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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology letters 4 (1982), S. 347-352 
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Cell retention and ethanol production using the flocculent bacterium Zymomonas mobilis NRRL B-12526 were studied in three bioreactor configurations. The flocculent growth characteristic of this strain and a special reactor design were combined to achieve relatively high cell concentrations in a continuous bioreactor for the conversion of glucose to ethanol.
    Type of Medium: Electronic Resource
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  • 2
    ISSN: 1476-5535
    Keywords: Fermentation ; Recombinant DNA ; Phage λp L promoter ; Expression vector ; α1-Antitrypsin ; Malaria vaccine
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The major leftward early promoter of phage λp L, has frequently been used to drive expression of heterologous genes inEscherichia coli.p L is typically maintained fully repressed by the lambda cl protein. When induction of heterologous protein synthesis is desired, one of several potential mechanisms of destroying cl function is employed and the expression of the foreign gene commences. One method of derepressingp L involves exposing cells to nalidixic acid, which results in the “activation” of RecA protein and the subsequent RecA-mediated proteolytic cleavage of cl. Activated RecA also mediates the cleavage of theE. coli LexA protein, resulting in induction of the SOS regulon (at least 15E. coli genes, includingrec A). We have examined the effect of two chromosomal mutations on the productivity of nalidixic acid inductions. One of the tested mutations (recA o) increased the intracellular concentration of RecA prior to induction; the other (lexAind−) resulted in a mutated lexA protein insensitive to RecA-mediated cleavage. These mutations were introduced into a strain carrying acl+ defective lysogen. Synthesis of two heterologous proteins, human α1-antitrypsin and a fusion protein partially derived from thePlasmodium falciparum circumsporozooite surface antigen, was examined in the wild-type and mutant strains. The maximum α-1 antitrypsin concentration achieved was improved by 50% when therecA o strain was used rather than the wild type; however; only smaller changes (20% or less) in the maximum concentration of the malaria fusion protein wer observed. Use of thelexAind− strain resulted in a decrease in the maximum concentration attained for both heterologous products.
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 24 (1982), S. 595-604 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Ethanol-producing bioreactors employing cells of Zymomonas mobilis attached to glass-fiber pads were operated continuously for as long as 28 days. Ethanol production, which is related to bed-associated biomass levels, was found to occur in three distinct phases: an exponential phase, a linear phase, and a “steady-state” phase. After prolonged operation, a bacterial floc developed in the reactor. The maximum effluent ethanol concentration and the maximum volumetric productivity were 6.4% and 152 g L-1 h-1, respectively, and both were attained at a liquid residence time of from 10-15 min. Both maxima occurred after the development of the bacterial floc. The flocculant bacterium has been isolated and tentatively identified as a flocculant strain of Z. mobilis.
    Additional Material: 6 Ill.
    Type of Medium: Electronic Resource
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  • 4
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 25 (1983), S. 2399-2411 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel 2.0-L columnar reactor has been developed for the production of thienamycin by cells of Streptomyces cattleya attached to celite particles. Successful immobilization of cells was achieved by operating the column continuously at a high dilution rate during the growth phase. Scanning electron micrographs of the celite particles indicate the involvement of subcellular fibrils in the attachment of cells to the solid surfaces. Reactor operation was divided into two distinct phases-a growth phase and a production phase. The kinetics of attached growth and thienamycin production were found to be strongly influenced by nutrient concentrations. The influences of nutrient concentration on CO2 production and thienamycin production during both the growth phase and the production phase are discussed.
    Additional Material: 7 Ill.
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 28 (1986), S. 842-849 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel 2-L bubble column was used to study the continuous, immobilized cell production of thienamycin. Cells of Streptomyces cattleya were immobilized by culturing them in an appropriate growth medium containing 60/80 mesh celite particles. The dilution rate used during the continuous growth phase was 0.2 h-1. This growth phase was terminated upon the development of heavy cell films (100-500 μm thickness), and the medium was replaced with an appropriate thienamycin production medium. The system was then operated in a batch mode until thienamycin production began. At that time, continuous feeding of the production medium was initiated and the influence of medium composition and dilution rate on CO2, NH4, biomass, and thienamycin production investigated. With synthetic production medium, a doubling of the dilution rate from 0.05 to 0.10 h-1 resulted in a doubling of the thienamycin volumetric productivity. Rates of CO2 and NH4 production increased by ca. factors of three and two, respectively. The rate of PO4 utilization also doubled. When the dilution rate was decreased to 0.05 h-1, the rates of CO2 production and PO4 utilization quickly decreased (i.e., within 3 h). The rates of NH4 and thienamycin production also decreased but more slowly (i.e., ca. 100 h after the decrease in dilution rate). With complex production medium, the rates of CO2 production and PO4 utilization appeared to be a direct function of dilution rate at the dilution rates tested. Thienamycin production in this case was not a function of dilution rate. Comparing the synthetic medium with the complex medium at either dilution rate, the volumetric rate of thienamycin production was higher in the system being fed complex medium. However, the specific activity (units thienamycin/g cell/h) observed with complex medium was lower than that observed with synthetic medium. The higher volumetric productivity observed with complex medium was the result of a high cell loading. The above observations will be discussed in terms of control of thienamycin synthesis and film thickness effects.
    Additional Material: 4 Ill.
    Type of Medium: Electronic Resource
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