Dall'interno del libro
Risultati 1-3 di 55
Pagina 41
Ch . 3 ] Materials and Methods 41 In order to lessen these complications one
might try using high flow rates , but it should be realized that the flow rate from the
fermenter to the calorimetric ... We propose a method for performing this
operation .
Ch . 3 ] Materials and Methods 41 In order to lessen these complications one
might try using high flow rates , but it should be realized that the flow rate from the
fermenter to the calorimetric ... We propose a method for performing this
operation .
Pagina 47
A method is presented for converting heat production rates measured in the
calorimetric cell into enthalpy changes occurring in the fermentor . It is shown that
the log of the heat production rate is a linear function of the so - called equivalent
...
A method is presented for converting heat production rates measured in the
calorimetric cell into enthalpy changes occurring in the fermentor . It is shown that
the log of the heat production rate is a linear function of the so - called equivalent
...
Pagina 135
The first section outlines the method used for automatic control of substrate
addition ; the second examines the effect of the ... MATERIALS AND METHODS
Microorganism Candida utilis A - 49 from the Prague Research Institute of Fodder
...
The first section outlines the method used for automatic control of substrate
addition ; the second examines the effect of the ... MATERIALS AND METHODS
Microorganism Candida utilis A - 49 from the Prague Research Institute of Fodder
...
Cosa dicono le persone - Scrivi una recensione
Nessuna recensione trovata nei soliti posti.
Sommario
Stoicheiometric Aspects of Microbial Growth | 1 |
Physiological State of Continuously Grown Microbial Cultures | 31 |
Flow Microcalorimetry of the Chemostat | 40 |
Copyright | |
32 sezioni non visualizzate
Altre edizioni - Visualizza tutto
Continuous Culture 6: Applications and New Fields A. C. R. Dean,D. C. Ellwood,C. G. Evans Visualizzazione frammento - 1976 |
Parole e frasi comuni
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