By Professor Dr. Anton Moser (auth.)
This ebook relies on a 1981 German language variation released via Springer Verlag, Vienna, less than the identify Bioprozesstechnik. Philip Manor has performed the interpretation, for which i'm deeply thankful. This publication differs from the German version in lots of methods in addition to language. it really is considerably enlargened and up to date, and examples of desktop simula tions were further including different appendices to make the paintings either extra entire and more effective. This ebook is the results of over 15 years of expertise in educating and study. It stems from lectures that i started in 1970 on the Technical collage of Graz, Austria, and endured on the collage of Western Ontario in London, Canada, 1980; on the unfastened college of Brussels, 1981; at Chalmers Technical collage in G6teborg, Sweden; on the Academy of Sciences in lena, East Germany; on the "Haus der Technik" in Essen, West Germany, 1982; on the Academy of technology in Sofia, Bulgaria; and on the Technical collage of Delft, Netherlands, 1986. the most pursuits of this booklet are, first, to bridge the space that usually exists among easy rules and utilized engineering perform, moment, to augment the combination among organic and actual phenomena, and, 3rd, to give a contribution to the interior improvement of the sphere of biotechnology through describing the process-oriented box of bioprocess technology.
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Additional info for Bioprocess Technology: Kinetics and Reactors
And theoretical limits of the efficiency (Roels, 1980a. ). 8. Relationship between substrate yield factor Y~ls and substrate degree of reduction Ys, and the theoretical limits to Y~IS (Roels, 1980a. ). 7 00 0 8 ... __ ~ 0 0 8 0 -" 0 ~ ~ I ,J" ct' 0 5 )Is where the maximum value of the yield is calculated in full accordance with the second law. This equation has been used in the analysis of some recent yield data from the literature. The data are presented graphically in Fig. 7: The thermodynamic efficiency 11th is plotted against the degree of reduction Ys of the substrate for growth, with NH3 as a nitrogen source.
18 are the same, their status in terms of the system's description is totally different. Equ. 18 is a macroscopic balance equation concerning the flow of substrate entering the microbial system. Equ. 17 is a microscopic assumption about the internal functioning of the regulation of the energy transformation processes in the cell, describing the fate of the energy carrier ATP (Roels, 1980b). Stouthamer and Bettenhaussen (1973) pointed out that the effect of maintenance energy on YATP has been underestimated, and it is one factor responsible for the wide range of YATP values found (5-32 g dry biomass per mole ATP, depending on the nature of the carbon).
1 shows the correspondence between the various technologies of bioprocessing and the containers in which the reactions are carried out on an engineering scale. These "bioreactors" range from sterilizers to proper bioreactors (microbiological reactors such as fermenters, waste water treatment units, vessels for cultivation of plant & animal cells, enzyme reactors) to miscellaneous containers such as bottles, barrels, and so on used primarily for carrying out "arts and crafts"-type complex biological processes.
Bioprocess Technology: Kinetics and Reactors by Professor Dr. Anton Moser (auth.)