Denbigh Reaction: Difference between revisions
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|<math>E_1</math> | |<math>E_1</math> | ||
|<math>10^3</math> | |<math>3 \cdot 10^3</math> | ||
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|<math>E_2</math> | |<math>E_2</math> | ||
|<math>10^ | |<math>6 \cdot 10^3</math> | ||
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|<math>E_3</math> | |<math>E_3</math> | ||
|<math>10</math> | |<math>3 \cdot 10^3</math> | ||
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|<math>E_4</math> | |<math>E_4</math> | ||
|<math> | |<math>0</math> | ||
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|<math>k_1^*</math> | |<math>k_1^*</math> | ||
|<math> | |<math>10^3</math> | ||
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|<math>k_2^*</math> | |<math>k_2^*</math> | ||
|<math> | |<math>10^7</math> | ||
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|<math>k_3^*</math> | |<math>k_3^*</math> | ||
|<math> | |<math>10</math> | ||
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|<math>k_4^*</math> | |<math>k_4^*</math> | ||
|<math> | |<math>10^{-3}</math> | ||
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|<math>t_f</math> | |<math>t_f</math> | ||
|<math>10^3</math> | |<math>10^3</math> | ||
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== Reference Solutions == | == Reference Solutions == | ||
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Here is one local solution to the above control problem. | Here is one local solution to the above control problem. | ||
<gallery caption="Reference solution plots" widths=" | <gallery caption="Reference solution plots" widths="500px" heights="300px" perrow="1"> | ||
Image:Denbigh.png| States and discretized control for a local optimum. | Image:Denbigh.png| States and discretized control for a local optimum. | ||
</gallery> | </gallery> | ||
Latest revision as of 12:56, 29 January 2026
| Denbigh Reaction | |
|---|---|
| State dimension: | 1 |
| Differential states: | 3 |
| Discrete control functions: | 1 |
The Denbigh Reaction problem is based on the system of chemical reactions initially considered by Denbigh [1], which was also studied by Aris [2] and more recently by Luus [3]:
where is an intermediate, is the desired product, and and are waste products. The optimal control problem is to find (the temperature of the reactor as a function of time) so that the yield of is maximized at the end of the given batch time .
Its dynamics are given by a three-dimensional ODE model. The optimal control functions is given by a path-constrained arc.
Mathematical formulation
Parameters
| Symbol | Value |
Reference Solutions
Here is one local solution to the above control problem.
- Reference solution plots
-
States and discretized control for a local optimum.
Miscellaneous and Further Reading
This formulation and a detailed description can be found in [1].
References
[1] Kenneth Denbigh, Chemical Reactor Theory an Introduction, Cambridge University Press, London, 1965.
[2] Rutherford Aris. The Optimal Design of Chemical Reactors A Study in Dynamic Programming. Academic Press, London, 1961.
[3] Rein Luus, Iterative Dynamic Programming. CHAPMAN & HALL/CRC Monographs and Surveys in Pure and Applied Mathematics, New York, 2000.
[4] Tomlab optimization: https://tomopt.com/docs/propt/tomlab_propt030.php