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  • 1
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary The use of a column cellulose hydrolysis reactor with continuous enzyme recycling was demonstrated by incorporating a continuous ultrafiltration apparatus at the effluent end of the column reactor. Using this setup, over 90% (w/v) cellulose hydrolysis was achieved, resulting in an average sugar concentration of 6.8% (w/v) in the effluent stream. The output of the system was 1.98 g of reducing sugar/l/h with a ratio of 87% (w/v) of the reducing sugars being monomeric sugars. Batch hydrolysis reactors were less effective, resulting in 57% (w/v) of the cellulose being hydrolyzed. The output of the batch reactor was 1.33 g of reducing sugar/l/h with similar product concentrations and percentage of monomeric sugars. The ratio of reducing sugar/filter paper unit of cellulase activity for the column method was 69.1 mg/U as compared to only 21.2 mg/U for the batch reactor.
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 2
    Digitale Medien
    Digitale Medien
    Springer
    Applied microbiology and biotechnology 25 (1986), S. 256-261 
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary A column cellulose hydrolysis reactor was set up using a single passage of cellulase enzyme which was followed with a continuous percolation of buffer. Hydrolysis rates were found to decline precipitously upon the removal of the non-adsorbed cellulase components. By comparing specific activities of the cellulase before and after adsorption on the cellulose column, it was concluded that the adsorption efficiencies for the cellulase components decreased from exoglucanase (1,4-β-d-glucan cellobiohydrolase EC 3.2.1.91) to endoglucanase [1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] to β-glucosidase (β-d-glucoside glucohydrolase, EC 3.2.1.21). Of the adsorbed cellulase components, the rate of endoglucanase leaching from the cellulose column was 20 times that for the exoglucanase despite the greater adsorption efficiency of the latter. By analysing the cellulase components which were bound and not bound by the cellulose column and comparing them with a purified exoglucanase enzyme on sodium dodecyl sulfate polyacrylamide gels, it was confirmed that the major cellulase component adsorbed to the cellulose column was an exoglucanase component. The resultant loss of other cellulase components from the reactor was probably the cause for the much reduced rate of cellulose hydrolysis when these components were flushed out of the column.
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 3
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary A novel column cellulose hydrolysis reactor with constant enzyme recycling was operated under various conditions to determine the effects of retention time, temperature, cellulase concentration and exogenously added cellobiase on the concentration of the product stream and the productivities of the reactor. Short term (7 days) hydrolysis was best at 42°C while longer term (14 days) hydrolysis was better at 37°C. A retention time of 11 h and reactor cellulase concentration of 30 filter paper units per gram of cellulose gave the best compromise for efficient operation by minimizing product inhibition, maximizing product concentration and minimizing enzyme consumption. The addition of cellobiase to the reactor increased cellulose hydrolysis and raised the proportion of monomeric sugars in the hydrolysate. Continuous cellulose hydrolyses were maintained for 7 and 14 days at 42°C and 37°C, respectively, resulting in volumetric productivities of 6.82 and 4.84 g/l/h and average sugar concentrations of 7.3% and 6.0% (w/v), respectively. Greater than 95% (w/w) of the sugars produced were in the monomeric state. Average cellulase used for the two runs were 8.4 and 5.3 filter paper units per gram of sugar produced, respectively.
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 4
    Digitale Medien
    Digitale Medien
    Springer
    Applied microbiology and biotechnology 28 (1988), S. 377-379 
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary A novel bacterial isolate, Bacillus amyloliquefaciens strain AL 35, produced high yields of a cyclodextrin glycosyltransferase (CGT'ase) when grown in a submerged culture. The stability of CGT'ase to high temperature and alkaline pH enabled processing for cyclodextrin production to be carried out at 60° C and pH 9.0. Crude culture filtrates containing the CGT'ase could convert gelatinized starch substrates to predominatly α-cyclodextrins (up to 95% of the total cyclodextrin yields).
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 5
    Digitale Medien
    Digitale Medien
    Springer
    Applied microbiology and biotechnology 19 (1984), S. 365-372 
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary Hemicellulose-rich fractions from several agricultural residues were converted to 2,3-butanediol by a combined enzymatic hydrolysis and fermentation process. Culture filtrates from Trichoderma harzianum E58 were used to hydrolyze the substrates while Klebsiella pneumoniae fermented the liberated sugars to 2,3-butanediol. Approximately 50–60% of a 5% (w/v) xylan preparation could be hydrolyzed and quantitatively converted to 2,3-butanediol using this procedure. Although enzymatic hydrolysis was optimal at pH 5.0 and 50° C, the combined hydrolysis and fermentation was most efficient at pH 6.5 and 30° C. Combined hydrolysis and fermentation resulted in butanediol levels that were 20–40% higher than could be obtained with a separate hydrolysis and fermentation process. The hemicellulose-rich water-soluble fractions obtained from a variety of steam-exploded agricultural residues could be readily used by the combined hydrolysis and fermentation approach resulting in butanediol yields of 0.4–0.5 g/g of reducing sugar utilized.
