solve it using polymath only no hand writing the part { i }

Problem 3 We want to simulate a gas phase reaction in a packed bed reactor using a silica alumina catalyst. The reaction can be assumed to be like the following - 2AB+C (reversible reaction) [a] Urite the mole balance? reaction rate constant, k1 [b] Write the rate law in terms of partial pressure? =4.25106atm2gmcat.smol and Ke=2.5 [c] Setup a Stoichiometric table fo this reaction. The molar flow rate into the packed bed reactor is 23.6mol/s [d] Write the partial pressure i terms of conversion. and the entering pressure is 18atm. (careful with the unit of k1 ) [e] Write the rate law in ermsof conversion only. Assume there is no pressure drop or temperature change in the [f] What is the equinbrium conversion Xe ? reactor. [g] How mapy kilograms of catalyst you will need to have a cenversion 90% of Xe in a packed bed regctor? [h] How many kilograms of catalyst you will need to have a conversion 90% of Xe in a fluidized bed reactor? [i] What conversion would be achieved if you use a packed bed reactor with 100kg catalyst with a pressure drop parameter =0.0098kg1. At what catalyst wt the pressure drop falls below 1atm ? [Use polymath]