Question: 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?
 Consider the elementary reaction AB occurring within a given flow reactor

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