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 6
    Digitale Medien
    Digitale Medien
    Springer
    Applied microbiology and biotechnology 24 (1986), S. 379-385 
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary A colorimetric method was modified for monitoring pentose release and utilization in the hydrolysis and fermentation of biomass substrates to fuels and chemicals. The proposed assay was specific for pentose monomers. Quantitation of pentoses by the assay method was not significantly interfered by other lignocellulosic components, common fermentation medium ingredients, and major volatile fermentation products encountered in biomass conversion processes. The assay procedure did not require sample pretreatment (e.g. deproteinization, desalting, or furfural extraction). Sugar estimation basing on the present assay correlated well with conventional sugar analysis by high performance liquid chromatography.
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 7
    Digitale Medien
    Digitale Medien
    Springer
    Applied microbiology and biotechnology 28 (1988), S. 546-552 
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary Various monomeric and polymerized cyclodextrins were investigated for their potential application in decaffeination. Treatment of aqueous caffeine solutions with monomeric gammacyclodextrin resulted in a significant reduction in the caffeine content of solutions over a wide range of caffeine concentration. Polymerized beta- and gamma-cyclodextrins were also demonstrated to be effective in removing caffeine by either a batch or column decaffeination process. Under the as-yet unoptimized process conditions, caffeine reduction of around 80% could readily be achieved. The process was applicable to caffeine-containing beverages (including coffee, tea, cocoa, and cola drinks) as well as theobromine-containing beverages (such as cocoa).
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 8
    ISSN: 1432-0614
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Summary A sequential co-culture approach was investigated for the conversion of lignocellulosic substrates to butanediol and ethanol. Growth of Clostridium thermocellum on solka floc and aspenwood xylan resulted in the release of extracellular endoglucanase and xylanase enzymes into the culture medium. Low levels of fermentation products were formed and unutilized sugars accumulated in the medium. Inoculation of Klebsiella pneumoniae as a sequential culture resulted in the rapid utilization of the accumulated sugars and the formation of additional fermentation products, including butanediol, ethanol, and acetoin. This approach was applicable to the use of mixed cellulose and hemicellulose substrates, including steam-exploded aspenwood. Further improvement in solvent production from steam-exploded substrates could be obtained by using a fed-batch approach to circumvent the problem of inhibitors associated with the natural substrates.
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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  • 9
    Digitale Medien
    Digitale Medien
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 30 (1987), S. 96-100 
    ISSN: 0006-3592
    Schlagwort(e): Chemistry ; Biochemistry and Biotechnology
    Quelle: Wiley InterScience Backfile Collection 1832-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: A process has been developed for the bulk purification of cellulase-free β-1,4-D-xylanase from the fungus Trichoderma harzianum E58. The process involved the primary step of ultrafiltering the culture filtrate via a 10,000-molecular-weight cut-off membrane to separate the cellulase (retentate) and xylanase (permeate) fractions. The cellulase component was concentrated by 40- to 60-fold, resulting in an enzyme complex that could effectively hydrolyze high concentrations of cellulose and xylan to glucose and xylose. The xylanase was concentrated and solvent exchanged by adsorption to a cationic exchanger, SP-ZetaPrep 250, followed by elution with a pH change in the buffer to give a purified and concentrated xylanase complex dissolved in a low-salt buffer. The resultant xylanase system was pure by the criteria of sodium dodecyl sulfate polyacrylamide electrophoresis, had a very high specific activity of 2400 IU/mg protein, was virtually free of filter paper activity, and had a ratio of contaminating filter paper activity of 2 × 10-6 (0.009% endoglucanase activity). Approximately 3.3 g protein, which contained in excess of 7 × 106 IU xylanase activity, was obtained from 17 L original culture filtrate. The process scheme was designed to facilitate scale-up to an industrial level of production.
    Zusätzliches Material: 4 Ill.
    Materialart: Digitale Medien
    Bibliothek Standort Signatur Band/Heft/Jahr Verfügbarkeit
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