1.6 The reaction is done in a liquid-phase CSTR which achieves a conversion of 20% of the B in the feed, and the final concentration of Q is 0.1mol/L. The initial concentration of A is 0.9mol/L and A and B are fed in a 1:4 ratio; the initial volumetric flowrate, v0=200L/s. If k1f=0.03 and k2=0.005 with units in L,mol and s as given in your answer for Q1.3: 1.6.1 What are the exit molar flowrates of A,B,C and Q ? 1.6.2 Calculate SC/Q 1.6.3 What are the exit concentration of A,B and C ? List your assumptions 1.6.4 Calculate k1r. [12] 1.6 The reaction is done in a liquid-phase CSTR which achieves a conversion of 20% of the B in the feed, and the final concentration of Q is 0.1mol/L. The initial concentration of A is 0.9mol/L and A and B are fed in a 1:4 ratio; the initial volumetric flowrate, v0=200L/s. If k1f=0.03 and k2=0.005 with units in L,mol and s as given in your answer for Q1.3: 1.6.1 What are the exit molar flowrates of A,B,C and Q ? 1.6.2 Calculate SC/Q 1.6.3 What are the exit concentration of A,B and C ? List your assumptions 1.6.4 Calculate k1r. [12]