Gene/Protein Disease Symptom Drug Enzyme Compound
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Query: EC:3.2.1.21 (beta-glucosidase)
 3,280 document(s) hit in 31,850,051 MEDLINE articles (0.00 seconds)

This research examined several enzymatic and microbial process for the conversion of waste cellulosic fibers into ethanol. The first was a one-stage process in which pulp fines were contacted with commercial enzyme solutions. The second process used sequential, multistage saccharification. The third used sequential enzyme addition in a countercurrent mode. Experiments compared the results with various feedstocks, different commercial enzymes, supplementation with beta-glucosidase, and saccharification combined with fermentation. The highest saccharification (65%) from a 4% consistency pulp and the highest sugar concentration (5.4%) from an 8% consistency pulp were attained when 5 FPU/g plus 10 IU/g of beta-glucosidase were used. Sequential addition of enzyme to the pulp in small aliquots produced a higher overall sugar yield/U enzyme than the addition of the same total amount of enzyme in a single dose. In the saccharification and fermentation experiments, we produced 2.12% ethanol from a 5.4% sugar solution. This represents 78% of the theoretical maximum. This yield could probably be increased through optimization of the fermentation step. Even when little saccharification occurred, the enzyme facilitated separation of water, fiber, and ash, so cellulase treatment could be an effective means for dewatering pulp sludges.
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PMID:Bioconversion of secondary fiber fines to ethanol using counter-current enzymatic saccharification and co-fermentation. 1039 79

Production of lactic acid from paper sludge has been performed by simultaneous saccharification and fermentation (SSF). The SSF process design was based on experimental data obtained from cellulose hydrolysis and fermentation. The SSF process was employed to avoid an excessively dense solution when the sludge content of the feed was higher than 15%; this is one of several benefits of SSF. The enzyme system used for hydrolysis of paper sludge for production of glucose was optimized. CMCase and beta-glucosidase with activities of 2.5 and 10 U mL(-1), respectively, were found to be optimum for hydrolyzing 5% sludge. In batch SSF 16 g L(-1) lactic acid was produced from 5% paper sludge with an yield of 80%. Paper sludge which served as a feed seemed to have a buffering effect during SSF, probably because of the inorganic ash component in the sludge. The final product concentration by SSF was observed to be limited by the cellulose content of the system, which can probably be resolved by intermittent feeding of the paper sludge. SSF of paper sludge fed in batch mode, with intermittent feeding, produced lactic acid at 162 g L(-1), with a yield of 74% and a productivity of 1.4 g L(-1) h(-1). The lactic acid production performance of the modified bioreactor improved after removal of indigestible solid materials from the upper compartment, which enabled the feed of paper sludge to be increased. A mathematical model is described which predicts glucose and subsequent lactic acid production on the basis of the rate expressions of each step of the SSF process. Saccharification kinetics were determined by experiments on enzymatic cellulose hydrolysis, by use of a Michaelis-Menten equation; growth kinetics of L. rhamnosus were determined by use of a Monod expression which incorporated lactic acid inhibition. The kinetic model is expected to predict the performance of the SSF process. For further use of the lactic acid, i.e. polylactic acid, it must be recovered and purified. Results from application of the simulated moving-bed (SMB) process for separation of lactic acid and acetic acid are given, as are several methods of lactic acid purification.
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PMID:Production of lactic acid from paper sludge by simultaneous saccharification and fermentation. 1521 7

