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  • 1985-1989  (6)
  • 1975-1979  (9)
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Year
  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 1 (1975), S. 95-119 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Azotobacter culture has been investigated in the physiological state in which it fixed molecular nitrogen. A chemically defined medium was formulated that would support the growth ofAzotobacter vinelandii, but not the growth ofSaccharomyces cerevisiae in pure culture, unless a nitrogen source was added. The yeast culture was allowed to grow in mixed culture with the bacterium. Transient and steady-state populations of each organism in mixed culture at various dilution rates were enumerated with hemocytometer under a microscope. The difference in size of the organisms permitted easy resolution. The essential nutrilite, nitrogen, which is fixed by the bacteria and required by yeast caused the yeast to be dependent on the growth of the bacterium. At low dilution rates the yeast population reflected changes in the numbers ofAzotobacter. The numbers ofAzotobacter were identical in pure culture or in mixed culture; thus the interaction can be termed competitive commensalism. In batch culture, yeast had no effect on the rate of nitrogen fixation byAzotobacter. E. Coli ML-30 had a slight inhibitory effect whileC1. pasteurianum exhibited a stimulating effect. In continuous culture at low dilution rates, yeast was found to increase the rate of nitrogen fixation byAzotobacter vinelandii by 4.5%. Differential equations characterizing commensalism in the chemostat have been proposed.
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  • 2
    Electronic Resource
    Electronic Resource
    [s.l.] : Nature Publishing Company
    Nature biotechnology 3 (1985), S. 591-591 
    ISSN: 1546-1696
    Source: Nature Archives 1869 - 2009
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: [Auszug] To the editor: This is a response to the letter from MIT's Arnold Demain (Sept. 1984) concerning inability on the part of some bioscientists from Israel to participate in the VIIth International Biotechnology Symposium held in New Delhi in February 1984. A key point seems to be missing from Dr. ...
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 21 (1979), S. 283-296 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The scope in improving enzyme productivities from the cellulose fermentation process is examined in laboratory-scale fermentors. The maximum productivity (30 IU/liter hr) is attained in a continuous-culture process with cell recycle using modified medium containing 0.5% cellulose. Optimum dilution rate and recycle ratio are determined as 0.025 hr-1 and 1.2, respectively, for the process. The system is analyzed and steady-state equations for predicting enzyme protein concentrations in the fermentor are developed. In fed-batch cultures, slow addition of cellulose at high concentrations can improve enzyme productivity by as much as 33% over a batch process. The scope and results of using modified medium for cellulase production are also presented.
    Additional Material: 4 Ill.
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  • 4
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 20 (1978), S. 927-935 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 5 Ill.
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  • 5
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 21 (1979), S. 1401-1420 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: High concentrations of both ethanol and sugar in the fermentation broth inhibit the growth of yeast cells and the rate of product formation. Inhibitory effects of ethanol on the yeast strain Saccharomyces cerevisiae NRRL-Y-132 were studied in batch and continuous chemostat cultures. Growth was limited by either glucose or ethanol. Feed medium was supplemented with different ethanol concentrations. Ethanol was found to inhibit growth and the activity of yeast to produce ethanol in a noncompetitive manner. A linear kinetic pattern for growth and product formation was observed according to μ = μm (1 - P/Pm) and v = vm (1 - P/Pm′), where μm is the maximum specific growth rate at P = 0 (hr-1); Pm is the maximum specific product formation rate at P = 0 (hr-1); Pm is the maximum ethanol concentration above which cells do not grow (g/liter); Pm′ is the maximum ethanol concentration above which cells do not produce ethanol (g/liter). Substrate inhibition studies were carried out using short-time experimental techniques under aerobic and anaerobic condition. The degree of substrate inhibition was found to be higher than that has been reported for ethanol fermentation of pure sugar. The kinetic relationships thus obtained were used to compute growth, substrate utilization, and alcohol production patterns and have been discussed with reference to batch and continuous fermentation of enzymatically produced bagasse hydrolysate.
    Additional Material: 16 Ill.
