin:cell mass was highest at a constant pH of 7.0. During the growth cycle of the cultures, when aeration rate alone or aeration rate and pH were held constant, the dissolved oxygen (DO) levels, initially set at 100% of saturation, decreased to 5 to 10% 4 to 5 h after inoculation. The oxygen demand of the culture then maintained this level for an additional 4 to 6 h. This interval of low DO was characterized by maximal growth and exoprotein production. When the DO was controlled at a constant value throughout growth (by increasing or decreasing the airflow rate as appropriate), the culture demonstrated different optima for maximal growth and exoprotein production. A constant DO of 100% stimulated growth to extremely high densities, but the accumulation of toxin and nuclease was not observed. On the other hand, maintaining constant DO levels at 50 or 10% raised exoprotein levels higher than those achieved in a culture grown at the optimal aeration rate. Compared to the optimal aeration rate culture, the 10% DO culture yielded 20% more nuclease, 25% more toxin, and 40 to 50% more total exoprotein. These results indicate that it is the DO and not the aeration rate, per se, that is influential in controlling growth, toxin, nuclease, and total exoprotein production.     

Continuous culture of a recombinantEscherichia coli and plasmid maintenance for tryptophan production

Summary Production of tryptophan by a temperature sensitive recombinant microorganism (Escherichia coli W3110 trpLDtrpR ^ts tna ^– (pCRT185)) was investigated. In a single-stage continous culture, at an elevated temperature, 42°C (derepressed condition), tryptophan concentration increased in an early phase of the fermentation, and then gradually decreased with time. The reduction in the production rate was mostly due to the segregation of the plasmid and subsequent increase of plasmid-free cells. However, the plasmid could be maintained stable at 37°C, with repressed condition oftrp-operon, over 200 generations. A two-stage continuous culture system, i.e. cell growth was maintained in the first stage at 37°C and gene expression was induced in the second stage at 42°C, was therefore tested to improve the performance of the fermentation system. Operation of the two-stage system showed that the plasmid stability was significantly improved, and the specific rate of tryptophan production was maintained almost constant for more than 500 hours in the second stage.     

Mass production of poly-β-hydroxybutyric acid by fully automatic fed-batch culture of methylotroph

Summary Fifty-one methylotrophs were checked with respect to their ability of poly--hydroxybutyric acid (PHB) production from methanol. One of them, Pseudomonas sp. K, was chosen from its good growth on a minimum synthetic medium. Optimal temperature and pH for its growth were 30° C and 7.0, respectively. Concentrations of PO ₄ ^3- and NH ₄ ⁺ in the medium should be kept at low levels. PHB formation was stimulated by deficiency of nutrient such as NH ₄ ⁺ , SO ₄ ^2- , Mg²⁺, Fe²⁺ or Mn²⁺. Among them, nitrogen deficiency was chosen from its effectiveness and easiness for PHB accumulation.The microorganism was cultivated to produce a large amount of poly--hydroxybutyric acid (PHB) from methanol by means of microcomputer-aided fully automatic fed-batch culture technique. During the cultivation, temperature, dissolved oxygen concentration (DO), and methanol concentration in the culture broth were maintained at 30° C 2.5±0.5 ppm and 0.5±0.2 g/l, respectively. Other nutrients, nitrogen source and mineral ions, were also controlled to maintain their initial concentrations in the medium during cell growth phase. When the high cell concentration was achieved (160 g/l), feedings of ammonia and minerals were stopped and only methanol was supplied successively to accumulate PHB. At 175 h, high concentration of PHB (136 g/l) was obtained and total cell concentration became 206 g/l. DO must be maintained above the critical level during the PHB formation phase, too. PHB yield from methanol (g PHB/g methanol) was 0.18 and the maximum PHB content reached 66% of dry weight. Solid PHB produced by the strain had the melting point of 176° C and the average molecular weight of 3.0x10⁵.     

