Q1) 100mol/hr equimolar feed of A and B with an elementary liquid phase reversible reaction A+BC enters a long pipe with diameter of 0.02m and 150m long. It is assumed that the first 50m pipe segment can be modeled as CSTR and the rest of the pipe can be modeled as PFR. The equilibrium constant, KC, is 10dm3/moland ane forward reaction rate constant k is 0.1. Take the initial concentrations of A and B2 mol/dm3 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 ( 40 pts)