SOLVE PART D ONLY!!!!!!!!

P4-5A Set up a stoichiometric table for each of the following reactions and express the concentration of each species in the reaction as a function of conversion, evaluating all constants (e.g., = =). Next, assume the reaction follows an elementary rate law, and write the reaction rate solely as a function of conversion, that is, -ra = f(x). a. For the liquid-phase reaction CH-OH CH2-CH,+H,0 H2SO4, CH, OH the entering concentrations of ethylene oxide and water, after mixing the inlet streams, are 16.13 and 55.5 mol/dm", respectively. The specific reaction rate is k = 0.1 dm /mols at 300 K with E = 12500 cal/mol. 1. After finding ra =f(X), calculate the CSTR space-time, t, for 90% conversion at 300 K and also at 350 K. 2. If the volumetric flow rate is 200 liters per second, what are the corresponding reactor volumes? (Ans: At 300 K: V=439 dm' and at 350 K: V = 22 dm) b. For the isothermal gas-phase pyrolysis C2H6 CH4 = H2 pure ethane enters a flow reactor at 6 atm and 1100 K, with AP = 0. Set up a stoichiometric table and then write --A = (X). How would your equation for the concentration and reaction rate, that is, -ra =f(x), change if the reaction were to be carried out in a constant-volume batch reactor? c. For the isothermal, isobaric, catalytic gas-phase oxidation cream C2H4+02 -CH-CH2 the feed enters a PBR at 6 atm and 260C, and is a stoichiometric mixture of only oxygen and ethylene. Set up a stoichiometric table and then writer as a function of partial pressures. Express the partial pressures and r as a function of conversion for (1) a fluidized batch reactor and (2) a PBR. Finally, write - r solely as a function of the rate constant and conversion. d. Set up a stoichiometric table for the isothermal catalytic gas-phase reaction carried out in a fluidized CSTR. + 2H2 Fluidized catalyst pellets d. Set up a stoichiometric table for the isothermal, catalytic gas-phase reaction carried out in a fluidized CSTR. +2H2 Fluidized catalyst pallets Fluidized CSTR = The feed is stoichiometric and enters at 6 atm and 170C. What catalyst weight is required to reach 80% conversion in a fluidized CSTR at 170C and at 270C? The rate constant is defined with respect to benzene and Vo = 50 dm3/min. 53 mol kg at 300 K with E = 80 kJ/mol 3 kgcat.min.atm First write the rate law in terms of partial pressures and then express the rate law as a function of conversion. Assume AP = 0. =