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Consider the elementary reaction A B occurring within a given flow reactor with volume V , and fixed inlet molar flowrate of A , F

Consider the elementary reaction AB occurring within a given flow reactor with volume V,
and fixed inlet molar flowrate of A,FA0. The Damkhler number is a positive dimensionless
number given by:
Da=-rA0VFA0=initialrateofreactionforAfeedflowrateA=reactionrateconvectionrate,
and is commonly used to estimate reactor conversion with the following rule of thumb:
Da0.1xA0.1
Da>10xA>0.9
(a) Using the differential form of the PFR design equation, derive an expression for the
conversion xA in terms of the Damkhler number for a liquid-phase first order reaction,
Da1. Assume the reaction occurs as AB.
(b) Using the differential form of the design equation for a PFR again, derive a similar
expression for the conversion xA in terms of the Damkhler number for a liquid-phase
second order reaction, Da2. Assume the reaction occurs as 2AB.
(c) Suppose we have a PFR with fixed reactor volume of 0.75m3, feed molar flowrate of
FA0=1000molhr, feed volumetric flowrate Q0=4000(L)hr, and first order rate constant k1=
0.411hr. Calculate the Damkhler number for the reactor and the reactor's final conversion.
Is the conversion in line with the Damkhler number rule of thumb?
(d) Suppose the reaction proceeds with a second order mechanism instead, with a different
second-order rate constant k2=245Lmol**hr. Calculate the Damkhler number for the
reactor and the reactor's final conversion. Is the final reactor conversion in line with the
Damkhler number rule of thumb?
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