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  • 1985-1989  (2)
  • 1989  (2)
Material
Years
  • 1985-1989  (2)
Year
  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 4 (1989), S. 129-138 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Heating, an old fashioned method for enzyme purification, was re-investigated as a continuous process in a jacketed tube heat exchanger. Biological, physical and process-engineering parameters were studied with regard to heating during the isolation of alcohol-dehydrogenase from cell homogenates of baker's yeast. The heat treatment served to coagulate cell debris and protein, thereby increasing not only the specific activity of the target enzyme in solution, but at the same time the particle size of the solids. The most important parameters of the process are the selected feed temperature, pH-value, volumetric flow rate and cell concentration. At optimal conditions a clear supernatant after centrifugation, (RCF 7000), is achieved containing only 50–40% of the soluble protein and 85–75% enzyme activity, resulting in a two-fold enrichment compared to the unheated crude extract. The experiments demonstrate that a continuous heating process can be applied for pre-purification and conditioning. Enzymes with better heat stability will give even higher yields.
    Type of Medium: Electronic Resource
    Library Location Call Number Volume/Issue/Year Availability
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 31 (1989), S. 215-222 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The continuous conversion of phenylglyoxylic acid to (R)-mandelic acid was performed in an enzyme membrane reactor with simultaneous coenzyme regeneration employing mandelate dehydrogenase and formate dehydrogenase. A mathematical model of the coupled enzyme reactions was formulated and applied to determine optimal conditions for (R)-mandelic acid production. The experiments and calculations showed that the optimal operational points depend strongly on enzyme kinetics. The individual kinetic parameters determined were appropriate for the description of (R)-mandelic acid production in the simultaneous two-enzyme process. Space time yields of 700 g/(l·day) were obtained at low enzyme consumption.
    Type of Medium: Electronic Resource
    Library Location Call Number Volume/Issue/Year Availability
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