A CSTR reactor is designed for the irreversible conversion of A into B and C. The reactor is operated with a inlet volumetric flow of Q = 50 L/hr with a concentration of compound A, [A]o= 100 g/L. The first order conversion can be described by the rate equation: -TA = K[A] where k = 1.2 hr¹ is the rate constant. A. What is the inlet mass flow rate of A, FA,0? B. Write a mass balance for compound A in the system C Rewrite the rate equation to express the rate as function of degree of conversion. X

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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A CSTR reactor is designed for the irreversible conversion of A into B and C. The reactor is operated with an
inlet volumetric flow of Qo= 50 L/hr with a concentration of compound A, [A]o= 100 g/L. The first order
conversion can be described by the rate equation:
-TA = K[A]
where k = 1.2 hr¹ is the rate constant.
A. What is the inlet mass flow rate of A, FA,0?
B. Write a mass balance for compound A in the system
C. Rewrite the rate equation to express the rate as function of degree of conversion, X
Transcribed Image Text:A CSTR reactor is designed for the irreversible conversion of A into B and C. The reactor is operated with an inlet volumetric flow of Qo= 50 L/hr with a concentration of compound A, [A]o= 100 g/L. The first order conversion can be described by the rate equation: -TA = K[A] where k = 1.2 hr¹ is the rate constant. A. What is the inlet mass flow rate of A, FA,0? B. Write a mass balance for compound A in the system C. Rewrite the rate equation to express the rate as function of degree of conversion, X
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