In Problem 2.11 you extracted the necessary information to describe the kinetics of a simple reaction. You must now complete the design of a CFSTR in order to convert A to product D.
a. Level I and Level III analyses: Derive the mathematical model describing the CFSTR system using the constitutive relation proposed in Problem 2.3.
b. The EPA has requested that the plant reduce its emission of A by 95%. Determine the volume V of the CFSTR and associated reactor residence time required to do this, given that the feed stream is a plant purge stream of 50 g-mol of A/L (CAf) at a volumetric flow rate of qf= 100 L/min.
Problem 2.3 and 2.11
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