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  • 6
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 21 (1979), S. 1387-1400 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Rapid fermentation of bagasse hydrolysate to ethanol under anaerobic conditions by a strain of Saccharomyces cerevisiae has been studied in batch and continuous cultures at pH 4.0 and 30°C temperature with cell recycle. By using a 23.6 g/liter cell concentration, a concentation of 9.7% (w/v)ethanol was developed in a period of 6 hr. The rate of fermentation was found to increase with supplementation of yeast vitamins in the hydrolysate. In continuous culture employing cell recycle and a 0.127 v/v/m air flow rate, a cell mass concentration of 48.5 g/liter has been achieved. The maximum fermentor productivity of ethanol obtained under these conditions was 32.0 g/liter/hr, which is nearly 7.5 times higher than the normal continuous process without cell recycle and air sparging. The ethanol productivity was found to decrease linearly with ethanol concentration. Conversion of glucose in the hydrolysate to ethanol was achieved with a yield of 95 to 97% of theoretical.
    Additional Material: 9 Ill.
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  • 7
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 27 (1985), S. 1353-1361 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Significant increase in extracellular cellulase and hemicellulase activities was observed in the biosynthesis of cellulase enzyme in mixed culture fermentation of Trichoderma reesei D 1-6 and Aspergillus wentii Pt 2804 when the A. wentii inoculation was phased by 15 h. The optimal conditions of fermentation by the mixed culture have been established. Presence of mannanase has been found to affect the release as well as activity of cellulase enzyme produced in mixed culture.
    Additional Material: 8 Ill.
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  • 8
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 28 (1986), S. 972-976 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The data on ethanol-water vapor-liquid equilibrium in the presence of cellulase enzyme, nutrients, yeast, and rice straw indicated a substantial increase in ethanol concentration in vapor phase at reduced pressures. Maximum relative volatility of ethanol in the presence of added components is approximately twice that of a pure ethanol-water system. The equation correlating the activity coefficient and ethanol concentration in the liquid phase adequately represents the equilibrium behavior.
    Additional Material: 8 Ill.
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  • 9
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 30 (1987), S. 868-874 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A significant increase in extracellular xylanase activity was observed in the mixed culture fermentation of Trichoderma reesei D1-6 and Aspergillus wentii Pt 2804 when A. wentii inoculation was phased by 15 h. A. wentii produced a polysaccharide, chiefly consisting of glucose monomeric units, which was required for expression of maximum xylanase activity. Expression of high activity of xylanase in the A. wentii phased mixed culture compared to that in either T. reesei or A. wentii single cultures appeared to be controlled by the combined action of a polysaccharide produced by A. wentii and the relative growth of the two fungi in the mixed culture.
    Additional Material: 6 Ill.
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  • 10
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 33 (1989), S. 1311-1316 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bacillus amyloliquefaciens H produces a restriction endonuclease enzyme BamHl which is heat labile even at low temperatures. Studies were conducted to enhance thermal stability of BamHl using cross-linking reagents, namely, glutaraldehyde, dimethyl adipimidate (DMA), dimethyl suberimidate (DMS), and dimethyl 3,3′-dithiobispropionimidate (DTBP). Reaction with glutaraldehyde did not result in a preparation with enhanced thermal stability. However, the DMA-, DMS-, and DTBP-cross-linked preparations of BamHI exhibited significant improvement in thermal stability. Studies on thermal denaturation of the cross-linked enzyme preparations revealed that these do not follow a true first-order kinetics A possible deactivation scheme has been proposed in which the enzyme has been envisaged to go through a fully active but more susceptible transient state which, on prolonged heat exposure, exhibits a first-order decay kinetics. At 35°C, which is close to the optimum reaction temperature of 37°C for BamHl activity, the half-line of DMA-, DMS-, and DTBP-cross-linked preparations were 4.0, 5.25, and 5.5 h, respectively, whereas the native enzyme exhibited a half-line of 1.2 h only. The apparent values of deactivation rate constants for native, DMA-, DMS-, and DTBP-cross-linked BamHl were 1.13, 0.39, 0.29, and 0.26 h-1, respectively, at the same temperature, and the apparent values of activation energies for denaturation of native, DMA-, DMS-, and DTBP-cross-linked BamHl were 2.63, 5.24, 6.55, and 9.2 kcal/mol, respectively. The DTBP-cross-linked Bam HI was, therefore, the best heat-stable preparation among those tested. The unusually low values of activation energies for denaturation of Bam Hl represent their highly thermolabile nature compared to other commonly encountered enzymes such as trypsin, having activation energies of more than 40 kcal/mol for their denaturation.
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