Effect of temperature and oxygen on cell growth and recombinant protein production in insect cell cultures

The effect of temperature and O₂ saturation on the production of recombinant proteins -galactosidase and human glucocerebrosidase by Spodoptera frugiperda cells (Sf9) infected with recombinant Autographa californica nuclear polyhedrosis virus was investigated. The rates of cell growth, glucose consumption, O₂ consumption and product expression were measured at temperatures between 22° C and 35° C. The results indicated that possible O₂ limitation may be alleviated without compromising the maximum cell yield by lowering the incubation temperature from 27° C to 25° C. The expression level of the recombinant proteins at 27° C was similar to that obtained at 22° C and 25° C; lower protein yields were obtained at 30° C. An increase in temperature from 22° C to 27° C led to earlier production of the proteins and to an increase in the proportion of the product released outside the cells. Correspondence to: J. Shiloach     

Polysulfide as a possible substrate for sulfur-reducing bacteria

Because of its low solubility it is unlikely that elemental sulfur serves as the direct substrate for sulfur-reducing bacteria. To test the hypothesis that polysulfide may represent a soluble intermediate of sulfur reduction, the maximal polysulfide concentrations formed from elemental sulfur in aqueous sulfide solutions were measured at near neutral pH and at temperatures up to 90°C. The saturation concentrations decreased by two orders of magnitude when the pH was lowered from 7 to 6 at a given temperature, and increased about tenfold when the temperature was raised from 37°C to 90°C at a given pH. The dissolution of 0.1 mM zerovalent sulfur in 1 mM sulfide (H₂S+HS^–) required a pH of 7.5 at 20°C and of only 6.1 at 100°C. A comparison with the growth optima of sulfur-reducers suggests that polysulfide is present at sufficient concentration at the growth conditions of the Bacteria and the moderately acidophilic Archaea. Polysulfide is apparently not available at the growth conditions of the extremely acidophilic Archaea. Alternative mechanisms for the sulfur utilization under these conditions are discussed.Abbreviations MOPS Morpholinopropanesulfonate - PIPES 1,4 piperazine-N,N-bis(2-ethanesulfonate) - HEPES N-2-hydroxy-ethylpiperazine-N-ethanesulfonate     

Ecological Physiology of a Coral Pathogen and the Coral Reef Environment

Laboratory studies on the ecological physiology of a coral pathogen were carried out to investigate growth potential in terms of environmental factors that may control coral diseases on reefs. The disease chosen for this study, white plague type II, is considered to be one of the major diseases of Caribbean scleractinian corals, affecting a wide range of coral hosts and causing rapid and widespread tissue loss. It is caused by a single pathogen, the bacterium Aurantimonas coralicida. A series of laboratory experiments using a pure culture of the pathogen was carried out to examine the roles of temperature, pH, and O₂ concentration on growth rate. Results revealed optimal growth between 30 and 35°C, and between pH values of 6 and 8. There was a distinctive synergistic relationship between pH and temperature. Increasing temperature from 25 to 35°C expanded the range of pH tolerance from a minimum of 6.0 down to 5.0. O₂ concentration directly affected growth rate, which increased with increasing O₂. The combined effects of increasing O₂ and increasing temperature resulted in a synergistic effect of more rapid growth. These laboratory results are discussed in terms of the coral host and the range of the environmental factors that occur on coral reefs. We conclude that changing environmental conditions in the reef environment, in particular observed increases in water temperature, may be promoting coral diseases by allowing coral pathogens to expand their ecological niches. In the case of the white plague type II pathogen, elevated temperature would allow A. coralicida to colonize the low pH environment of the coral surface mucopolysaccharide layer as an initial stage of infection. The synergistic effect between temperature and oxygen concentration appeared to be less environmentally relevant for this coral pathogen.     

Formation of Short-Chain Fatty Acids from H2 and CO2 by a Mixed Culture of Bacteria

The biological utilization of CO₂ and H₂ for the formation of short-chain fatty acids was studied by using a mixed culture of bacteria. Optimization of a medium was carried out in continuous culture to identify limiting factors which controlled growth and production of organic acids. The optimal pH for growth and acid production was 7.0 at 37°C; the maximal cell concentration obtained was 5.9 g of cells per liter (dry weight), and the maximal amount of volatile acids formed was 4.7 g/liter, with acetic acid as the predominant acid. With the optimized medium, it was found that the rate of transfer of hydrogen or carbon dioxide, or both, from gas to liquid was the limiting factor which controlled growth and production of acids.     

