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Pagina 164
3 x 10 3M glycerol the inducers were added simultaneously ( 10 - 2M L -
tryptophan and 5 x 10 M methylthiogalactoside ) at 60 , 120 and 180 min in the
individual flasks . Control flasks contained a single inducer added at the same
time ...
3 x 10 3M glycerol the inducers were added simultaneously ( 10 - 2M L -
tryptophan and 5 x 10 M methylthiogalactoside ) at 60 , 120 and 180 min in the
individual flasks . Control flasks contained a single inducer added at the same
time ...
Pagina 165
The inducers ( methylthiogalactoside and L - tryptophan ) were added to the
culture separately by a feeding device to maintain a concentration of 5 . 10 3 and
10 - 2M , respectively . The rate of inducer feeding ( P ) and the concentration of ...
The inducers ( methylthiogalactoside and L - tryptophan ) were added to the
culture separately by a feeding device to maintain a concentration of 5 . 10 3 and
10 - 2M , respectively . The rate of inducer feeding ( P ) and the concentration of ...
Pagina 300
It was suggested that exclusion of the inducer by competition at the carrier level is
a more powerful control mechanism than catabolite repression and the latter may
act as a fine control on the rate of enzyme synthesis . The kinetics of mixed ...
It was suggested that exclusion of the inducer by competition at the carrier level is
a more powerful control mechanism than catabolite repression and the latter may
act as a fine control on the rate of enzyme synthesis . The kinetics of mixed ...
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Sommario
Stoicheiometric Aspects of Microbial Growth | 1 |
Physiological State of Continuously Grown Microbial Cultures | 31 |
Flow Microcalorimetry of the Chemostat | 40 |
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Continuous Culture 6: Applications and New Fields A. C. R. Dean,D. C. Ellwood,C. G. Evans Visualizzazione frammento - 1976 |
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acetate acid activity addition ammonia amount appears assimilation bacteria batch culture Biochem biomass calculated carbon source cell cellulose changes chemical chemostat coli complex concentration constant containing continuous culture decreased dehydrogenase dependent determined dilution rate effect energy source enzyme equations example experiments feed feedstock fermentation FIGURE flow formation formed function glucose glutamate glycerol growing grown growth rate higher important increased inducer initial levels limitation material maximum measured mechanism medium metabolism methanol method microbial Microbiol microorganisms mixed culture mixture mutant natural nitrogen nutrient observed obtained occur operation organisms oxygen pathway phosphate population possible present production protein References regulation relative repression Research selected showed shown similar specific activity steady strain studies substrate suggested surface synthesis Table Tank temperature Tempest tion transport units uptake utilization values wall weight yeast yield