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The two liquid phase reactions are taking place in a semi batch reactor. Pure feed of A with concentration 0.5- mol is fed to B at volumetric flow rate of 12 L/min. The rates of the two reactions are listed below. The initial volume of B in the reactor is 500 L and the concentration mol of B is 2 The maximum volume of the reactor is 5000 L. 12 i. A+B 2C, -n = K1ACA CB ,kA = 5 min mol2 ii. A + 3C D, -r, = K24CA Cc, k2A = 10 %3D min mol3 a) Derive the set of mole balances ODES of N, Ng, Ne, Np as a function of time using feed concentration CA0, feed volumetric flow rate vo, initial volume Vo, rate constants kA, k2A, and time t.

The two liquid phase reactions are taking place in a semi batch reactor. Pure feed of A with concentration 0.5- mol is fed to B at volumetric flow rate of 12 L/min. The rates of the two reactions are listed below. The initial volume of B in the reactor is 500 L and the concentration mol of B is 2 The maximum volume of the reactor is 5000 L. 12 i. A+B 2C, -n = K1ACA CB ,kA = 5 min mol2 ii. A + 3C D, -r, = K24CA Cc, k2A = 10 %3D min mol3 a) Derive the set of mole balances ODES of N, Ng, Ne, Np as a function of time using feed concentration CA0, feed volumetric flow rate vo, initial volume Vo, rate constants kA, k2A, and time t.

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
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1. The two liquid phase reactions are taking place in a semi batch reactor. Pure feed of A with mol is fed to B at volumetric flow rate of 12 L/min. The rates of the two concentration 0.5 reactions are listed below. The initial volume of B in the reactor is 500 L and the concentration of B is 2 mol The maximum volume of the reactor is 5000 L. A + B 2C, -r, = k1ACA CB,kA = 5 L2 i. min mol2 ii. A +3C D, -r, = K24CA Cc, k24 = 10- %3D min mol3 a) Derive the set of mole balances ODES of Na, Ng, Ne, N, as a function of time using feed concentration Ca0, feed volumetric flow rate v,, initial volume Vo, rate constants kA, k2A, and time t.
Transcribed Image Text:1. The two liquid phase reactions are taking place in a semi batch reactor. Pure feed of A with mol is fed to B at volumetric flow rate of 12 L/min. The rates of the two concentration 0.5 reactions are listed below. The initial volume of B in the reactor is 500 L and the concentration of B is 2 mol The maximum volume of the reactor is 5000 L. A + B 2C, -r, = k1ACA CB,kA = 5 L2 i. min mol2 ii. A +3C D, -r, = K24CA Cc, k24 = 10- %3D min mol3 a) Derive the set of mole balances ODES of Na, Ng, Ne, N, as a function of time using feed concentration Ca0, feed volumetric flow rate v,, initial volume Vo, rate constants kA, k2A, and time t.
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