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Chapter 10: Catalysis and Catalytic Reactors
Learning Resources
Example CD10-2: Least Squares Analysis to Determine the Rate Law Parameters k, K T, and K B
(Example 6-2 in 2nd ed.)Use the data in Table 10-6 together with Equation (10-81) to evaluate the rate law parameters. Then calculate the catalyst weight necessary for these rate law parameters. |
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SolutionThe calculations are shown in Table CD10-2.1. A plot of |
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![]() Figure CD10-2.1 |
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Rearranging Equation (10-81) for PB = 0, we have |
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(CD10-2.1) |
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From Figure CD10-2.1, |
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Substituting these values into Equation (CD10-2.1), we find that |
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(CD10-2.2) |
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The constant K B can be evaluated
from the slope of the plot of |
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![]() Figure CD10-2.2 |
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In addition to the graphical determination, we can use linear regression
to determine the rate law parameters. We will use Equations (5-31) through (5-33)
along with Table CD10-2.2 to determine k, K T , and |
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(10-81) |
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and Equation (5-30), |
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(5-30) |
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where Y= |
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(CD10-2.3) |
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If we were to use a software package such as POLYMATH, we would simply enter Y, X 1 X 2 , and for each run and the parameters a 0 , a 1 , and a 2 would be displayed in a few seconds. Alternatively, we can form Table CD10-2.2 and carry out the numerical operations ourselves to determine the rate law parameters. We can either form the table using a calculator or by using a spreadsheet such as Excel or Lotus 123. |
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Equation (CD10-2.3) becomes |
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6.62 X 109 = 16a0 + 12a1 + 61.5a2 |
(CD10-2.6) |
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Equation (CD10-2.4) becomes |
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5.67 X 109 = 12a0 = 44a = 12a21 |
(CD10-2.7) |
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Equation (CD10-2.5) becomes |
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6.0 X 1010 = 61.5a0 + 12a1 + 761.25a2 |
(CD10-2.8) |
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Solving these three equations simultaneously, we obtain a0 = 7.12 x 10 7 , a 1 = 9.0 x 10 7 , and a 2 = 7.16 x 10 7 . The corresponding rate law parameters are |
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Using POLYMATH, we obtain |
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with, of course, the parameter values being the same as those obtained
from Table CD10-2.2 and Equation (CD10-2.5). is given by the equation |
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(CD10-2.9) |
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whereP i is in atm. |
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After we have the adsorption constant K T and K B ,
we could calculate the ratio of sites. For example, the ratio of toluene sites to
benzene sites at 40% conversion is |
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We see that at 40% conversion there are approximately 20% more sites occupied by toluene than by benzene. |
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Calculate the catalyst weight necessary for these parameters: |
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If we were to neglect pressure drop, we can solve for the catalyst weight necessary to achieve 65% conversion with the aid of Simpson's five-point formula. |
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Substituting for k, K T , K B ,P B , PH 2, and PT in Equation (E10-3.2) yields |
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(CD10-2.10) |
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We can now proceed to solve for the catalyst weight necessary to obtain this conversion by using Equation (CD10-2.10). |
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Hand calculations: The calculations for X versus (1/ |
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Using numerical integration (Appendix A.5), after dividing the area under the curve into two parts: X = 0 to X = 0.52 with h 1 = 0.13 and X = 0.52 to X = 0.65 with h 2 = 0.13, we have |
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Numerical |
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Since the reciprocal of the rate of reaction increases sharply as the conversion approaches unity, the numerical integration probably should have included a greater number of integrals than the six used in the calculation. |