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Unformatted text preview: C, = F , ~ U ~ , and then by compariwn with Figure 112 plot the concenrration of A as a function of rertctor volume as shown in Figure El1.1. Figure EI1.1 Concentration prufile. 2. Derive an equation relating Y v,, k, CAo, and CA. For a tubular reactor, the mole balance on species A Cj = A) was shown to be given by Equation ( 1  1 1). Then for species A (j = A) results For a fistorder reaction, the rate law (discussed in Chapter 3) is Because the volumetric flow rate. u , is constant ( u = uo). as it is for most liquid phase reactions, Multiplying both sides of Equation (EI1.2) by minus one and then substituting Equation (E 11. I) yields...
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 Spring '08
 Vanderwal,C
 Mole, Reaction, Kinetics

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