The desired product C is to be produced in a well stirred reactor of 2000 dm3. Assume that volume of the mixture in the reactor remains constant and the reactor operates at steady state. The irreversible liquid phase reactions are shown below: Reaction (1) A + BC ri = k CA Reaction (2) A+ C + D 72 = kCA The liquid reactant A with a concentration of 1 mole/dm enters the reactor at 10 dm3/s. On the other hand, the reactant B is fed to the reactor in gas phase at 200 dm3/s which is bubbled up through the liquid. The partial pressure of reactant B in feed stream is 6 atm. Assume that the reactant B is completely consumed in the reaction and the flowrate of the gas stream does not change. Both reactants are supplied to the reactor at 60C and to operate the reactor under isothermal conditions at 60C it is suggested to immerse a rod in the reaction mixture. a) Draw the reactor configuration and insert all the information given in the problem. Find the concentrations of A, B, C, and D at the exit of the reactor. Additional information: R = 0.082 atm. dm3/mol.K Henry's law: C = HiPi The Henry's constant for B: 0.00233 mol B/atm. dm3 ky and k2 at 60C ki = 1.28 x 10-35-1 k2 = 2.24 x 10-4 5-1 = 30 cal/mol. K = 20 cal/mol. K CPB = 60 cal/mol. K = 35 cal/mol. K AHxn1 = -6500 cal/mol AH,xn2 = +8000 cal/mol CPA Cpc Cpp