The oxidation of carbon monoxide is carried out in excess oxygen in a "fluidized" CSTR containing catalyst particles impregnated with platinum: | |||
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The rate law for the disappearance of CO, (A), is | (CDE8-3.1) | ||
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Combining a mole balance with the rate law gives | (CDE8-3.2) | ||
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which is of the form | |||
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(CDE8-3.3) | ||
At the bifurcation point, | |||
(CDE8-3.4) | |||
and Equation (CD8-12) requires | |||
(CDE8-3.5) | |||
Combining Equations (CDE8-3.4) and (CDE8-3.5) yields | |||
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(CDE8-3.6) | ||
Solving Equation (CDE8-1.6) for CA gives us | |||
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(CDE8-3.7) | ||
For, no real roots exist and there are no possible steady states. A rearrangement of Equation (CDE8-1.4) gives | |||
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(CDE8-3.8) | ||
Note that the right-hand side of Equation (CDE8-3.8) goes through a maximum asis increased from 1. To find this maximum we set the derivative of the right-hand side of Equation (CDE8-3.8) with respect to CA equal to zero, and solve to find that the maximum occurs at | |||
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(CDE8-3.9) | ||
Substituting Equation (CDE8-3.9) into the right-hand side of Equation (CDE8-3.8) gives the maximum as | |||
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(CDE8-3.10) | ||
The maximum value of the right-hand side is 1/27; consequently, ifis smaller than 27. Equation CDE8-3.10 can never be satisfied and there will be no MSS. Figure CDE8-1.1 shows a mapping of those regions where no multiple steady states will exist. | |||
Figure CDE8-3.1 |
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To learn the regions where MSS exist, we need to carry the analysis further. If we let, Equation (CDE8-3.6) can be written as | |||
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(CDE8-3.11) | ||
and Equation (CDE8-3.5) as | |||
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(CDE8-3.12) | ||
Equations (CDE8-3.11) and (CDE8-3.12) are used to form Table CDE8-3.1. Figure CDE8-3.2 shows a plot of as a function of. The shaded area shows the combinations of these variables that will produce multiple steady states. | |||
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Figure CDE8-3.2 |