100 mol/hr equimolar feed of A and B with an elementary liquid phase reversible reaction

A + B --> C centers a long pipe with diameter of 0.02 m and 150 m long. It's assumed that the first 50 m pipe segment can be modeled as CSTR and the rest of the pipe can be modeled as a PFR. The equilibrium constant Kc is 10 dm^3/mol and the forward reaction rate constant k is 0.1. Take the initail concentration of A and B = 2 mol/dm^3.

Calculate:

a) The equilibrium conversion.

b) Conversion at the exit of CSTR pipe segment and species concentrations.

c) Conversion at the exit of PFR pipe segment and species concentrations.