i would like solution with EES application. this example is in element of chemical reaction engineering 4th edition

Example 10-6 Catalyst Decay in a Fluidized Bed Modeled as a CSTR The gas-phase cracking reaction Gasoil(g)AProducts(g)B+C + For simplicity, gas oil is used to represent the reactive portion of the feed. In actuality. gas oil. distilled from crudc, is made up of complex hydrocarbons, which can be cracked. and simple hydrocarbons, which will not crack and are therefore inert in this application. 718 Catalysis and Catalytic Reactors Chap. 10 is carried out in a fluidized CSTR reactor. The feed stream contains 80% crude (A) and 20% inert I. The crude oil contains sulfur compounds, which poison the catalyst. As a first approximation we will assume that the cracking reaction is first order in the crude oil concentration. The rate of catalyst decay is first order in the present activity, and first order in the reactant concentration. Assuming that the bed can be modeled as a well-mixed CSTR, determine the reactant concentration, activity, and conversion as a function of time. The volumetric feed rate to the reactor is 5000m3/h. There are 50.000kg of catalyst in the reactor and the bulk density is 500kg/m3. Additional information: CA0=0.8mol/dm3CTO=1.0mol/dm3k=Bk=45h1kd=9dm3/molh