(5 points) The elementary, gas-phase reversible reaction C6H12 + C6H6 + 3H2 takes place in an isothermal catalyst-packed membrane reactor where H2 flows out through the sides of the reactor and the transport coefficient is k2 = 0.105 s. The bulk density is 1.8 kg/dm. The specific reaction rate constant is 1.35 min-- and the equilibrium constant is 1.1 mol/dm. Pure cyclohexane enters the reactor at 12 atm and 25 C and a molar flow rate of 8.0 mol/min. Assume no pressure drop. Use the CRE Algorithm in terms of mole balances for each species and show Steps 1- 3. Use Polymath to evaluate and plot the flow rates of each chemical species and conversion (X) (can be computed based on amount of cyclohexane) along the weight of catalyst in the reactor. Now consider the reaction to occur in a PBR. Use the CRE Algorithm in terms of mole balances. Use Polymath to evaluate and plot the flow rates of each chemical species and conversion (X) along the weight of catalyst in the reactor. How does the conversion compare with the corresponding plot from the membrane reactor? What generalizations can you make? Would the conversion of cyclohexane be greater or smaller if benzene were diffusing out instead of hydrogen