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Reaction 2: A2C A is fed at a rate of 100mol/s with an inert and the mole fraction of AyA0=0.36, a temperature of 150C, and

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Reaction 2: A2C A is fed at a rate of 100mol/s with an inert and the mole fraction of AyA0=0.36, a temperature of 150C, and a concentration of 0.1mol/dm3. Determine the temperature and molar flow rate profiles down the reactor. HR1A=20,000J/(mol of A reacted in reaction 1) HB2A=60,000J/(mol of A reacted in reaction 2) CPA=90J/molCk1A=10exp[RE1(3001T1)]s1CPBP=90J/mol,CE1/R=4000KCPC=180J/molCk2A=0.09exp[RE2(3001T1)]dm3/mol.sUa=4000J/m3sCE2/R=9000KTa=100C(constant) Using polymath, show all your equations, assumptions, and results. Please provide the polymath code. The following results are needed: 1. The variation of instantaneous selectivity of the desired product B to that of undesired C within the reactor length (volume). Repeat that for the yield. 2. Plot the reactor temperature and utility temperature versus reactor length (volume). 3. Plot the conversion from these reactions with reactor length (volume). 4. Plot the flowrates of all species with reactor length (volume)

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