Statistical design was used to determine the optimal levels of medium components, the optimal initial pH of the enzyme production medium, the temperature of fermentation, age of the organism in the slant growth and the age of the inoculum for the production of chitinase in shake flask fermentations. The use of high concentrations of chitin and ammonium sulphate and exclusion of peptone and urea from the medium resulted in the production of higher level of the enzyme. The optimal concentrations of the medium components were 12.5 kg/m3 and 4.2 kg/m3 for the chitin and ammonium sulphate respectively. The effect of the addition of peptone and urea to the optimized medium was studied. The optimal values of initial pH and temperature were 5.6 and 28 °C respectively. The optimal age of the slant and the inoculum were found to be 105 h and 43 h respectively. The highest level of chitinase before optimization of the above variables was 0.054 U which was maximized to the level of 0.197 U.

T Panda

Department Of Chemical Engineering

CHITINASE

article

culture medium

ENVIRONMENTAL FACTOR

enzyme analysis

enzyme synthesis

fungus culture

HYPHOMYCETES

nonhuman

priority journal

Temperature

IIT Madras is a public technical and research university located in Chennai, Tamil Nadu. Founded in 1959, it is recognised as an Institute of National Importance.

IIT Madras has been ranked as the top engineering institute in India for four years in a row by the National Institutional Ranking Framework of the MHRD

It currently offers undergraduate, postgraduate and research degrees across 16 disciplines in Engineering, Sciences, Humanities and Management. About 596 faculty belonging to science and engineering departments and centres of the Institute are engaged in teaching, research and industrial consultancy.

IIT Madras

Optimization of carbon and nitrogen sources in the medium and environmental factors for enhanced production of chitinase by Trichoderma harzianum

Bioprocess Engineering

The generalized distance function approach is employed to obtain a suitable near optimal conditions of variables. The optimal values of variables (medium constituents, microbiological parameters, and process parameters) have been evaluated separately using single responses (either specific esterase activity or cell mass) as per central-composite-design and multi-responses following generalized distance function approach. The optimal conditions (medium composition (g l-1): dextrose, 13.43; peptone, 7.285; yeast extract, 2.55; and malt extract, 1.695; microbiological parameters: slant age, 39.9 h; inoculum age, 9.6 h; and number of cells, 1.49 × 108 numbers ml-1; process conditions: temperature, 29.9 °C; and pH, 6.2) obtained by generalized distance approach can be considered as a 'near optimal' solution of interactive multi-response systems of intracellular esterase synthesis by Saccharomyces cerevisiae. © 2007 Elsevier Ltd. All rights reserved.

Bioresource Technology

Critical analysis of application of generalized distance function for optimization of important variables for esterase synthesis by Saccharomyces cerevisiae

Chitinases help degradation of cell walls containing chitin and thus accelerates protoplast formation. It indirectly helps strain improvement and development of new strains which are economically viable for industrial use. Chitinases consist of endochitinase, exochitinase, β-N-acetylglucosaminidases and chitobiases. The endochitinases can be further characterized for better understanding of mechanism of the enzyme reaction. This review covers the recent advances in isolation and characterization of endochitinases and its components, gene encoding sequences and cloning.

Characterization and applications of chitinases from Trichoderma harzianum - A review

The chitinase fermentation process utilizing chitin as the sole carbon source was investigated in a stirred tank bioreactor. Agitator speed of 224 rpm was found to be most suitable for cell growth as well as for chitinase production. Chitinase yield decreased rapidly at higher agitator speed, while decrease in cell yield at higher agitator speed was not rapid. Probably, mass transfer limitation was predominant in the fermentation process at lower agitator speed. Higher agitator speed appears to reduce chitinase production.

Biochemical Engineering Journal

Submerged culture production of chitinase by Trichoderma harzianum in stirred tank bioreactors - The influence of agitator speed

Production of microbial chitinases have received increased attention in recent years due to its potential application in various fields. There has been an all around effort to increase the production of chitinases by using genetically engineered organisms and by incorporating modern fermentation techniques. This review presents a brief outline on the production of microbial chitinases which includes information on random screening and selection of chitinolytic organisms and the rationale behind the use of genetically engineered organisms. The problems and perspectives involved in large scale production of chitinases is discussed with special reference to bioreactor studies and new fermentation methods. The present limitations in the understanding of the chitinase fermentation process is also discussed and the scope for future investigation is outlined in this communication.

Production of microbial chitinases - A revisit

A novel optimization procedure has been developed to determine the best combination of variables in large scale fermentation systems. The self- directing optimization or the rotating simplex method of optimization was employed to determine the best suitable combination of parameters, pH (controlled), aeration rate and agitation rate for maximal production of chitinase by Trichoderma harzianum in batch culture. Extracellular enzyme activity increased from an initial value of 0.109 U under unoptimized conditions to a final value of 0.384 U after optimization. A controlled pH of 4.9, an aeration rate of 1.51 l-1 per min, and an agitation rate of 224 rpm was found to be the best combination.

Process Biochemistry

Self-directing optimization of parameters for extracellular chitinase production by Trichoderma harzianum in batch mode

Surface and submerged culture studies were carried out for the production of extracellular β-1,3-glucanase and carboxymethylcellulase from Trichoderma harzianum, NCIM 1185. The different parameters which influence the enzyme production, viz., spore age in the slant growth, seed age, and pH (initial) of the production medium have been optimized. The ranges of these parameters studied were: Spore age of T. harzianum between 2 and 10 days, seed age between 12 h and 48 h, and pH (initial) between 3 and 7. The other conditions of fermentation were: Temperature 30°C, gyratory shaker speed 160 rev. min-1. It was observed that the activities of β-1,3-glucanase and carboxymethylcellulase varied during the entire fermentation cycle which had a distinct effect on protoplast generation from T. reesei mycelium. The optimum values of the above-mentioned parameters for lytic enzymes production were: Spore age of T. harzianum in the slant growth 5 days, seed age 36 h, and pH (initial) 5.0 for both surface and submerged culture processes. © 1994 Springer-Verlag.

Production of β-1,3-glucanase from Trichoderma harzianum in surface and submerged culture processes and its role on protoplast generation from Trichoderma reesei mycelium

Efficient synthesis of a large number of viable protoplasts from Trichoderma longibrachiatum (Trichoderma reesei) mycelium has been found to be influenced by a number of factors. In this case, Trichoderma harzianum NCIM 1185 culture filtrate has been used to prepare protoplasts from Trichoderma longibrachiatum QM 9414. A method has been devised to isolate a large number of viable protoplasts from the mycelium. Detailed analysis of different factors affecting the synthesis of protoplasts from T. longibrachiatum has not yet been reported. The most suitable conditions for protoplasting were as follows: age of the organism in slant, 3 days; mycelium age, 20 h; volume of lytic enzymes, 190 ml; mycelial weight (dry equivalent), 1.66 g; time of contact with lytic enzymes, 2 h; temperature of protoplasting, 30°C; phosphate buffer, 25 mm, pH 6.5; KCl as osmotic stabilizer, 0.7 m. Proper spreading of the mycelium in contact with the lytic enzymes was also found to be necessary. © 1992.

Journal	Data powered by TypesetBioprocess Engineering
Publisher	Data powered by TypesetSpringer Verlag
ISSN	0178515X
Open Access	No