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Product inhibition in packed-bed immobilized enzyme reactors for complex processes: Modelling of two-substrate processes
Authors:S Guzy  N Lotan
Institution:(1) Department of Biomedical Engineering, Technion-Israel Institute of Technology, 32000 Haifa, Israel
Abstract:An analytical model was developed for describing the performance of packed-bed enzymic reactors operating with two cosubstrates, and when one of the reaction products is inhibitory to the enzyme. To this aim, the compartmental analysis technique was used. The relevant equations obtained were solved numerically, and the effect of the main operational parameters on the reactor characteristics were studied.Notation C infa,i sup* local concentration of products in the pores of stage i - C j,i concentration of substrate j in the pores of stage i - D infa sup* internal (pore) diffusion coefficient for the reaction product a - D j internal (pore) diffusion coefficient of substrate j - J infa,i sup* net flux of product a, taking place from the pores of stage i into the corresponding bulk phase - J j,i net flux of substrate j, taking place from the bulk phase of stage i into the corresponding pores - K b inhibition constant - K m,1, K m,2 Michaelis constants for substrate 1 and 2, respectively - K q inhibition constant - n total number of elementary stages in the reactor - Q volumetric flow rate throughout the reactor - R j,i, R infa,i sup* local reaction rates in pores of stage i, in terms of concentration of substrate j and product a respectively - S infa,i sup* , S infa,i-1 sup* bulk concentration of the reaction product a, in the stages i and i — 1, respectively - S j,0 concentration of substrate j in the reactor feed - S j,i-1, S j,i concentration of substrate j in the bulk phase leaving stages i — 1 and i, respectively - V total volume of the reactor - V m maximal reaction rate in terms of volumetric units - y axial coordinate of the pores - y 0 depth of the pores - agr * dimensionless parameter, defined in Equation (22) - agr 1 dimensionless parameter, defined in Equation (6) - agr 2 dimensionless parameter, defined in Equation (6) - beta 1 dimensionless parameter, defined in Equation (6) - beta 2 dimensionless parameter, defined in Equation (6) - ngr * dimensionless parameter, defined in Equation (22) - ngr 1 dimensionless parameter, defined in Equation (6) - ngr 2 dimensionless parameter, defined in Equation (6) - theta * dimensionless parameter, defined in Equation (22) - epsi * dimensionless parameter, defined in Equation (22) - rhov volumetric packing density of catalytic particles (dimensionless) - phgr porosity of the catalytic particles (dimensionless) - lambdaV infi sup* dimensionless concentration of reaction product in pores of stage i, defined in Equation (17) - lambdaj,i dimensionless concentration of substrate j in pores of stage i; defined in Equation (6) - psgr j,i-1, psgr j.i dimensionless concentration of substrate j in the bulk phase of stage i; defined in Equation (6) - xgr dimensionless position along the pore; defined in Equation (6)
Keywords:Bioreactors  enzyme  two-substrate  inhibition
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