Filamentous fungi and media for cellulase production in solid state cultures.

Cellulase production was evaluated in two reference strains (T. reesei Rut-C30 and T. reesei QM9414), two strains isolated from a sugarcane cultivation area (Trichoderma sp. IPT778 and T. harzianum rifai IPT821) and one strain isolated in a program for biodiversity preservation in São Paulo state (Myceliophthora thermophila M77). Solid state cultures were performed using sugarcane bagasse (C), wheat bran (W) and/or soybean bran (S). The highest FPA was 10.6 U/gdm for M77 in SC (10:90) at 80% moisture, which was 4.4 times higher than production in pure W. C was a strong inducer of cellulase production, given that the production level of 6.1 U/gdm in WC (40:60) was 2.5 times higher than in pure W for strain M77; T. reesei Rut-C30 did not respond as strongly with about 1.6-fold surplus production. S advantageously replaced W, as the surplus production on SC (20:80) was 2.3 times relative to WC (20:80) for M77.

Filamentous fungi and media for cellulase production in solid state cultures

Cellulase production was evaluated in two reference strains (T. reesei Rut-C30 and T. reesei QM9414), two strains isolated from a sugarcane cultivation area (Trichoderma sp. IPT778 and T. harzianum rifai IPT821) and one strain isolated in a program for biodiversity preservation in São Paulo state (Myceliophthora thermophila M77). Solid state cultures were performed using sugarcane bagasse (C), wheat bran (W) and/or soybean bran (S). The highest FPA was 10.6 U/gdm for M77 in SC (10:90) at 80% moisture, which was 4.4 times higher than production in pure W. C was a strong inducer of cellulase production, given that the production level of 6.1 U/gdm in WC (40:60) was 2.5 times higher than in pure W for strain M77; T. reesei Rut-C30 did not respond as strongly with about 1.6-fold surplus production. S advantageously replaced W, as the surplus production on SC (20:80) was 2.3 times relative to WC (20:80) for M77.

Effect of yeast extract on growth kinetics of Monascus purpureus.

Growth kinetics and red pigment production of Monascus purpureus CCT 3802 was studied. A reproducible inoculum with extremely dispersed hyphae for bioreactor runs was obtained through a two-step cultivation in a shaker. First, the spores were cultivated in a complex medium rendering a suspension of vegetative cells. In the second step these cells were grown in a semisynthetic medium. Two types of media were employed in the bioreactor runs: a semisynthetic (glucose, salts, and yeast extract), and a synthetic, without yeast extract. The inclusion of yeast extract, caused an increase in cell yield on glucose (Yx/s) as high as 40%. Also, yeast extract probably yielded a higher proportion of red pigment associated with the cell, relative to the synthetic medium. On the other hand, cells grown on the synthetic medium were slightly higher producers of red soluble pigments.

Bioaffinity extraction of glucoamylase in aqueous two-phase systems using starch as free bioligand.

Aqueous two-phase systems with bioligands bound to the polymer, usually polyethylene glycol (PEG), have high selectivity. However, such kind of systems can be costly since some specific synthetic ligands are expensive, making them non-viable for bioaffinity extraction of low-cost proteins. The use of free bioligands is an alternative for decreasing the high cost of these systems. This work describes the use of starch as a free bioligand on the partition of glucoamylase in PEG 300-phosphate system. The results were separated into two parts. In the first part, analysis of the starch distribution between the phases showed one-sided distribution to the bottom phase. In the second part, filtered broth from submerged cultivation of Aspergillus awamori, containing glucoamylase and contaminants, was submitted to the extraction in the system with starch. In the system without starch, glucoamylase and contaminants are partitioned in the upper phase. Upon starch addition, the partition coefficient of glucoamylase was decreased nine-fold without altering the partition of contaminants. These results indicate the possibility of separation of enzymes with high-molecular-mass and hydrophilic substrates, like glucoamylase, cellulase and pullulanase, from their contaminants in a one-step extraction. Since systems made of low-molecular-mass PEG partitioned almost all of the proteins to the upper phase, the separation can be achieved by extraction of the target enzyme in the bottom phase, as in the case of the presented study.

Separation and purification of glucoamylase in aqueous two-phase systems by a two-step extraction.

Extraction in two steps of glucoamylase was studied in poly(ethylene glycol) (PEG) and potassium phosphate systems at pH values of 6, 7 and 9. Ten different conditions using PEG 300, 600, 1500, 4000 and 6000 were studied. The bottom phase of the first extraction step, with the enzyme, was reused in an appropriate concentration of PEG to form the second extraction step. The optimal partitioning conditions for glucoamylase separation were obtained in PEG 4000 (first step), PEG 1500 (second step) at pH 7 and resulted in a three-fold increase in glucoamylase purification.

Recombinant gene expression in Escherichia coli cultivation using lactose as inducer.

The use of lactose as inducer of foreign gene expression under control of the lac UV5 promoter was investigated in recombinant Escherichia coli. Chicken muscle troponin C (TnC) gene was transcripted by T7 RNA polymerase and expressed in bioreactor cultivations after a feed-forward controlled fed-batch growth phase. Cell concentrations of 22 g l-1 dry cell weight (DCW)--before induction started--were used to achieve a TnC content of 19.5% of total cell protein through an induction strategy that combined the addition of a specific lactose amount of 4.7 g g-1 DCW divided into three pulses and the addition of yeast extract (1 g l-1) together with the second and the third lactose pulses. The results presented suggest that the residual lactose concentration plays an important role on the production of the heterologous protein.