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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 50 (1996), S. 145-150 
    ISSN: 0006-3592
    Keywords: high-pressure homogenization ; cell disruption ; cell size distribution ; simulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Measurements of size distributions are provided for the breakage of commercial packed bakers' yeast cells as a function of operating pressure and number of passes through a Manton Gaulin high-pressure homogenizer. A two parameter model was developed, based upon the use of a Boltzmann function, to simulate the changes in size distribution that accompany the cell breakage process. The effects of operating pressure and number of passes are incorporated in the model and the result is used to simulate the particle size distribution of the cell homogenate. The results show that there is little breakage below a threshold pressure of 115 bar and above which breakage is critically dependent upon the pressure and number of passes through the homogenizer. The analysis provides a means of studying the efficiency of centrifugation that may follow cell disruption and provides the basis for further studies of size distribution changes accompanying cell disruption. © 1996 John Wiley & Sons, Inc.
    Additional Material: 6 Ill.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 58 (1998), S. 453-463 
    ISSN: 0006-3592
    Keywords: Saccharopolyspora erythraea ; airlift reactor ; propeller ; heterogeneity ; cycling dissolved oxygen tension ; hydrodynamics ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bioreactor heterogeneity has been studied in a multiconfigurable pilot-scale airlift reactor (0.25 m3) which created different degrees of heterogeneity. The impact of the two sparger configurations, i.e. in the draft tube or the annulus, in conjunction with a marine propeller fitted at the base of the downcomer, on the physiology of Saccharopolyspora erythraea was studied. Cellular growth, morphology, and productivity were compared between airlift and stirred tank reactors. Dissolved oxygen tension heterogeneity caused by differences in dissolved oxygen tension around the vessel did not affect growth, but the reduction of heterogeneity improved the specific erythromycin production rate and final specific production. Erythromycin production was shown to be proportional to the energy dissipation rate. The enhancement of bubble coalescence with increasing apparent viscosity led to the reduction of the sectional gas holdups and the improvement of liquid mixing. The extent of the changes with increasing apparent viscosity was dependent on the broth morphology, reactor configurations, and operating conditions. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58: 453-463, 1998.
    Additional Material: 9 Ill.
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 45 (1995), S. 80-85 
    ISSN: 0006-3592
    Keywords: rheology ; morphology ; actinomycete ; Saccharopolyspora erythraea ; Actinomadura roseorufa ; Streptomyces rimosus ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The broth rheologies and morphologies of three actinomycetes (Saccharopolyspora erythraea, Actinomadura roseorufa, and Streptomyces rimosus) in submerged culture have been examined. The rheology of all the broths became pseudoplastic as soon as significant growth occurred with the power law index, n, falling to 0.20 to 0.25. The consistency index, K, rose with biomass concentration although in some instances it fell later in the fermentation. The mean main hyphal lengths of all cultures were in the range, 15 to 25 μm, and did not alter greatly even when large changes in K were occurring. © 1995 John Wiley & Sons, Inc.
    Additional Material: 9 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 60 (1998), S. 768-770 
    ISSN: 0006-3592
    Keywords: SDS-alkaline lysis process ; lysis reaction time ; chromosomal DNA denaturation ; shear damage of DNA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: SDS-alkaline lysis of recombinant Escherichia coli cell suspensions was carried out in a coaxial cylinder rheometer, and the data were used to establish the time course of lysis reaction. The results of the experiments showed that cell lysis reaction time depended on cell strain but was unaffected by plasmid size and plasmid copy number. The high molecular weight globular proteins and chromosomal DNA were denatured, and the resulting changes in rheometric measurements characterised the denaturation time. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 768-770, 1998.
    Additional Material: 2 Ill.
    Type of Medium: Electronic Resource
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