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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology letters 2 (1980), S. 315-320 
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary A controlled shift down of the specific growth rate in a fed batch culture is proposed for microbial product formation processes. The growth kinetics depend on three preset parameters: initial biomass concentration, initial specific growth rate, and the transient constant (time derivative of the specific growth rate). An experimental example is given.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Combustion, explosion and shock waves 16 (1980), S. 212-214 
    ISSN: 1573-8345
    Source: Springer Online Journal Archives 1860-2000
    Topics: Energy, Environment Protection, Nuclear Power Engineering , Mechanical Engineering, Materials Science, Production Engineering, Mining and Metallurgy, Traffic Engineering, Precision Mechanics
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 23 (1981), S. 1563-1572 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: By investigation of a model of benzylpenicillin fermentation it was demonstrated that high fermentation productivity is connected with low stability. The increasing instability is not the result of external disturbances but of peculiarities inherent to the system. The main process variables and the essential parameters were selected by analysis of data obtained from fermentation runs in a pilot plant. By simulation on an analog computer it was shown that the proposed model gives a sufficient description of the kinetic behavior of the fermentation runs. By varying the initial conditions it was possible to obtain two types of fermentation runs. One type is distinguished by a high productivity connected with low initial concentrations of sucrose. An increase of the initial sucrose concentration also causes an increase of productivity. When a certain value of this concentration is exceeded a changeover to a faster growth of biomass takes place combined with the breakdown of productivity. The same phenomenon occurs at a defined initial concentration of sucrose if a disturbance of oxygen transfer rate takes place. Whether the culture stays in the one or in the other state after the disturbance has passed depends on the duration, the strength, and the beginning of the disturbance. In the pilot plant similar behavior can be observed. The sensitivity of fermentation processes to disturbances increases with the increase of productivity.
    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 23 (1981), S. 2771-2777 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The optimal substrate profile is calculated by Pontryagin's maximum principle for a simplified mathematical model of microbial growth and product formation. This model is fitted to experimental data of turimycin fermentation. Sub optimal control is studied for comparison.
    Additional Material: 4 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 24 (1982), S. 2129-2136 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: For a simple mathematical model of microbial product formation, the productivities of stationary and nonstationary cultivation methods (chemostat and cyclic batch) are compared. Conditions of superiority of the cyclic batch cultivation are characterized. The model includes substrate inhibition of the product formation and the age-dependent loss of productivity of the culture.
    Additional Material: 5 Ill.
    Type of Medium: Electronic Resource
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