Now showing items 1-5 of 5
| Abstract: | L-Glutamine amidohydrolase (L-glutaminase, EC 3.5.1.2) is a therapeutically and industrially important enzyme. Because it is a potent antileukemic agent and a flavor-enhancing agent used in the food industry, many researchers have focused their attention on L-glutaminase. In this article, we report the continuous production of extracellular L-glutaminase by the marine fungus Beauveria bassiana BTMF S-10 in a packed-bed reactor. Parameters influencing bead production and performance under batch mode were optimized in the order-support (Na-alginate) concentration, concentration of CaCl2 for bead preparation, curing time of beads, spore inoculum concentration, activation time, initial pH of enzyme production medium, temperature of incubation, and retention time. Parameters optimized under batch mode for L-glutaminase production were incorporated into the continuous production studies. Beads with 12 × 108 spores/g of beads were activated in a solution of 1% glutamine in seawater for 15 h, and the activated beads were packed into a packed-bed reactor. Enzyme production medium (pH 9.0) was pumped through the bed, and the effluent was collected from the top of the column. The effect of flow rate of the medium, substrate concentration, aeration, and bed height on continuous production of L-glutaminase was studied. Production was monitored for 5 h in each case, and the volumetric productivity was calculated. Under the optimized conditions for continuous production, the reactor gave a volumetric productivity of 4.048 U/(mL·h), which indicates that continuous production of the enzyme by Ca-alginate-immobilizedspores is well suited for B. bassiana and results in a higher yield of enzyme within a shorter time. The results indicate the scope of utilizing immobilized B. bassiana for continuous commercial production of L-glutaminase |
| Description: | Applied Biochemistry and Biotechnology,Vol. 102–103, 2002 |
| URI: | http://dyuthi.cusat.ac.in/purl/4260 |
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| Continuous Prod ... in Packed-Bed Reactor.pdf | (89.19Kb) |
| Abstract: | A marine Pseudomonas sp BTMS-51, immobilized by Ca-alginate gel entrapment was used for the production of extracellular Lglutaminase under repeated batch process and continuous process employing a packed bed reactor (PBR). Immobilized cells could produce an average of 25 U/ml of enzyme over 20 cycles of repeated batch operation and did not show any decline in production upon reuse. The enzyme yield correlated well with the biomass content in the beads. Continuous production of the enzyme in PBR was studied at different substrate concentrations and dilution rates. In general, the volumetric productivity increased with increased dilution rate and substrate concentrations and the substrate conversion efficiency declined. The PBR operated under conditions giving maximal substrate conversion efficiency gave an average yield of 21.07 U/ml and an average productivity of 13.49 U/ml/h. The system could be operated for 120 h without any decline in productivity |
| Description: | Process Biochemistry 38 (2003) 1431 /1436 |
| URI: | http://dyuthi.cusat.ac.in/purl/4244 |
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| Continuous prod ... n a packed bed reactor.pdf | (208.7Kb) |
| Abstract: | Beauveria sp. BTMF S10 isolated from marine sediment produced extracellular L-glutaminase. Maximal L- glutaminase yield (46.9 U/ml) was obtained in a medium supplemented with 1% (w/v) yeast extract and sorbitol, 9% (w/v) sodium chloride and 0.2% (w/v) methionine, initial pH 9.0 and at 27 °C after 108 h. This enzyme was inducible and growth-associated. |
| Description: | World Journal of Microbiology & Biotechnology 15: 751±752, 1999. |
| URI: | http://dyuthi.cusat.ac.in/purl/4247 |
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| Extracellular p ... d from marine sediment.pdf | (70.09Kb) |
| Abstract: | Extracellular L-glutaminase production by Beau6eria sp., isolated from marine sediment, was observed during solid state fermentation using polystyrene as an inert support. Maximal enzyme production (49.89 U:ml) occurred at pH 9.0, 27°C, in a seawater based medium supplemented with L-glutamine (0.25% w:v) as substrate and D-glucose (0.5% w:v) as additional carbon source, after 96 h of incubation. Enzyme production was growth associated. Results indicate scope for production of salt tolerant L-glutaminase using this marine fungus |
| Description: | Process Biochemistry 35 (2000) 705–710 |
| URI: | http://dyuthi.cusat.ac.in/purl/4241 |
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| L-Glutaminase p ... lid state fermentation.pdf | (310.7Kb) |
| Abstract: | 3.4. Lipase (EC-3.1. 1.3) 3.5. Other Known Enzymes 3.6. Extremozymes (Enzymes from extremophiles) 3.7. Recognition of Valuable Extremozymes 4. Enzymes as Tools in Biotechnology 4.1. Restriction Enzymes from Marine Bacteria 4.2. Other Nucleases from Marine Bacteria 4.3. Bacteriolytic Enzyme by Bacteriophage from Seawater 5. Innovations in Enzyme Technology 5.1. Enzyme Engineering 5.2. Immobilization Technology 5.3. Gene Cloning for Marine Enzymes 6. Future Prospects |
| Description: | Biotechnology vol 9,pp 1-15 |
| URI: | http://dyuthi.cusat.ac.in/purl/4255 |
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| Marine Microbial Enzymes.pdf | (493.5Kb) |
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