Please help me correctly. Don't give me wrong answers. Thank you.

(100 points) A reversible liquid-phase reaction, 2AB, is to be run in one or more adiabatic reactors. The rate law for this reaction is known to be: rA=k(CA2CBB/K) Where the rate constant and equilibrium constant are given by: k=575exp(RT12000)K=14000exp(RH(T01T1)) k[=]molmincm3 where T is in K, and the enthalpy of reaction, Hrx, is given below. a) (30 points) If this reaction were run in a CSTR until a temperature of 380K, what conversion would be achieved? What volume CSTR would be required for this conversion? b) (40 points) What is the maximum conversion you could expect to get from this reaction in a single adiabatic reactor? c) (30 points) If two large reactors (large enough to reach equilibrium) and a heat exchanger capable of returning the temperature to T0 are available, what conversion could you achieve? information:CAOo=0.2mol/cm3CBB0=0Cso0=2mol/cm3(inletconcentrationofthesolvent) Mean heat capacities can be used: Cpipi=15J/mol/K Cps=20J/mol/K (heat capacity of the solvent) Hzxu(298K)=45,000J/mol Cp=0 FA0=1.5mol/min T0=305k