P4-5 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 (0.g... C). Next, assume the reaction follows an elementary rate law, and write the reaction rate solely as a function of conver- sion, i.e., -- - f. (a) For the liquid-phase reaction CH2-OH CH, CH, HO H2SO4 CH, OH the entering concentrations of @thylene oxide and water, after mixing the inlet streams, are 16.13 mol/dm, and 55.5 mol/dmy, respectively. The specific reaction rate isk-0.1 dm,/mol.s at 300 K with E. 12,500 cal/mol. (1) After finding -- = 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 vol- umes? (Ans.: At 300 K: V - 439 dm, and at 350 K: V = 22 dm) (a) Set up a stoichiometric table for the isothermal, catalytic gas-phase reaction carried out in a flu- idized CSTR. 2H2 dir + 2H2 || U Fluidized catalyet pollers 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 u = 50 dm3/min. kg 53 mol 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