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ProcessDynamics2

# ProcessDynamics2 - Process Dynamics 2 Copyright Brian G...

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Process Dynamics 2 ü Copyright Brian G. Higgins (2004) Overview In these notes we show how to derive the governing equations for a perfectly mixed flow through reactor, also known as a CSTR. A schematic of the reactor (taken from Ref 1) is shown below Figure 1 The reactor displayed in Figure 1 has a single entrance stream at 1 and an exit stream at 2. The overall mass balance for this vessel is (1) ÅÅÅÅÅÅÅ t V H t L r „ V = A 1 r v ÿ n A - A 2 r v ÿ n A Here v is the velocity of the fluid, r is the density of the fluid, and n is the outward directed unit normal at the entrance and exits of the control volume V H t L . The cross-sectional areas at positions 1 and 2 are denoted by A 1 and A 2 . Note that r v ÿ n A is the mass flux passing through the differential area A. Thus we can write (1) as (2) M ÅÅÅÅÅÅÅ t = F ° 1 - F ° 2 where M is the mass of fluid in the tank at time t and F ° i is the mass flow rate across exit/entrance i. In liquid systems it is reasonably (at low to moderate pressures) to assume that the density r is constant so that (3) M = r V, F ° i = r Q ° i where now Q ° i is the volumetric flow rate across exit/entrance i. Thus (2) becomes (4) V ÅÅÅÅÅÅÅ t = Q ° 1 - Q ° 2 Now consider a species A in the inlet stream with concentration C H kg ê m 3 L that undergoes a irreversible reaction with a rate constant k: (5) A ö k B, r A = - kC A , r B = kC A A species balance over the reactor gives

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(6) ÅÅÅÅÅÅÅ t V H t L C i V = A 1 C i v i ÿ n A - A 2 C i v i ÿ n A + V r i V, i = A, B Here v i is the i th species velocity which at entrances and exits can be approximated by the mass average velocity v (since diffusion effects are negligible at entrances and exits). Thus the two species balances become (7) C A ÅÅÅÅÅÅÅÅÅ t = Q ° ÅÅÅÅ V C Af - Q ° ÅÅÅÅ V C A + r A , r A = - kC A C B ÅÅÅÅÅÅÅÅÅ t = Q ° ÅÅÅÅ V C Bf - Q ° ÅÅÅÅ V C B + r B r B = kC a We have assumed that the exit concentration of the species are the same as the species concentrations in the reactor and the volume V of the reactor remains constant. The latter assumption implies that the flow rates Q ° 1 = Q ° 2 . The assumption C i = C 2 i is reasonable if the reactor is well mixed! Further we will assume that there is
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