| 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,
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(CDE8-3.4) | |
| and Equation (CD8-12) requires | |||
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(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 as is 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, if is 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.
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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 |