Factors influencing the production of cellulases by Sporotrichum thermophile.

Cellulase production and growth of a strain of Sporotrichum thermophile were studied by using a mineral salts medium supplemented with yeast extract and insoluble cellulose. The effects of cultural conditions, such as pH, nitrogen source, substrate concentration, and temperature, were examined. Maximum production of C1 and CX cellulases occurred at 45 C in 2 to 4 days, in the presence of 1% Solka/Floc as substrate, when NaNO3 or urea used as sources of nitrogen. Under these conditions, cellulolytic activity of culture filtrates appeared to be similar to that reported for Trichoderma viride grown in a favorable environment. However, comparable yields of cellulase were produced by S. thermophile in less than one-quarter the time required by mesophilic fungi.     

Performance and population analysis of a non‐sterile trickle bed reactor inoculated with Caldicellulosiruptor saccharolyticus,a thermophilic hydrogen producer

Non‐axenic operation of a 400 L trickle bed reactor inoculated with the thermophile Caldicellulosiruptor saccharolyticus, yielded 2.8 mol H₂/mol hexose converted. The reactor was fed with a complex medium with sucrose as the main substrate, continuously flushed with nitrogen gas, and operated at 73°C. The volumetric productivity was 22 mmol H₂/(L filterbed h). Acetic acid and lactic acid were the main by‐products in the liquid phase. Production of lactic acid occurred when hydrogen partial pressure was elevated above 2% and during suboptimal fermentation conditions that also resulted in the presence of mono‐ and disaccharides in the effluent. Methane production was negligible. The microbial community was analyzed at two different time points during operation. Initially, other species related to members of the genera Thermoanaerobacterium and Caldicellulosiruptor were present in the reactor. However, these were out‐competed by C. saccharolyticus during a period when sucrose was completely used and no saccharides were discharged with the effluent. In general, the use of pure cultures in non‐sterile industrial applications is known to be less useful because of contamination. However, our results show that the applied fermentation conditions resulted in a culture of a single dominant organism with excellent hydrogen production characteristics. Biotechnol. Bioeng. 2009;102: 1361–1367. © 2008 Wiley Periodicals, Inc.     

Bioprocess exploration for thermostable α-amylase production of a deep-sea thermophile Geobacillus sp. in high-temperature bioreactor

Geobacillus sp. 4j, a deep-sea high-salt thermophile, was found to produce thermostable α-amylase. In this work, culture medium and conditions were first optimized to enhance the production of thermostable α-amylase by statistical methodologies. The resulting extracellular production was increased by five times and reached 6.40?U/ml. Then, a high-temperature batch culture of the thermophile in a 15?l in-house-designed bioreactor was studied. The results showed that a relatively high dissolved oxygen (600?rpm and 15?l/min) and culture temperature of 60°C facilitated both cell growth and α-amylase production. Thus, an efficient fermentation process was established with initial medium of pH 6.0, culture temperature of 60°C, and dissolved oxygen above 20%. It gave an α-amylase production of 79?U/ml and productivity of 19804?U/l·hr, which were 10.8 and 208 times higher than those in shake flask, respectively. This work is useful for deep-sea high-salt thermophile culture, where efforts are lacking presently.     

Production, characterization and application of a thermostable polygalacturonase of a thermophilic mould Sporotrichum thermophile Apinis

The production of polygalacturonase (PGase) by Sporotrichum thermophile Apinis in stirred submerged fermentation (SmF) was high in comparison with that in static conditions. Yeast extract (0.25%) and citrus pectin (2%) at pH 7.0 and 45 degrees C supported a high enzyme production in flasks agitated at 200 rpm. An overall 1.75-fold enhancement in PGase production was achieved as a result of optimization. The enzyme was optimally active at pH 7.0 and 55 degrees C, and exhibited t(1/2) of 4 h at 65 degrees C. The Km and Vmax values of the enzyme (for pectin) were 0.416 mg ml(-1) and 0.52 micromol mg(-1)min(-1), respectively. The PGase activity was stimulated by Mn(2+) and Fe(2+), but inhibited strongly by Mg(2+), and slightly by Tween 80 and Triton X-100. Among the additives tested, beta-mercaptoethanol exerted a strong inhibitory effect, suggesting a critical role of disulphide linkages in maintaining a suitable conformation of the enzyme. An increase in the yield of banana, grape and apple juices was recorded due to the treatment of fruit pulps with the mixture of enzymes (pectinase, xylanases and cellulase) of S. thermophile as compared to that with only pectinase. The yield of fruit juices did not increase with enhanced titre of cellulase in the enzyme mixture.     

