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 hr* is the rate constant. D. Plot Fao /-Ta Vs. degree of conversion, in the range 0< X < 0.9. Which reactor volume is needed for X = 0.75?

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Chapter13: Rates Of Reaction
Section13.5: Temperature And Rate; Collision And Transisiton-state Theories
Problem 13.5CC: Consider the following potential-energy curves for two different reactions: a. Which reaction has a...
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Problem 3
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 hr* is the rate constant.
D. Plot Fa,0 /-ra vs. degree of conversion, in the range 0 < X < 0.9. Which reactor volume is needed for X
= 0.75?
Transcribed Image Text:Problem 3 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 hr* is the rate constant. D. Plot Fa,0 /-ra vs. degree of conversion, in the range 0 < X < 0.9. Which reactor volume is needed for X = 0.75?
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