Denbigh Reaction: Difference between revisions
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\quad \dot{x_3}(t) & = & k_3(t) \cdot x_2(t),\\ | \quad \dot{x_3}(t) & = & k_3(t) \cdot x_2(t),\\ | ||
\quad k_i(t) & = & k_i^* \cdot \exp\left( \frac{-E_i}{T(t)} \right), \ i=1,\ldots,4, \\ | \quad k_i(t) & = & k_i^* \cdot \exp\left( \frac{-E_i}{T(t)} \right), \ i=1,\ldots,4, \\ | ||
\quad T(t) & \in & [273, 415] \ \quad \forall t \in [0,t_f] \\ | \quad T(t) & \in & [273, 415] \ \quad \forall t \in [0,t_f], \\ | ||
\quad x(0) &=& (1, 0, 0)^T | \quad x(0) &=& (1, 0, 0)^T. | ||
\end{array} | \end{array} | ||
</math> | </math> | ||
Revision as of 14:18, 22 August 2025
| 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