In a chemostat with cell recycle has F=100 ml/h and V=1000 ml. The system is operated under glucose limitation, and. Glucose concentration in the feed S0=10 g/l. The kinetic constants of the organisms are μmax=0.25 h-1, Ks=1 g/l. The concentration factor is 1.5 and the recycle ratio (α)=0.7. The system is at steady state: a) the substrate concentration at the exit of the bioreactor b) the value of µ c) the cell concentration at the exit of the bioreactor
In a chemostat with cell recycle has F=100 ml/h and V=1000 ml. The system is operated under glucose limitation, and. Glucose concentration in the feed S0=10 g/l. The kinetic constants of the organisms are μmax=0.25 h-1, Ks=1 g/l. The concentration factor is 1.5 and the recycle ratio (α)=0.7. The system is at steady state: a) the substrate concentration at the exit of the bioreactor b) the value of µ c) the cell concentration at the exit of the bioreactor
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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In a chemostat with cell recycle has F=100 ml/h and V=1000 ml. The system is operated under glucose limitation, and. Glucose concentration in the feed S0=10 g/l. The kinetic constants of the organisms are μmax=0.25 h-1, Ks=1 g/l. The concentration factor is 1.5 and the recycle ratio (α)=0.7. The system is at steady state:
a) the substrate concentration at the exit of the bioreactor
b) the value of µ
c) the cell concentration at the exit of the bioreactor
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