Reaction engineering Question StatementEthylbenzene is a widely used industrial chemical. It is often found in othermanufactured products such as pesticides, inks, synthetic rubbers, paints, and tobaccoproducts. Global consumption of ethylbenzene is estimated to grow up to 5% per yearfor the next 5 years, with the escalation of growth mainly contributed by the recoveryprocess from the steep decline due to the impact of Covid-19 global pandemic circa2020. It is expected that the global ethylbenzene market will reach 40.2 million tons by2027. Due to the market potential of ethylbenzene, a chemical company, ChemMajuSdn. Bhd. is planning to expand its production by producing ethylbenzene as one of itsmajor products.At industrial scale, ethylbenzene is produced via various production routes. Themost widely known route is the alkylation of ethylene (AEO). Since alkylation ofethylene is an established process, as a beginner in ethylbenzene production inMalaysia, ChemMaju Sdn. Bhd. is planning to produce ethylbenzene via this route. Theproduction capacity is expected to be around 40, 000 MTPA of ethylbenzene. AlthoughAEO is an established process, it has a drawback in which the production ofethylbenzene is accompanied by the production of styrene as an undesired product:C6H5CH3 + 2 C2H4 → C6H5C2H5 + C3H6(Equation 1 - Main reaction)C6H5C2H5C3H8 + H2(Equation 2 - Side reaction)As the lead process engineer in ChemMaju Sdn. Bhd., you are given the task to designof an ethylbenzene production plant. Your first step is to lead your team in designingthe reactor for the alkylation of ethylene process. In orderto use a non-catalytic, adiabatic flow reactor. Since the reaction is non-catalytic, theprocess should be a thermal process to ensure its thermodynamic feasibility, withminimum required inlet reaction temperature of 227 °C. The homogeneous reaction isin gas phase, with constant total pressure of 7.5 atm. The reaction of the reactants is1:2 (toluene: ethylene) based on stoichiometric ratio. However, the feed is 1:4 (toluene:ethylene), making it insufficient toluene to consume all the ethylene. Therefore, tolueneis the limiting reactant for the basis of calculation.save cost, you proposed Task 2Aside from designing a new reactor, you are also planning to repurpose an unusedCSTR(VCSTR = 4.3 m) that has been placed in the maintenance warehouse for far toolong. The repurposing of this CSTR would save a huge cost for your company if it isproven that the CcSTR is suitable for the non-catalytic, adiabatic alkylation of ethyleneprocess. Assess the suitability of this unused CSTR for the process by conductingdetailed design calculation and analysis and compare its feasibility for the thermalalkylation of ethylene process with the reactor selected in Task 1.Note:1) Assume that side reaction is negligible.2) For Task 2, assume that the reaction of order is 2nd order of reaction withrespect to toluene and zero order of reaction with respect to ethylene.3) Use the same rate constant as the one used in Task 1.4) Given that the root equation of X;2(tkCA0 + 1)(To/T)² – /4tkCA0(To/T)² + 12(tkCA0) (To/T)2

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Given :Reactions areC6H5CH3+2C2H4  →  C6H5C2H5+C3H6C6H5C2H5  →  C8H8+H2The elementary rate law is…