Principles of Microbe and Cell CultivationWiley, 1975 - 274 pagine |
Dall'interno del libro
Risultati 1-3 di 34
Pagina 51
... substitute for μ2 in Eqn 6.25 by means of Eqn 6.22 and put x1 : Y ( S01-51 ) then we obtain = x2 = Y ( Da Sot D12 So1 + - D2 D02 S02-52 D2 6.26 To solve for 52 we substitute in Eqn 6.25 μ2 ELABORATIONS ON THE CHEMOSTAT 51.
... substitute for μ2 in Eqn 6.25 by means of Eqn 6.22 and put x1 : Y ( S01-51 ) then we obtain = x2 = Y ( Da Sot D12 So1 + - D2 D02 S02-52 D2 6.26 To solve for 52 we substitute in Eqn 6.25 μ2 ELABORATIONS ON THE CHEMOSTAT 51.
Pagina 213
... substitute D≈μ in Eqn 21.4 which gives s≈ DKs / ( μm - D ) 21.6 The rate of increase in the total biomass during the quasi - steady state is given by hence dx / dt = FYs , X = Xo + FYs , t 21.7 21.8 Comparing a fed batch culture in ...
... substitute D≈μ in Eqn 21.4 which gives s≈ DKs / ( μm - D ) 21.6 The rate of increase in the total biomass during the quasi - steady state is given by hence dx / dt = FYs , X = Xo + FYs , t 21.7 21.8 Comparing a fed batch culture in ...
Pagina 215
... substitute X = XmV = Xm ( Vo + Ft ) Then the total amount of product formed in time , t will be t P − P 。= xm qp ( t ) ( Vo + Ft ) dt S $ 0 Substituting , pV = P and p。V。= Po we obtain PoVoXm р = • t - Povo + xm ( q2 ( t ) ( Vo + Ft ) ...
... substitute X = XmV = Xm ( Vo + Ft ) Then the total amount of product formed in time , t will be t P − P 。= xm qp ( t ) ( Vo + Ft ) dt S $ 0 Substituting , pV = P and p。V。= Po we obtain PoVoXm р = • t - Povo + xm ( q2 ( t ) ( Vo + Ft ) ...
Sommario
Estimation of biomass | 15 |
Batch culture and plugflow culture 22 | 22 |
Chemostat culture | 29 |
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Parole e frasi comuni
acid activity amino acids amount anaerobic assumed bacteria batch culture becomes biomass biomass concentration carbon carbon dioxide causes cell chemostat culture coli colony concentration constant decrease depends determined diffusion dilution rate dissolved oxygen effect elements energy source enzyme estimated example expressed factors fermenter flow follows formation function given glucose growing growth yield growth-limiting substrate hence important increase inhibition inhibitor initial ions Klebsiella limited liquid lower mass maximum means measurement medium metabolism metal method microbial mixed mycelium nutrient obtain occur organisms output oxidation oxygen pellet phase Pirt possible present pressure range relation shown shows solution specific growth rate spore stage steady steady-state substitute substrate concentration supply synthesis Table temperature tion utilization vary volume zero