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Applied Biochemistry and Biotechnology: Part A: Enzyme Engineering and Biotechnology (v.101, #1)
Inexpensive isolation of β-d-glucopyranosidase from α-l-arabinofuranosidase, α-l-rhamnopyranosidase, and o-acetylesterase by Riccardo N. Barbagallo; Giovanni Spagna; Cristina Abbate; Giuseppe Azzaro; Rosa Palmeri (pp. 1-13).
β-d-Glucopyranosidase (βG, EC 3.2.1.21) has been isolated from some collateral activities, α-l-arabinofuranosidase (Ara, EC3.2.1.55), α-l-rhamnopyranosidase (Rha, EC 3.2.1.40), and o-acetylesterase (Est, EC 3.1.1.53), using a commercial enzyme preparation and a simple method economically sustainable for the food industry. The procedure comprises precipitation of extraneous substances by adding ethanol and CaCl2, ultrafiltration, and adsorption, first on bentonite and then on chitosan. The results obtained were the complete isolation of βG from the above-mentioned activities, a drastic reduction in extraneous compounds, such as brown substances and polysaccharides, and a slight increase in purification.
Keywords: β-d-Glucopyranosidase isolation; α-l-arabinofuranosidase; α-l-rhamnopyranosidase; o-acetylesterase; brown substances and polysaccharides
Effect of starting xylose concentration on the microaerobic metabolism of Debaryomyces hansenii by Attilio Converti; Patrizia Perego; Andrea Sordi; Paolo Torre (pp. 15-29).
Xylitol production by Debaryomyces hansenii NRRL Y-7426 was performed on synthetic medium varying the initial xylose concentration between 50 and 300 g/L. The experimental results of these tests were used to investigate the effect of substrate level on xylose consumption by this yeast. Satisfactory values of product yield on substrate (0.74–0.83 g/g) as well as volumetric productivity (0.481–0.694 g/L·h) were obtained over a wide range of xylose levels (90–200 g/L), while a worsening of kinetic parameters took place at higher concentration, likely due to a substrate inhibition phenomenon. The metabolic behavior of D. hansenii was studied, under these conditions, through a carbon material balance to estimate the fractions of xylose consumed by the cell for different activities (xylitol production, biomass growth, and respiration) during the lag, exponential, and stationary phases.
Keywords: Xylitol; Debaryomyces hansenii ; starting substrate concentration; synthetic medium; carbon material balance
Oxidation of kojic acid catalyzed by manganese peroxidase from Ceriporiopsis subvermispora in the absence of hydrogen peroxide by Francisco Bastidas; Ulises Urzúa; Rafael Vicuña (pp. 31-40).
We have previously reported the oxidation of kojic acid catalyzed by manganese peroxidase (MnP) from Ceriporiopsis subvermispora. This reaction is strictly dependent on Mn(II), although it does not require the addition of hydrogen peroxide. We have extended these studies because this reaction can be considered as a model system for the in situ generation of hydrogen peroxide in natural environments. We show here that oxidation of kojic acid with horseradish peroxidase (HRP) plus hydrogen peroxide or with manganic acetate rendered a product with identical chromatographic and spectral properties as the one obtained in the reaction catalyzed by MnP. The initial lag observed in the latter reaction decreased significantly upon UV irradiation of the substrate. On the other hand, ascorbic acid increased the lag and did not affect the yield of the reaction. The superoxide anion trapping agents glutathione, nitroblue tetrazolium, and superoxide dismutase markedly affected the reaction. In contrast, addition of the hydroxyl radical scavengers mannitol and salicylic acid had no effect. Based on these results, a mechanism for the MnP-catalyzed reaction is proposed.
Keywords: Manganese peroxidase; kojic acid; autooxidation; oxygen radicals; Ceriporiopsis subvermispora
A model explaining declining rate in hydrolysis of lignocellulose substrates with cellobiohydrolase I (Cel7A) and endoglucanase I (Cel7B) of Trichoderma reesei by Torny Eriksson; Johan Karlsson; Folke Tjerneld (pp. 41-60).