Enhanced resistance to peroxide stress in Escherichia coli grown outside their niche temperatures

Extended exposure of Escherichia coli to temperatures above and below their growth optimum led to significant changes in oxidant production and antioxidant defense. At 20 °C an increase in the intracellular H₂O₂ concentration and oxidized glutathione (GSSG) level was observed against a background of low levels of reduced glutathione (GSH) and decreased catalase and glutathione reductase (GOR) activities. The intracellular H₂O₂ and GSSG concentrations had minimal values at 30 and 37 °C, but rose again at 42 °C, suggesting that oxidative processes were intensified at high temperatures. An increase in temperature from 20 to 42 °C led to an elevation in the oxygen respiration rate and superoxide production; a 5-fold increase in the intracellular GSH concentration and in the GSH:GSSG ratio occurred simultaneously. Catalase HPI and GOR activities were elevated 4.4- and 1.5-fold, respectively. Prolonged exposure to sublethal temperatures facilitated an adaptation to subsequent oxidative stress produced by the addition of H₂O₂.     

Production of extracellular lactase fromFusarium moniliforme

Summary A strain ofFusarium moniliforme, previously used for microbial protein production, excreted lactase (-D-galactosidase, EC.3.2.1 23) when cultivated either in a whey liquid medium or on a wheat bran solid medium. The enzyme produced in both media had pH and temperature optima of 4–5 and 50–60°C respectively and was particularly suitable for processing acid whey.In the whey culture, maximum lactase yield was observed after 95 h of growth at 30°C and whey lactose concentration of 9%. The addition of ammonium, potassium and sodium ions to the growth medium considerably enhanced lactase production. A maximum enzyme yield corresponding to hydrolysis of 3 nmoles o-nitrophenyl--D-galactopyranoside sec^–1 ml^–1 of growth medium, at pH 5 and 60°C, was obtained.In the wheat bran culture, the maximum enzyme yield was obtained after 140 h of growth at 28–30°C. A marked increase in the enzyme production was observed when nitrate or phosphate was added to the growth medium. Also, the addition of certain agricultural by-products (molasses, whey) enhanced lactase production. The observed maximum yield corresponding to the hydrolysis of 182 nmoles of ONPG sec^–1 g^–1 of wheat bran, at pH 5 and 60°C, is comparable to that reported for certain microorganisms used commercially for lactase production.     

Production of dextranase byLipomyces starkeyi

Summary The optimal growth rate ofLipomyces starkeyi, with dextran as sole carbon source, was found within the pH range 2.5–4.0, and temperature between 25–30°C. This yeast was unable to grow above 33°C. Dextranase production optima paralleled growth optima, except at pH 2.5. Decrease in enzyme yield at this pH could not be attributed to poor yeast growth or enzyme stability.     

Effect of pH,aeration and sucrose feeding on the invertase activity of intactS. cerevisiae cells grown in sugarcane blackstrap molasses

S. cerevisiae was grown in a blackstrap molasses containing medium in batch and fed-batch cultures. The following parameters were varied: pH (from 4.0 to 6.5), dissolved oxygen (DO) (from 0 to 5.0 mg O₂L^–1) and sucrose feeding rate. When glucose concentration (S) was higher than 0.5 g L^–1 a reduction in the specific invertase activity of intact cells (v) and an oscillatory behavior of v values during fermentation were observed. Both the invertase reduction and the oscillatory behavior of v values could be related to the glucose inhibitory effect on invertase biosynthesis. The best culture conditions for attainingS. cerevisiae cells suitable for invertase production were: temperature=30°C; pH=5.0; DO=3.3 mg O₂L^–1; (S)=0.5 g L^–1 and sucrose added into the fermenter according to the equations: (V–V_o)=t²/16 or (V–V_o)=(V_f–V_o)·(e^0.6t–1)/10.This work was supported by FAPESP     

Kinetic analysis of L-lysine production by a fluoropyruvate sensitive mutant of B.lactofermentum

The kinetics of L-lysine production by a fluoropyruvate sensitive (FP^s) mutant of B.lactofermentum have been analysed in batch and continuous culture. Under optimal conditions (viz. T = 30° C, pH = 7.0, DO = 10 % air saturation) it was established that the initial phosphate level could be used to extend the batch culture to give an L-lysine.HCl concentration of 68.0 g/l and a yield of 0.43 g/g. In continuous culture the yield increased at low dilution rates under conditions similar to those for extended batch culture.