Q1) 100mol/hr equimolar feed of A and B with an elementary liquid phase teversible reaction A+BC enters a long pipe with diameter of 0,02m and 150m long. It is issumed 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/mol and the forward reaction rate constant k is 0.1. Take the initial concentrations of A and B2 mol/dm? 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)