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is carried out isothermally in a continuous flow reactor. Calculate both the CSTR and the PFR reactor volumes (if it is possible) necessary to consurme 96% of S (ie. S = 0.04 *S) when the entering volumetric flow rate is at a constant 12 L/hr. Assume the reaction rate -s follows normal Michaelis-Menten kinetics (the product formation step is slow and rate limiting) where the substrate binds with the enzyme to form complex ES. Assume that there is no immobilization or inhibition effects present. a. So-1.5 mol/L and Vmax-4.50 mol/(hr L) and Km- 0.0300 mol/L b. S,-0.030 mol/L and Vmax = 0.10 mol/(hr*L) and Km = 0.095 mol/L c. So= 0.90 mol/L and Vmax 0.10 mol/(hr*L) and Km = 0.0750 mol/L lfitismotpossibletodetermine thereactor vol esforthedata given above, l tthe remai ingvariables that are needed to determine the reactor volumes.

is carried out isothermally in a continuous flow reactor. Calculate both the CSTR and the PFR reactor volumes (if it is possible) necessary to consurme 96% of S (ie. S = 0.04 *S) when the entering volumetric flow rate is at a constant 12 L/hr. Assume the reaction rate -s follows normal Michaelis-Menten kinetics (the product formation step is slow and rate limiting) where the substrate binds with the enzyme to form complex ES. Assume that there is no immobilization or inhibition effects present. a. So-1.5 mol/L and Vmax-4.50 mol/(hr L) and Km- 0.0300 mol/L b. S,-0.030 mol/L and Vmax = 0.10 mol/(hr*L) and Km = 0.095 mol/L c. So= 0.90 mol/L and Vmax 0.10 mol/(hr*L) and Km = 0.0750 mol/L lfitismotpossibletodetermine thereactor vol esforthedata given above, l tthe remai ingvariables that are needed to determine the reactor volumes.

Introduction to Chemical Engineering Thermodynamics
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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is carried out isothermally in a continuous flow reactor. Calculate both the CSTR and the PFR reactor volumes (if it is possible) necessary to consurme 96% of S (ie. S = 0.04 *S) when the entering volumetric flow rate is at a constant 12 L/hr. Assume the reaction rate -s follows normal Michaelis-Menten kinetics (the product formation step is slow and rate limiting) where the substrate binds with the enzyme to form complex ES. Assume that there is no immobilization or inhibition effects present. a. So-1.5 mol/L and Vmax-4.50 mol/(hr L) and Km- 0.0300 mol/L b. S,-0.030 mol/L and Vmax = 0.10 mol/(hr*L) and Km = 0.095 mol/L c. So= 0.90 mol/L and Vmax 0.10 mol/(hr*L) and Km = 0.0750 mol/L lfitismotpossibletodetermine thereactor vol esforthedata given above, l tthe remai ingvariables that are needed to determine the reactor volumes.
Transcribed Image Text:is carried out isothermally in a continuous flow reactor. Calculate both the CSTR and the PFR reactor volumes (if it is possible) necessary to consurme 96% of S (ie. S = 0.04 *S) when the entering volumetric flow rate is at a constant 12 L/hr. Assume the reaction rate -s follows normal Michaelis-Menten kinetics (the product formation step is slow and rate limiting) where the substrate binds with the enzyme to form complex ES. Assume that there is no immobilization or inhibition effects present. a. So-1.5 mol/L and Vmax-4.50 mol/(hr L) and Km- 0.0300 mol/L b. S,-0.030 mol/L and Vmax = 0.10 mol/(hr*L) and Km = 0.095 mol/L c. So= 0.90 mol/L and Vmax 0.10 mol/(hr*L) and Km = 0.0750 mol/L lfitismotpossibletodetermine thereactor vol esforthedata given above, l tthe remai ingvariables that are needed to determine the reactor volumes.
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