Difference between revisions of "Batch reactor"
FelixMueller (Talk | contribs) |
FelixMueller (Talk | contribs) |
||
| Line 57: | Line 57: | ||
[[Category:MIOCP]] | [[Category:MIOCP]] | ||
[[Category:ODE model]] | [[Category:ODE model]] | ||
| − | [[Chemical engineering]] | + | [[Category:Chemical engineering]] |
| − | [[Path-constrained arcs]] | + | [[Category:Path-constrained arcs]] |
Revision as of 23:01, 27 June 2016
| Batch reactor | |
|---|---|
| State dimension: | 1 |
| Differential states: | 2 |
| Continuous control functions: | 1 |
| Interior point equalities: | 2 |
This batch reactor problem describes the consecutive reaction of some substance A via substance B into a desired product C.
The system is interacted with via the control function 
which stands for the temperature.
The goal is to produce as much of substance B (which can then be converted into product C) as possible within the time limit.
Mathematical formulation
The optimal control problem is given by
![\begin{array}{llcl}
\displaystyle \max_{x, u} & x_2(t_f) \\[1.5ex]
\mbox{s.t.} & \dot{x}_1 & = & -k_1 x_1^2,\\
& \dot{x}_2 & = & k_1 x_1^2 - k_2 x_2,\\
& k_1 & = & 4000 \; e^{(-2500/T(t))}, \\
& k_2 & = & 620000 \; e^{(-5000/T(t))}, \\[1.5ex]
& x(0) &=& (1, 0)^T, \\
& T(t) &\in& [298, 398].
\end{array}](https://mintoc.de/images/math/a/b/1/ab1bc5c4f948e77cae38bccca4a243fd.png)
and 
represent the concentrations of A and B at timepoint 
respectively. The control function represents the temperature.
Parameters
The starting time and end time are given by ![[t_0, t_f] = [0, 1]](https://mintoc.de/images/math/9/0/d/90d354576ba03d7a9fb1d63ba2ecc7cc.png)
.
Reference Solutions
This solution was computed using JuMP with a collocation method and 300 discretization points. The differential equations were solved using the explicit Euler Method. The source code can be found at Batch reactor (JuMP).
The optimal objective value of the problem is 
.
- Reference solution plots
Optimal states
and .
Optimal control
.
Source Code
Model descriptions are available in
References
The problem can be found in the Tomlab PROPT guide or in the Dynopt guide.