Rice hulls, a complex lignocellulosic material with high lignin (15.38 +/- 0.2%) and ash (18.71 +/- 0.01%) content, contain 35.62 +/- 0.12% cellulose and 11.96 +/- 0.73% hemicellulose and has the potential to serve as a low-cost feedstock for production of ethanol. Dilute H2SO4 pretreatments at varied temperature (120-190 degrees C) and enzymatic saccharification (45 degrees C, pH 5.0) were evaluated for conversion of rice hull cellulose and hemicellulose to monomeric sugars. The maximum yield of monomeric sugars from rice hulls (15%, w/v) by dilute H2SO4 (1.0%, v/v) pretreatment and enzymatic saccharification (45 degrees C, pH 5.0, 72 h) using cellulase, beta-glucosidase, xylanase, esterase, and Tween 20 was 287 +/- 3 mg/g (60% yield based on total carbohydrate content). Under this condition, no furfural and hydroxymethyl furfural were produced. The yield of ethanol per L by the mixed sugar utilizing recombinant Escherichia colistrain FBR 5 from rice hull hydrolyzate containing 43.6 +/- 3.0 g fermentable sugars (glucose, 18.2 +/- 1.4 g; xylose, 21.4 +/- 1.1 g; arabinose, 2.4 +/- 0.3 g; galactose, 1.6 +/- 0.2 g) was 18.7 +/- 0.6 g (0.43 +/- 0.02 g/g sugars obtained; 0.13 +/- 0.01 g/g rice hulls) at pH 6.5 and 35 degrees C. Detoxification of the acid- and enzyme-treated rice hull hydrolyzate by overliming (pH 10.5, 90 degrees C, 30 min) reduced the time required for maximum ethanol production (17 +/- 0.2 g from 42.0 +/- 0.7 g sugars per L) by the E. coli strain from 64 to 39 h in the case of separate hydrolysis and fermentation and increased the maximum ethanol yield (per L) from 7.1 +/- 2.3 g in 140 h to 9.1 +/- 0.7 g in 112 h in the case of simultaneous saccharification and fermentation.
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PMID:Dilute acid pretreatment, enzymatic saccharification, and fermentation of rice hulls to ethanol. 1593 61

The effectiveness of two amendments for the in situ remediation of a Cd- and Ni-contaminated soil in the Louis Fargue long-term field experiment was assessed. In April 1995, one replicate plot (S1) was amended with 5% w/w of beringite (B), a coal fly ash (treatment S1+B), and a second plot with 1% w/w zerovalent-Fe iron grit (SS) (treatment S1+SS), with the aim of increasing metal sorption and attenuating metal impacts. Long-term responses of daily respiration rates, microbial biomass, bacterial species richness and the activities of key soil enzymes (acid and alkaline phosphatase, arylsulfatase, beta-glucosidase, urease and protease activities) were studied in relation to soil metal extractability. Seven years after initial amendments, the labile fractions of Cd and Ni in both the S1+B and S1+SS soils were reduced to various extents depending on the metal and fractions considered. The soil microbial biomass and respiration rate were not affected by metal contamination and amendments in the S1+B and S1+SS soils, whereas the activity of different soil enzymes was restored. The SS treatment was more effective in reducing labile pools of Cd and Ni and led to a greater recovery of soil enzyme activities than the B treatment. Bacterial species richness in the S1 soil did not alter with either treatment. It was concluded that monitoring of the composition and activity of the soil microbial community is important in evaluating the effectiveness of soil remediation practices.
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PMID:Biochemical parameters and bacterial species richness in soils contaminated by sludge-borne metals and remediated with inorganic soil amendments. 1651 62

Increasing proportions of coal fly ash were co-composted with municipal green waste to produce manufactured soil for landscaping use. Only the 100% green waste treatment reached a thermophilic composting phase (50 degrees C) which lasted for 6 days. The 25% and 50% ash treatments reached 36-38 degrees C over the same period while little or no self-heating occurred in the 75% and 100% ash treatments. Composted green waste had a low bulk density and high total and macro-porosity. Addition of 25% ash to green waste resulted in a 75% increase in available water holding capacity. As the proportions of added ash in the composts increased, the organic C, soluble C, microbial biomass C, basal respiration and activities of beta-glucosidase, L-asparaginase, alkali phosphatase and arylsulphatase enzymes in the composted products all decreased. It could be concluded that addition of fly ash to green waste at a proportion higher than 25% did not improve the quality parameters of manufactured soil.
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PMID:Chemical, microbial and physical properties of manufactured soils produced by co-composting municipal green waste with coal fly ash. 1953 64

The effect of metal ions in ash on enzymatic hydrolysis of crop straw has not attracted sufficient attention. In present study, rice straw with high ash content was taken as an example to study the effect. It was found that the common cations of ash (K(+), Mg(2+), Ca(2+), Al(3+), Mn(2+), Fe(3+), Cu(2+), and Zn(2+)) all showed inhibitive effects on cellulase at different levels, except for the stimulative effects of Ca(2+) and Mg(2+) on beta-glucosidase. Interestingly, washing treatment, combined with steam explosion, could effectively remove the ash cations of rice straw. The kinetic study of enzymatic hydrolysis indicated that, compared with the unwashed steam-exploded rice straw (SERS), the maximal hydrolysis velocity of washed SERS was increased by 12.5%. Therefore, the removal of ash by washing could facilitate the enzymatic hydrolysis of SERS.
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PMID:Effect of the ash on enzymatic hydrolysis of steam-exploded rice straw. 2068 16