A <----> 2B (gas phase, elementary, reversible, isothermal) carried out in flow reactor. Pure A fed at 5 mol/L, volumetric flow rate 3 L/min. K1 (forward rate const.) = 8 1/min, Kc (eqil. conts) = 60 mol/ L. (i) Find the rate law only in terms if X (conversion) (ii) Find out the Xe (equil. conversion at this temp). (iii) What is the volume needed if we use a CSTR and want to achieve 60% Xe (Equil. conversion).
A <----> 2B (gas phase, elementary, reversible, isothermal) carried out in flow reactor. Pure A fed at 5 mol/L, volumetric flow rate 3 L/min. K1 (forward rate const.) = 8 1/min, Kc (eqil. conts) = 60 mol/ L. (i) Find the rate law only in terms if X (conversion) (ii) Find out the Xe (equil. conversion at this temp). (iii) What is the volume needed if we use a CSTR and want to achieve 60% Xe (Equil. conversion).
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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A <----> 2B (gas phase, elementary, reversible, isothermal) carried out in flow reactor. Pure A fed at 5 mol/L, volumetric flow rate 3 L/min. K1 (forward rate const.) = 8 1/min, Kc (eqil. conts) = 60 mol/ L.
(i) Find the rate law only in terms if X (conversion)
(ii) Find out the Xe (equil. conversion at this temp).
(iii) What is the volume needed if we use a CSTR and want to achieve 60% Xe (Equil. conversion).
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