Showing papers on "Trichoderma reesei published in 1979"

Induction of cellulolytic enzymes in Trichoderma reesei by sophorose.

Abstract: Sophorose (2-O-beta-glucopyranosyl-D-glucose) induces carboxymethyl cellulase in Trichoderma reesei QM6a mycelium with 1.5 to 2 h. The induction response to sophorose concentration, although complicated by the metabolism of sophorose, shows saturation kinetics. Most of the cellulase appears after most of the sophorose has been taken up, but the presence of an inducer is required to maintain cellulase synthesis because enzyme production ceases after separation of the mycelium from the induction medium. Cellulase appears simultaneously in the medium and in the mycelium, and no appreciable levels accumulate in the mycelium. Response to pH suggest either that synthesis and secretion of the enzyme are closely associated or concurrent events affected by surface interactions with the medium. Effects of temperature and pH on cellulase induction by sophorose are similar to those reported for induction by cellulose. The kinetics of absorption by mycelium differs from that of other beta-linked saccharides and glucose, the uptake of sophorose being much slower. Under our cultural conditions, sophorose appears to induce an incomplete array of cellulase enzymes, as indicated by enzymatic and electrophoretic studies.

Transglycosylation products of cellulase system of Trichoderma reesei

Abstract: From cellulose and cellobiose the formation of sophorose, laminaribiose, and gentiobiose was catalyzed byTrichoderma reesei culture filtrate containing exo- and endoglucanase and β-glucosidase activity and from cellobiose by a broken cell suspension fromT.reesei with β-glucosidase activity. The results indicate that β-glucosidase is the component responsible for transglycosylation reaction catalyzed byT.reesei cellulase enzyme complex.

Formation and release of cellulolytic enzymes during growth of Trichoderma reesei on cellobiose and glycerol

Abstract: Production and release of cellulolytic enzymes by Trichoderma reesei QM 9414 were studied under induced and non-induced conditions. For that purpose, a method was developmed to produce cellulases by Trichoderma reesei QM 9414 using the soluble inducer, cellobiose, as the only carbon source. The production was based on continuous feeding of cellobiose to a batch culture. For optimum production, the cellobiose supply had to be adjusted according to the consumption so that cellobiose was not accumulated in the culture. With a proper feeding program the repression and/or inactivation by cellobiose could be avoided and the cellulase production by Trichoderma reesei QM 9414 was at least equally as high as with cellulose as the carbon source.

Cellulase production and ammonia metabolism in Trichoderma reesei on high levels of cellulose.

Abstract: Trichoderma can be cultured in stirred-tank fermentors on high (8%)cellulose concentrations without increasing the salt concentration of the medium when NH4OH is used to control pH and as a nitrogen source. Approximation 90% of the ammonia consumed by the organism can be added as NH4OH. The advantage of using high concentrations of cellulose is that culture filtrates with greater cellulase activity are obtained. The advantage of a low salts medium is that unwanted solutes in the final enzyme preparation are reduced. The appearance of cellulase in the medium occurs later than net ammonia uptake so that only 20% of the final amount of cellulase has appeared when 80% of the maximum amount of ammonia has been consumed.

Production of cellulases by Trichoderma reesei QM 9414 in fed-batch and continuous-flow culture with cell recycle.

Abstract: The scope in improving enzyme productivities from the cellulose fermentation process is examined in laboratory-scale fermentors. The maximum productivity (30 IU/liter hr) is attained in a continuous-culture process with cell recycle using modified medium containing 0.5% cellulose. Optimum dilution rate and recycle ratio are determined as 0.025 hr−1 and 1.2, respectively, for the process. The system is analyzed and steady-state equations for predicting enzyme protein concentrations in the fermentor are developed. In fed-batch cultures, slow addition of cellulose at high concentrations can improve enzyme productivity by as much as 33% over a batch process. The scope and results of using modified medium for cellulase production are also presented.

Studies on quantitative physiology of Trichoderma reesei with two‐stage continuous culture for cellulose production

Abstract: By employing a two-stage continuous-culture system, some of the more important physiological parameters involved in cellulose biosynthesis have been evaluated with an ultimate objective of designing an optimally controlled cellulose process. The two-stage continuous-culture system was run for a period of 1350 hr with Trichoderma reesei strain MCG-77. The temperature and pH were controlled at 32°C and pH 4.5 for the first stage (growth) and 28°C and pH 3.5 for the second stage (enzyme production). Lactose was the only carbon source for the both stages. The ratio of specific uptake rate of carbon to that of nitrogen, Q(C)/Q(N), that supported good cell growth ranged from 11 to 15, and the ratio for maximum specific enzyme productivity ranged from 5 to 13. The maintenance coefficients determined for oxygen, MO, and for carbon source, MC, are 0.85 mmol O2/g biomass/hr and 0.14 mmol hexose/g biomass/hr, respectively. The yield constants determined are: YX/O = 32.3 g biomass/mol O2, YX/C = 1.1 g biomass/g C or YX/C = 0.44 g biomass/g hexose, YX/N = 12.5 g biomass/g nitrogen for the cell growth stage, and YX/N = 16.6 g biomass/g nitrogen for the enzyme production stage. Enzyme was produced only in the second stage. Volumetric and specific enzyme productivities obtained were 90 IU/liter/hr and 8 IU/g biomass/hr, respectively. The maximum specific enzyme productivity observed was 14.8 IU/g biomass/hr. The optimal dilution rate in the second stage that corresponded to the maximum enzyme productivity was 0.026 ∼ 0.028 hr−1, and the specific growth rate in the second stage that supported maximum specific enzyme productivity was equal to or slightly less than zero.

Mathematical model for enzymatic hydrolysis and fermentation of cellulose by Trichoderma

Abstract: This paper describes a mathematical model for the enzymatic hydrolysis and fermentation of cellulose by Trichoderma reesei. The principal features of the model are the assumption of two forms of cellulose (crystalline and amorphous), two sugars (cellobiose and glucose), and two enzymes (cellulase and β-glucosidase). An inducer–repressor–messenger RNA mechanism is used to predict enzyme formation, and pH effects are included. The model consists of 12 ordinary differential equations for 12 state variables and contains 38 parameters. The parameters were estimated from four sets of experimental data by optimization. The results appear satisfactory, and the computer programs permit simulation of a variety of system changes.