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It is desired to achieve 70% conversion of the reactant A in a gas stream of pure A at 900 kPa entering a reactor with a volumetric flow rate (po) of 3 Ls1 at 300 °C. The reaction A?B follows second order rate equation: where-a rate of reaction of A, moll-s-1 CA concentration of A, moll-1 i) Initial concentration of A, Cao (in moll-) k specific rate constant, 0.30 Lmol-1s-1 Calculate: i) Initial molar flow rate of A, Fxo (in mols) ii) Volume of a CSTR, (in L). iv) Volume of PFR (in L). You may assume the gases are ideal, and pressure, temperatures remain constant throughout the reaction. [Additional data: R-8314 Jrnol-1 K-1 ]. 8.1 Integral Table dX a dX 1- X (1 tex)dx +X- (1 +EX) dX (1 +e)2x e-x ?? PROC2083 Reaction Engineering
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