Solve polymath /matlab also Solve complete and correctly I will give you thumb up

P4-22 B Alkylated cyclohexanols are important intermediates in the fragrance and perfume industry [Ind. Eng. Chem. Res., 28, 693 (1989)]. Recent work has focused on gas-phase catalyzed hydrogenation of o-cresol to 2-methylcyclohexanone, which is then hydrogenated to 2-methylcyclohexanol. In this problem we focus on only the first step in the reaction (Figure P4-22). The reaction on a nickel-silica catalyst was found to be zero-order in o-cresol and first-order in hydrogen with a specific reaction rate at 170C of 1.74mol of o-cresol /(kg cat minatm). The reaction mixture enters the packed-bed reactor at a total pressure of 5atm. The molar feed consists of 67%H2 and 33% o-cresol at a total molar rate of 40mol/min. Figure P4-22 (a) Neglecting pressure drop, plot the rate of reaction of o-cresol and the concentrations of each species as a function of catalyst weight. What is the ratio of catalyst weight needed to achieve the last 5% conversion to the weight necessary to achieve the first 5% conversion ( 0 to 5% ) in the plug-flow reactor? (b) Accounting for the pressure drop in the packed bed using a value of =0.034kg1, redo part (a) along with a plot of pressure versus catalyst weight. 1. A document containing the derivation of differential equations, solution graphs as required in question 4.22B. The values used by each member must be indicated clearly. 2. Polymath/MATLAB files. No need to write a separate full report. The textbook question 4.22B is presented below for your reference