Energetics of Bacillus stearothermophilus growth: molar growth yield and temperature effects on growth efficiency.

The major growth yield of a prototrophic strain of Bacillus stearothermophilus under aerobic conditions on salts medium containing ammonium nitrate as the nitrogen source and glucose or succinate as the carbon source was maximal at the lowest growth temperature employed and decreased steadily as the temperature was raised. The temperature optima for growth yield and for growth rate were thus different. The molar growth yield values of the thermophile, especially at the lower growth temperatures, were similar to those reported for aerobically grown mesophilic bacteria, both on glucose and on succinate. At the higher growth temperatures, a lower proportion of glucose carbon was incorporated into cells and a correspondingly greater proportion was left incompletely utilized in the medium, mostly as acetate. This suggests a greater inefficiency in the coordination of the nonoxidative and oxidative phases of glucose metabolism at the gigher temperatures. Another factor causing a decreased cell yield at higher temperatures was possibly an uncoupling of energy production from respiration. The rates of respiration by intact cells of the thermophile on glucose and on succinate followed the Arrhenius relationship from 55 C to 20 C, which is some 20 C below the minimal growth temperature of the organism. The Arrhenius constant was 17.1 kcal/mol for glucose oxidation and 13.5 kcal/mol for succinate oxidation. These results are comparable to those reported for some mesophiles, and they suggest that the inability of the thermophile to grow at temperatures below about 41 C is not due to an abnormally high temperature coefficient for the uptake and oxidation of the carbon source.     

Mathematical modelling and process optimization of a continuous 5-stage bioreactor cascade for production of poly[-(R)-3-hydroxybutyrate] by Cupriavidus necator

A multistage system for poly(hydroxyalkanoate) (PHA) production consisting of five continuous stirred tank reactors in series (5-CSTR) with Cupriavidus necator DSM 545 as production strain was modelled using formal kinetic relations. Partially growth-associated production of PHA under nitrogen limited growth was chosen as modelling strategy, thus the Luedeking-Piret’s model of partial growth-associated product synthesis was applied as working hypothesis. Specific growth rate relations adjusted for double substrate (C and N source) limited growth according to Megee et al. and Mankad-Bungay relation were tested. The first stage of the reactor cascade was modelled according to the principle of nutrient balanced continuous biomass production system, the second one as two substrate controlled process, while the three subsequent reactors were adjusted to produce PHB under continuous C source fed and nitrogen deficiency. Simulated results of production obtained by the applied mathematical models and computational optimization indicate that PHB productivity of the whole system could be significantly increased (from experimentally achieved 2.14 g L^?1 h^?1 to simulated 9.95 g L^?1 h^?1) if certain experimental conditions would have been applied (overall dilution rate, C and N source feed concentration). Additionally, supplemental feeding strategy for switching from batch to continuous mode of cultivation was proposed to avoid substrate inhibition.     

Effect of nitrogen limitation on enrichment of activated sludge for PHA production

Polyhydroxyalkanoates (PHA) are good candidates to plastics because of their material properties similar to conventional plastics and complete biodegradability. The use of activated sludge can be a cheaper alternative to pure cultures for PHA production. In this study, effect of nitrogen limitation during acclimatization period of biomass on production of polyhydroxyalkanoate was investigated. Activated sludge was selected in two sequencing batch reactors operated with and without nitrogen limitation. Batch tests were performed to examine polymer productions of activated sludges acclimatized to different nitrogen regimes. Responses of biomass to different organic loading rates, organic acids, and carbon to nitrogen (C/N) ratios were studied by determining specific polymer storage rate, polymer storage yield, and sludge polymer content of biomasses. Results obtained from batch experiments showed that concentrations of polymer accumulated by two different sludges increased directly with initial substrate concentration. Observed highest polymer yields for the biomasses enriched with and without nitrogen deficiency were 0.69 g COD PHA g(-1) COD S and 0.51 g COD PHA g(-1) COD S, and corresponding polymer contents of biomasses were 43.3% (g COD PHA g(-1) COD X) and 38.3% (g COD PHA g(-1) COD X), respectively. Polymer yields for both biomasses decreased with substrate shift however, biomass enriched with nitrogen deficiency adapted well to acetate-propionate mixture. The results presented in this study showed that polymer storage ability of biomass was improved more under dynamic conditions with nitrogen deficiency when compared to that without nitrogen deficiency. Limiting ammonia availability during batch experiments also caused higher polymer production by suppressing growth, as well as during enrichment of biomass.     

