• Title/Summary/Keyword: filter paperase

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Production of Cellulase from Cellulomonas sp. KL-6 (Cellulomonas sp. KL-6에 의한 섬유소 분해효소의 생산)

  • Chung, Yung-Gun;Kwon, Oh-Jin
    • Applied Biological Chemistry
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    • v.38 no.6
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    • pp.490-495
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    • 1995
  • Among the cellulases by Cellulomonas sp. KL-6. CMCase and filter paperase, which were produced as the out enzymes of cell, had been much produced, but very small amounts of ${\beta}-glucosidase $, the enzyme of which is cell bound form, was produced by this organism. The optimal culture times for CMCase and filter paperase productions were 5 days, while that of ${\beta}-glucosidase$ was 4 days. When this strain was cultured under the optimal medium for enzyme production, CMCase, FPase and ${\beta}-glucosidase$ were $82\;units/m{\ell},\;80\;units/m{\ell}\;and\;1.2\;units/m{\ell}$, respectively. Thus these results were showed to increase enzyme productivities as about $60{\sim}70%$ than those produced in basal medium. $CaCO_3$ injected to the medium as the ratio of 0.1% was not only enhanced cellulase activities but also effective as acid neutralizing agent. The production effects of lignase and lactase by this bacterium in filter paper medium was not appeared.

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Production of Cellulolytic Enzymes by Aspergillus niger on Solid and Submerged State Fermentation (액체와 고체 발효 조건에서 Aspergillus niger의 셀루로오스계 효소 생산)

  • Chandra, M. Subhosh;Reddy, B. Rajasekhar;Choi, Yong-Lark
    • Journal of Life Science
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    • v.18 no.8
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    • pp.1049-1052
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    • 2008
  • Microbial production of cellulolytic enzymes by Aspergillus niger in solid state fermentation (SSF) and submerged state fermentation (SF) in laboratory scale was compared. Czapek Dox liquid broth amended with cellulose (0.5%) was used for cultivation in SF, whereas rice bran was used as a solid support, moistened with cellulose, amended Czapek Dox broth for growth in SSF. The production of Carboxymethyl cellulase, Filter paperase and ${\beta}$-Glucosidase was monitored at regular intervals. The peak production of the enzymes occurred within 3 days of incubation in SSF as against $\geq$ 7 days in SF. SSF gave higher yields of enzymes in comparison to SF. Maximum titres of 0.40, 0.62 and 0.013 U/ml in respect of FPase, CMCase and ${\beta}$-glucosidase in SSF were recovered as against 0.13, 0.06 and 0.0013 U/ml in SF respectively, at their respective peak time intervals. Hence, SSF appeared to be a better choice for production of cellulolytic enzymes by Aspergillus niger.

Production of Thermostable $\alpha$-Amylase and Cellulase from Cellulomonas sp.

  • EMTIAZI, G.,;I. NAHVI,
    • Journal of Microbiology and Biotechnology
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    • v.14 no.6
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    • pp.1196-1199
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    • 2004
  • A bacterium, isolated from rabbit's waste and identified as Cellulomonas sp., had cellulase and thermostable $\alpha$-amylase activity when grown on wheat bran. Maximum activity of thermostable $\alpha$-amylase was obtained by adding $3\%$ soluble starch. However, soybean oil (1 ml $1^{-1}$) could increase the production of $\alpha$-amylase and cellulase in 'wheat bran. The $\alpha$-amylase was characterized by making a . demonstration of optimum activity at $90^{\circ}C$ and pH 6- 9, with soluble starch as a substrate. The effect of ions on the activity and the stability of this enzyme were investigated. This strain secreted carboxymethyl cellulase (CMCase), cellobiase ($\beta$­glucosidase), and filter paperase (Fpase) during growth on wheat bran. Carboxymethy1cellulase, cellobiase, and Fpase activities had pH optima of 6, 5.5, and 6, respectively. CMCase and cellobiase activities both had an optimum temperature of $50^{\circ}C$, whereas Fpase had an optimum temperature of $45^{\circ}C$.

Optimization of Extraction of Fpase from the Fermented Bran of Aspergillus niger in Solid State Fermentation

  • Chandra, M. Subhosh;Reddy, B. Rajasekhar;Choi, Yong-Lark
    • Journal of Applied Biological Chemistry
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    • v.51 no.4
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    • pp.155-159
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    • 2008
  • A local isolate of Aspergillus niger was cultivated under optimal growth conditions on wheat bran in solid state fermentation. Filter paperase from fermented bran was separately extracted with different solvents to test the recovery of the enzyme. Among solvents tested, distilled water served as the best leachate, thus the conditions were further optimized with distilled water. After two washes of fermented bran with distilled water for 1.5 h each under stationary conditions at 1 g wheat bran: 5 mL distilled water, the maximum recovery of 13.5 $Ug^{-1}$ of wheat bran was obtained.

Saccharification of Foodwastes Using Cellulolytic and Amylolytic Enzymes from Trichoderma harzianum FJ1 and Its Kinetics

  • Kim Kyoung-Cheol;Kim Si-Wouk;Kim Myong-Jun;Kim Seong-Jun
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.10 no.1
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    • pp.52-59
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    • 2005
  • The study was targeted to saccharify foodwastes with the cellulolytic and amylolytic enzymes obtained from culture supernatant of Trichoderma harzianum FJ1 and analyze the kinetics of the saccharification in order to enlarge the utilization in industrial application. T. harzianum FJ1 highly produced various cellulolytic (filter paperase 0.9, carboxymethyl cellulase 22.0, ${\beta}$-glucosidase 1.2, Avicelase 0.4, xylanase 30.8, as U/mL-supernatant) and amylolytic (${alpha}$-amylase 5.6, ${\beta}$-amylase 3.1, glucoamylase 2.6, as U/mL-supernatant) enzymes. The $23{\sim}98\;g/L$ of reducing sugars were obtained under various experimental conditions by changing FPase to between $0.2{\sim}0.6\;U/mL$ and foodwastes between $5{\sim}20\%$ (w/v), with fixed conditions at $50^{\circ}C$, pH 5.0, and 100 rpm for 24 h. As the enzymatic hydrolysis of foodwastes were performed in a heterogeneous solid-liquid reaction system, it was significantly influenced by enzyme and substrate concentrations used, where the pH and temperature were fixed at their experimental optima of 5.0 and $50^{\circ}C$, respectively. An empirical model was employed to simplify the kinetics of the saccharification reaction. The reducing sugars concentration (X, g/L) in the saccharification reaction was expressed by a power curve ($X=K{\cdot}t^n$) for the reaction time (t), where the coefficient, K and n. were related to functions of the enzymes concentrations (E) and foodwastes concentrations (S), as follow: $K=10.894{\cdot}Ln(E{\cdot}S^2)-56.768,\;n=0.0608{\cdot}(E/S)^{-0.2130}$. The kinetic developed to analyze the effective saccharification of foodwastes composed of complex organic compounds could adequately explain the cases under various saccharification conditions. The kinetics results would be available for reducing sugars production processes, with the reducing sugars obtained at a lower cost can be used as carbon and energy sources in various fermentation industries.