It is commonly observed that the rate of enzymatic hydrolysis of solid cellulose substrates declines markedly with time. In this work the mechanism behind the rate reduction was investigated using two dominant cellulases of Trichoderma reesei: exoglucanase Cel7A (formerly known as CBHI) and endoglucanase Cel7B (formerly EGI). Hydrolysis of steam-pretreated spruce (SPS) was performed with Cel7A and Cel7B alone, and in reconstituted mixtures. Throughout the 48-h hydrolysis, soluble products, hydrolysis rates, and enzyme adsorption to the substrate were measured. The hydrolysis rate for both enzymes decreases rapidly with hydrolysis time. Both enzymes adsorbed rapidly to the substrate during hydrolysis. Cel7A and Cel7B cooperate synergistically, and synergism was approximately constant during the SPS hydrolysis. Thermal instability of the enzymes and product inhibition was not the main cause of reduced hydrolysis rates. Adding fresh substrate to substrate previously hydrolyzed for 24 h with Cel7A slightly increased the hydrolysis of SPS; however, the rate increased even more by adding fresh Cel7A. This suggests that enzymes become inactivated while adsorbed to the substrate and that unproductive binding is the main cause of hydrolysis rate reduction. The strongest increase in hydrolysis rate was achieved by adding Cel7B. An improved model is proposed that extends the standard endo-exo synergy model and explains the rapid decrease in hydrolysis rate. It appears that the processive action of Cel7A becomes hindered by obstacles in the lignocellulose substrate. Obstacles created by disordered cellulose chains can be removed by the endo activity of Cel7B, which explains some of the observed synergism between Cel7A and Cel7B. The improved model is supported by adsorption studies during hydrolysis.
Keywords: Cellulase; cellulose; lignocellulose; hydrolysis; Trichoderma reesei ; synergism; adsorption; Cel7A; Cel7B
Possibilities for recycling cellulases after use in cotton processing by Helena Azevedo; David Bishop; Artur Cavaco-Paulo (pp. 61-75).
Preliminary recycling experiments with cellulase enzymes after cotton treatments at 50°C showed that activity remaining in the treatment liquors was reduced by about 80% after five recycling steps. The potential problems of end-product inhibition, thermal and mechanical deactivation, and the loss of some components of the cellulase complex by preferential and or irreversible adsorption to cotton substrates were studied. End-product inhibition studies showed that the build-up of cellobiose and glucose would be expected to cause no more than 40% activity loss after five textile treatment cycles. Thermal and mechanical treatments of cellulases suggested that the enzymes start to be deactivated at 60°C and agitation levels similar to those used in textile processing did not cause significant enzyme deactivation. Analysis of cellulase solutions, by fast protein liquid chromatography, before and after adsorption on cotton fabrics, suggested that the cellobiohydrolase II (Ce16A) content of the cellulase complex was reduced, relative to the other components, by preferential adsorption. This would lead to a marked reduction in activity after several treatment cycles and top-up with pure cellobiohydrolase II would be necessary unless this component is easily recoverable from the treated fabric.
Keywords: Cellulases; textile processing; enzyme recycling; adsorption; depletion; inhibition; deactivation
Possibilities for recycling cellulases after use in cotton processing by Helena Azevedo; David Bishop; Artur Cavaco-Paulo (pp. 77-91).
The adsorption and activity of a total cellulase (Trichoderma reesei) was measured and compared on undyed and dyed cotton fabrics. Recovery of enzymes from the reaction mixture and by desorption from the cotton substrate was evaluated. About 80% of the initial protein could be recovered. The removal of released products (soluble reducing sugars and dyes) from the treatment liquor and subsequent concentration of cellulase proteins was performed using an ultrafiltration membrane. Strong protein-dye interactions made it impossible to separate efficiently the dyes from the enzymecontaining treatment liquors. The use of surfactants did not enhance cellulase desorption from cotton fabric. Although anionic surfactants have a deactivating effect on cellulases, this effect seems to be reversible, since after ultrafiltration the cellulase activity was similar to that of enzymes desorbed with buffer only. Humicola insolens cellulases were shown to be much more sensitive to anionic surfactant than T. reesei cellulases. The use of cellulases that bind reversibly to cellulose is suggested for achieving more efficient cellulase recycling and for reducing backstaining by dye-cellulase complexes.
Keywords: Cellulases; textile processing; dyes; surfactants; recovery; desorption; ultrafiltration; tailoring