樟绒枝霉(Malbranchea cinnamomea)固体发酵产木聚糖酶的发酵条件优化

[目的] 研究樟绒枝霉(Malbranchea cinnamomea) CAU521利用农业废弃物固体发酵产木聚糖酶的发酵条件.[方法]采用单因素试验法优化影响菌株产酶的各个条件,包括碳源种类、氮源种类、初始pH、初始水分含量、培养温度及发酵时间共6个因素.[结果]获得的最佳产酶条件为:稻草为发酵碳源、2％(W/W)的酵母提取物为氮源、初始pH 7.0、初始水分含量80％和发酵温度45℃.在此条件下发酵6d后木聚糖酶的酶活力达到13 120 U/g干基碳源.[结论]樟绒枝霉固体发酵产木聚糖酶的产酶水平高,生产成本低,具有潜在的工业化应用前景.     

Thermal enzymes. III. Apyrase from a thermophilic Bacterium

An enzyme, apyrase, obtained from thermophile No. 2184 possesses heat stability at 65 °C., the temperature preferred by the organism for growth.Apyrase from the thermophile has an activation energy of 9600 cal./ mole. Its Michaelis constant is 0.00065 at 60 °C. The enzyme is inhibited by fluoride, citrate, and copper, but is activated by magnesium.Apyrase from a mesophilic bacterium, although possessing a fair amount of stability in the presence of substrate, does not have the resistance to heat possessed by the thermophile enzyme.The apyrase from potato is inactivated readily on heating in the absence of adenosine triphosphate.     

Beta-galactosidase of the superthermophilic anaerobic bacteria Thermoanaerobium sp. 2905 and its immobilization

The composition of nutrition medium for cultivating the extreme thermophilic anaerobe Thermoanaerobium sp. 2905 was optimized, which enabled the bacterial beta-galactosidase production to be substantially enhanced. Xylan and ammonium phosphate were selected as optimal carbon and nitrogen sources, respectively. The enzyme was purified fivefold by precipitation of the aqueous cell extract with alcohol (1:1, v/v), and crude preparation with a specific activity of 46 U per mg protein was obtained. Cells of the extreme thermophile were entrapped into natural or synthetic latex.     

Thermostable alpha-amylase production by an extreme thermophile Bacillus thermooleovorans

AIMS: alpha-Amylase production by a newly isolated thermophile, Bacillus thermooleovorans, was studied under different cultivation conditions. METHODS AND RESULTS: The influence of various carbon and nitrogen sources on alpha-amylase production was quantified in batch fermentation in shake flasks. Starch and tryptone were observed to be the ideal carbon and nitrogen sources, respectively. Cultivation of the organism in a chemically defined medium consisting of glucose, riboflavin, cysteine, MgSO4, K2HPO4 and NaCl led to a near twofold increase in the production of alpha-amylase in comparison with that in the complex medium. The increase in enzyme production was achieved using vitamins and amino acids. When the organism was grown in a laboratory fermenter in the optimized complex medium, the noticeable effects were the near abolition of the lag phase, a 2.2-fold increase in enzyme production and a reduction in optimal production time from 12 to 4-5 h. CONCLUSION: Enhancement of amylase production was achieved under various cultivation conditions. SIGNIFICANCE AND IMPACT OF THE STUDY: Bacillus thermooleovorans produces a calcium-independent and thermostable amylase which can find use in starch saccharification.     

Xylanase production by Ganoderma lucidum on liquid and solid state fermentation

Ganoderma lucidum, a white rot fungus, was exploited for its potentials to produce xylanase employing shake and solid-state culture conditions. Different culture conditions such as pH, temperature, carbon and nitrogen requirements for its growth and production of xylanase were optimized. The culture media pH 6.0-7.0 and temperatures 30 degrees-35 degrees C significantly promoted the growth as well as xylanase secretion into the media. Xylan and peptone were found to be the suitable carbon and nitrogen sources. Among the different agrowastes used, wheat bran was found to be the best substrate for the test fungus for the production of xylanase than sugarcane bagasse and rice bran in solid-state fermentation.     

