An approximate solution for a transient two-phase stirred tank bioreactor with nonlinear kinetics.
The derivation of an approximate solution method for models of a continuous stirred tank bioreactor where the reaction takes place in pellets suspended in a well-mixed fluid is presented. It is assumed that the reaction follows a Michaelis-Menten-type kinetics. Analytic solution of the differential equations is obtained by expanding the reaction rate expression at pellet surface concentration using Taylor series. The concept of a pellet's dead zone is incorporated; improving the predictions and avoiding negative values of the reagent concentration. The results include the concentration expressions obtained for (a) the steady state, (b) the transient case, imposing the quasi-steady-state assumption for the pellet equation, and (c) the complete solution of the approximate transient problem. The convenience of the approximate method is assessed by comparison of the predictions with the ones obtained from the numerical solution of the original problem. The differences are in general quite acceptable.
Valdés-Parada
Francisco J
FJ
Universidad Autónoma Metropolitana-Iztapalapa, Av. San Rafael Atlixco 186 Col. Vicentina, México D.F., México, C.P. 09340.
Alvarez-Ramírez
José
J
Ochoa-Tapia
J Alberto
JA
D019149:Bioreactors; D045424:Complex Mixtures / Q000737:chemistry*; D003198:Computer Simulation; D004800:Enzymes, Immobilized / Q000737:chemistry*; D019544:Equipment Failure Analysis / Q000379:methods*; D007700:Kinetics; D044085:Microfluidics / Q000379:methods*; D008956:Models, Chemical; D017711:Nonlinear Dynamics; D013997:Time Factors
D045424:Complex Mixtures; D004800:Enzymes, Immobilized