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Pseudo steady states were not reached because the average cellulose
concentration in each of the 20 % draw - off cycles continued to fall . Also , since
the biomass continued to drop , it would appear that productivity had not been
optimized .
Pseudo steady states were not reached because the average cellulose
concentration in each of the 20 % draw - off cycles continued to fall . Also , since
the biomass continued to drop , it would appear that productivity had not been
optimized .
Pagina 334
RESULTS The experiment was started with the inoculation of a swiple of river
sediment into Tank A . Up to the end of the second day the bacterial biomass
increased rapidly , not only in the planktonic phase but also in the periphyton in
all of ...
RESULTS The experiment was started with the inoculation of a swiple of river
sediment into Tank A . Up to the end of the second day the bacterial biomass
increased rapidly , not only in the planktonic phase but also in the periphyton in
all of ...
Pagina 335
Ch . 25 ] Biomass Changes 335 Tank A Tank B Volume biomass ( mm . 10° / ml )
Tank C Volume biomass ( mm . 10 * 1 cm ? ) 4 . Time ( days ) FIGURE 3 .
Biomass of bacteria suspended ( filled circles ) and attached ( empty circles ) .
The right ...
Ch . 25 ] Biomass Changes 335 Tank A Tank B Volume biomass ( mm . 10° / ml )
Tank C Volume biomass ( mm . 10 * 1 cm ? ) 4 . Time ( days ) FIGURE 3 .
Biomass of bacteria suspended ( filled circles ) and attached ( empty circles ) .
The right ...
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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