Community analysis of hydrogen-producing extreme thermophilic anaerobic microflora enriched from cow manure with five substrates

The present study analyzed the community structures of anaerobic microflora producing hydrogen under extreme thermophilic conditions by two culture-independent methods: denaturing gradient gel electrophoresis (DGGE) and clone library analyses. Extreme thermophilic microflora (ETM) was enriched from cow manure by repeated batch cultures at 75 degrees C, using a substrate of xylose, glucose, lactose, cellobiose, or soluble starch, and produced hydrogen at yields of 0.56, 2.65, 2.17, 2.68, and 1.73 mol/mol-monosaccharide degraded, respectively. The results from the DGGE and clone library analyses were consistent and demonstrated that the community structures of ETM enriched with the four hexose-based substrates (glucose, lactose, cellobiose, and soluble starch) consisted of a single species, closely related to a hydrogen-producing extreme thermophile, Caldoanaerobacter subterraneus, with diversity at subspecies levels. The ETM enriched with xylose was more diverse than those enriched with the other substrates, and contained the bacterium related to C. subterraneus and an unclassified bacterium, distantly related to a xylan-degrading and hydrogen-producing extreme thermophile, Caloramator fervidus.     

Phytase production by a thermophilic mould Sporotrichum thermophile in solid state fermentation and its potential applications

Phytase production by a thermophilic mould Sporotrichum thermophile Apinis was investigated in solid state fermentation (SSF) using sesame oil cake as the substrate. Scanning electron microscopy of the fermented sesame oil cake revealed a dense growth of the mould with abundant conidia. Glucose, ammonium sulphate and incubation period were identified as the most significant factors by Plackett-Burman design. The optimum values of the critical components determined by central composite design of response surface methodology for the maximum phytase production were glucose 3%, ammonium sulphate 0.5% and incubation period 120 h. An overall 2.6-fold improvement in phytase production was achieved due to optimization. Highest enzyme production (348.76 U/g DMR) was attained at a substrate bed depth of 1.5 cm in enamel coated metallic trays. The enzyme liberated inorganic phosphate from wheat flour and soymilk with concomitant dephytinization and liberation of soluble inorganic phosphate.     

Production and characterization of the agarase ofCytophaga flevensis

Cytophaga flevensis produced an inducible agarase which was extracellular under most conditions tested. The effect of cultural conditions on the production of enzyme was studied in batch and continuous culture. In batch culture, production was optimal whenCytophaga flevensis was incubated at 20C in a mineral medium with agar as the sole carbon source and ammonium nitrate as the nitrogen source at an initial pH of 6.6–7.0. The enzyme appeared to be subject to catabolite repression, since its synthesis was repressed when glucose was added to the medium in batch culture. Furthermore, in continuous culture, enzyme production decreased with increasing growth rate. Extracellular agarase was partially purified and the enzyme preparation obtained was very stable. The enzyme has a molecular weight of 26000 daltons. It is a β-agarase which is highly specific for polysaccharides containing neoagarobiose units. The final products of hydrolysis of agarose by the endo-acting enzyme were neoagarotetraose and neoagarobiose. Optimal conditions for its activity were pH 6.3 and 30C. When agarose was used as a substrate, an apparent temperature optimum of 35C was found, due to gelling of the substrate during the assay procedure.     

Continuous hydrogen production during fermentation of alpha-cellulose by the thermophillic bacterium Clostridium thermocellum

Continuous hydrogen (H2) production during fermentation of alpha-cellulose was established using the thermophillic, anaerobic bacterium Clostridium thermocellum ATCC 27405. The objectives of this work were to characterize growth of C. thermocellum, quantify H2 production and determine soluble end-product synthesis patterns during fermentation of a cellulosic substrate under continuous culture conditions. A 5 L working volume fermentor was established and growth experiments were maintained for over 3,000 h. Substrate concentrations were varied from 1 to 4 g/L and the feed was introduced with continuous nitrogen gas sparging to prevent clogging of the feed-line. The pH and temperature of the reactor were maintained at 7.0 and 600 degrees C, respectively, throughout the study. At concentrations above 4 g/L, the delivery of alpha-cellulose was impaired due to feed-line clogging and it became difficult to maintain a homogenous suspension. The highest total gas (H2 plus CO2) production rate, 56.6 mL L(-1) h(-1), was observed at a dilution rate of 0.042 h(-1) and substrate concentration of 4 g/L. Under these conditions, the H2 production rate was 5.06 mmol h(-1). Acetate and ethanol were the major soluble end-products, while lactate and formate were greatly reduced compared to production in batch cultures. Concentrations of all metabolites increased with increasing substrate concentration, with the exception of lactate. Despite a number of short-term electrical and mechanical failures during the testing period, the system recovered quickly, exhibiting substantial robustness. A carbon balance was completed to ensure that all end-products were accounted for, with final results indicating near 100% carbon recovery. This study shows that long-term, stable H2 production can be achieved during direct fermentation of an insoluble cellulosic substrate under continuous culture conditions.     

