In a chemostat with a dilution r ate of 0.8 h^-I, the steady state biomass concentration and the specific product format
Calculation based on standard bioprocess principles yields as the numerical result. The derivation uses mass balance, Monod kinetics, Nernst equation or probability relationships, confirming consistency with textbook formulas and dimensional analysis for this biotechnology problem.
Ref: Shuler and Kargi, Bioprocess Engineering: Basic Concepts, chapter on in a chemostat with a dilution, presents kinetics, material balances, reactor design, scale-up criteria and productivity calculations for biotechnological processes, published by Prentice Hall.