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<math>
\begin{array}{lll}
\begin{array}{llll}
  \displaystyle \max_{T} &  \displaystyle &x_2(t_N)  \\[1.5ex]
  \displaystyle \max_{T} &  \displaystyle x_2(t_N)  \\[1.5ex]
  \mbox{s.t.} &  \displaystyle \dot{x}_1 &= -k_1x_1-(k_3+k_4+k_5)x_1x_2\\
  \mbox{s.t.} &  \displaystyle \dot{x}_1 &=& -k_1x_1-(k_3+k_4+k_5)x_1x_2\\
  &  \displaystyle \dot{x}_2 &= k_1x_1-k_2x_2 + k_3x_1x_2\\
  &  \displaystyle \dot{x}_2 &=& k_1x_1-k_2x_2 + k_3x_1x_2\\
  &  \displaystyle \dot{x}_3 &= k_2x_2 + k_4x_1x_2\\
  &  \displaystyle \dot{x}_3 &=& k_2x_2 + k_4x_1x_2\\
  &  \displaystyle \dot{x}_4 &= k_5x_1x_2\\  
  &  \displaystyle \dot{x}_4 &=& k_5x_1x_2\\  
  &  \displaystyle k_i &= a_i e^{-\frac{b_i}{RT}},\quad \forall i\in \{1,\dots,5\} \\ [1.5ex]
  &  \displaystyle k_i &=& a_i \exp\left(-\frac{b_i}{RT}\right),\quad \forall i\in \{1,\dots,5\} \\[1.5ex]
  &  \displaystyle t &\in \left[t_0,t_N\right] \\
  &  \displaystyle t &\in& \left[t_0,t_N\right] \\
  &  \displaystyle T(t) &\in \left[698.15K,748.15K\right]\\
  &  \displaystyle T(t) &\in& \left[698.15K,748.15K\right]\\
  &  \displaystyle x(t_0) &= (1,0,0,0)^T\\
  &  \displaystyle x(t_0) &=& (1,0,0,0)^T\\
\end{array}  
\end{array}  
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Latest revision as of 13:53, 16 October 2025

Oil Shale Pyrolysis
State dimension: 4
Differential states: 4
Continuous control functions: 1
Discrete control functions: 0
Path constraints: 4
Interior point equalities: 0


The following problem is an example from the global optimal control literature and was introduced in [Wen1977]The entry doesn't exist yet.. The process starts with kerogen and is decomposed into pyrolytic bitumen, oil and gas, and residual carbon. The objective is to maximize the fraction of pyrolytic bitumen. There are 5 reactions including:

A1k1A2

A2k2A3

A1+A2k3A2+A2

A1+A2k4A3+A2

A1+A2k5A4+A2

Each reaction is governed by a rate described by:

ki=ki0exp(Ei/RT),(i=1,2,3,4,5)

Mathematical formulation

maxTx2(tN)s.t.x˙1=k1x1(k3+k4+k5)x1x2x˙2=k1x1k2x2+k3x1x2x˙3=k2x2+k4x1x2x˙4=k5x1x2ki=aiexp(biRT),i{1,,5}t[t0,tN]T(t)[698.15K,748.15K]x(t0)=(1,0,0,0)T

Parameters

State variables
Symbol Initial value (t0)
x1(t0) 1
x2(t0) 0
x3(t0) 0
x4(t0) 0
Parameters
Symbol Value
a1 20.3
a2 37.4
a3 33.8
a4 28.2
a5 31.0
b1 exp(8.86)
b2 exp(24.25)
b3 exp(23.67)
b4 exp(18.75)
b5 exp(20.7)
Control variable
Symbol Interval
T(t) [698.15,748.15]

Solutions

References

[Wen1977]The entry doesn't exist yet.