Please Include Excel and Matlab

Additional information: In order to determine the reaction kinetic parameters, separate independent experiments were carried out in a batch reactor where the experimental data of conversion vs. time were obtained at different temperatures as given in the following Table 1 and 2. Table 1. Experimental data for Conversion vs. time (h) obtained at different temperatures for reaction 1: 2A + B where ramol L-ih-1) = -K (T)CA. The initial CAD = 5 mol l-1 0 0.5 13.8 0 T(K) t(h) ( Conversion of A (%) 303 0.00 303 7.2 303 1 303 2 25.8 303 3 36.1 303 4 45.0 Problem statement 200 303 5 52.6 323 0 0.00 A series reaction is carried out in a semi-batch reactor and catalysed by mineral acid: 323 0.5 14.3 323 1 26.7 ki .kz 323 2 323 2ABC 46.2 323 3 3 60.6 (1) (2) OU. 323 4 4 71.1 323 5 78.8 All reactions are first order with regards to the reactant concentration. 348 0.00 The semi-batch reactor is equipped with a heat exchange jacket (UA = 126440 Jh.K) and the 348 0.5 29.1 utility temperature of 30 C 348 1 49.7 The heat of reaction for reaction 1 and 2 are AHR,1 = -27226 J/mol A and AHR,2 = 348 2 74.7 -33470 J/mol B, respectively, whereas the specific heat capacity for each component are 348 3 87.3 listed as follows: 348 4 93.6 CA = 121.8 J/mol.K; 348 5 96.8 = 244.9 J/mol.K; 373 0 0.00 373 0.5 CS = 84.8 J/mol.K; 49.6 373 1 74.6 ccatalyst = 147.5J/mol.K 373 2 93.5 373 3 98.3 Feed stream containing pure A enters the reactor at concentration of 5 mol/L, volumetric flow 373 4 99.5 rate of 200 L/h and temperature of 35 C. 373 5 99.8 Initially (at t=0), inside the reactor there is 100 L liquid containing 1 mol/L of A and 0.5 mol/L Table 2. Experimental data for Conversion vs. time (h) obtained at different temperatures for of catalyst at initial temperature of 27 C. Note that the reaction rate expression is independent reaction 2: B+C where ro (molh-) = -K (T). The initial Cho = 5 mol 1-1 of the catalyst concentration. T(K) t(h) Conversion of B (%) 303 0 Answer the questions below: 303 4.7 a. Determine the reaction kinetic parameters the each of reaction above by referring to the 303 9.1 experimental data given in Table 1 and 2. (20 marks) 303 17.4 b. Derive detailed equations for mole and energy balances for the reactor that will be solved 303 31.8 in part (c). (40 marks) 303 38.1 c. Using Matlab, solve the mole and energy balances and plot the concentrations of A, B, and 323 0 0 C as well as the reactor temperature as a function of time (from 0 to 5 hrs). What is the total 323 7.4 selectivity of B after 5 hrs of reaction? (40 marks) 323 14.3 323 26.5 323 45.9 323 53.7 348 0 348 12.1 348 22.7 348 40.3 348 64.4 348 72.4 373 0 373 18.3 373 33.1 373 55.3 373 80.1 373 86.6 0 1 2 4 8 10 0 1 2 4 8 10 0 1 2 4 8 10 0 1 2 4 8 10