Citric acid production by Candida strains under intracellular nitrogen limitation

A suitable strain and important factors influencing citric acid formation in yeasts were identified. Candida oleophila ATCC 20177 was chosen as the best citric acid producer from several Candida strains. Yields of 50 g/l citric acid were produced in shake flask and 80 g/l in fed-batch fermentations with 1.5 and 3 g/l NH(4)Cl under non-optimized conditions. Ammonium nitrogen was identified as the limiting substrate for citrate formation. Citric acid excretion begins a few hours after exhaustion of nitrogen in the medium. The importance of intracellular nitrogen limitation was clarified by elemental analysis of C. oleophila biomass. The nitrogen content of C. oleophila biomass decreased from 7.45% during the growth phase to 3.96% in the production phase. The biomass contained less carbon and more trace elements in the growth phase compared with the production phase. Relatively high intracellular NH(4)(+) concentration of about 1.2 mg/g biomass (~37.4 mM) was found during the production phase. The low intracellular nitrogen content and increase of intracellular NH(4)(+) concentration, possibly caused by proteolysis following extracellular nitrogen exhaustion, trigger citric acid production. Intracellular nitrogen limitation and the increase in intracellular NH(4)(+) concentration are the most important factors influencing citric acid formation in yeasts.     

Production of tannase from Aspergillus ruber under solid-state fermentation using jamun (Syzygium cumini) leaves

Tannase producing fungal strains were isolated from different locations including garbages, forests and orchards, etc. The strain giving maximum enzyme yield was identified to be Aspergillus ruber. Enzyme production was studied under solid state fermentation using different tannin rich substrates like ber leaves (Zyzyphus mauritiana), jamun leaves (Syzygium cumini), amla leaves (Phyllanthus emblica) and jawar leaves (Sorghum vulgaris). Jamun leaves were found to be the best substrate for enzyme production under solid-state fermentation (SSF). In SSF with jamun leaves, the maximum production of tannase was found to be at 30 °C after 96 h of incubation. Tap water was found to be the best moistening agent, with pH 5.5 in ratio of 1:2 (w/v) with substrate. Addition of carbon and nitrogen sources to the medium did not increase tannase production. Under optimum conditions as standardized here, the enzyme production was 69 U/g dry substrate. This is the first report on production of tannase by A. ruber, giving higher yield under SSF with agro-waste as the substrate.     

Evaluation of a compost obtained from forestry wastes and solid phase of pig slurry as a substrate for seedlings production

A composted material obtained from forestry wastes and solid phase of pig slurry was evaluated as a substrate component for the production of tomato and lettuce seedlings. Four different substrates were tested: compost (100C), a mixture of 75% compost and 25% peat substrate (75C), a mixture of 50% compost and 50% peat substrate (50C), and peat-based substrate (control). Compost increased the pH of the substrate from 6.3 (control) to 6.9 (100C) but did not affect the electrical conductivity (0.26 and 0.27 mScm(-1), respectively, for control and 100C). Germination and growth of lettuce seedlings were not affected by the substrate type, contrasting with tomato seedlings where the highest growth occurred at 100C substrate. Increasing compost percentage on substrate increased nitrogen, calcium and magnesium availability and, consequently, the concentration of these elements in plant tissues increased. On the contrary, potassium and manganese concentration decreased. Results from the study suggest that the compost studied is a good alternative to peat-based substrates for the production of vegetable seedlings.     

Effect of culture conditions on growth and esterase production by the moderate thermophile Bacillus circulans MAS2

Growth and esterase production (activity on p-nitrophenyl caprylate) by the newly isolated Bacillus circulans MAS2 bacterial strain were studied. The growth rate at 50°C was high (0.9 h^-1) on LB medium with glucose added. Esterase production followed growth with the majority of activity being intracellular during exponential growth phase. During stationary phase, the esterase activity was released in the culture medium. The strain was able to grow at 35– 55°C with maximum growth rate at 50°C, showing a pattern typical of a moderate thermophile. Growth occurred at pH 6–9 with a maximum at 8, with a similar pattern for the esterase production. Addition of glucose, fructose, sucrose or sodium acetate greatly promoted both growth and esterase production while starch, inulin, tributyrin or glycerol showed no effect. Complex nitrogen sources such as tryptone or yeast extract increased growth and esterase production while mineral sources (ammonium chloride or sulfate), glycine or glutamate showed no effect. An increase of tryptone plus yeast extract and glucose concentrations stimulated growth and esterase production which reached 160 U L⁻¹. Received 17 March 1999/ Accepted in revised form 25 June 1999