enzyme production

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  • Microbial production of enzymes

  • Cellulase production A case studyA cellulosic enzyme system consists of three major components: endo--glucanase (EC 3.2.1.4), scission of cellulose chains -Yields glucose and cello-oligo saccharides. exo--glucanase (EC 3.2.1.91) and exo-attack on the non-reducing end of cellulase Yields cellobiose -glucosidase (EC 3.2.1.21).hydrolysis of cellobiose to glucose.

  • Schematic representation of sequential stages in cellulolysis

  • large number of microorganisms are capable of degrading cellulosesignificant quantities of cell-free enzymes Fungi - main cellulase-producing microorganisms Trichoderma and Aspergillus - high cellulase producers Trichoderma reesei QM-9414 - was selected as the best cellulase-producing strain - subjected to mono-colony isolation -strain KY-746 A plate screening system -the isolation and evaluation of mutants -for producing high titer cellulase UV and nitrosoguanidine (NTG) treatment A strain free from catabolite repression - was induced using a culture medium - glycerol and glucose, high titer strain was induced - L-sorbose to the medium.

  • Clearing zones formed by T. reesei mutants on Walseth's Cellulose Agar Plates

  • Genealogy of artificial mutants of Trichoderma reesei

  • Representative mutants derived from KY-746 were batch cultured in a 5-L fermentor.evaluation of carbon source utilization -increase in the concentration of Avicel - 6% in batch culture semi-batch culturing -initial Avicel concentration of 6%, followed by subsequent addition of 4% Avicel optimize the stirring rate, aeration volume, feed change, seed volume, and the seed culture period

  • Effect of initial substrate concentration on cellulase production by batch fermentation

  • Time course of cellulase production by T. reesei KDG-3 in a 1kL tank

  • Effect of alkali concentration of the production of cellulase from biomass

  • Cellulase fermentation was conducted with high-titer enzyme-producing strain CDU-11 under semi-batch conditions in a 4-L fermentor, using inexpensive carbon and nitrogen sources and the pH-shift system. This resulted in the production of CMCase activity exceeding 600 U/ml