Difference between revisions of "DOW Experimental Design"

DOW Experimental Design
State dimension:	1
Differential states:	11
Discrete control functions:	2
Path constraints:	4
Interior point equalities:	11

Revision as of 12:22, 25 September 2024

The DOW Experimental Design problem models the OED problem for the parameter estimation problem formulated by the DOW Chemical Co. in 1981. The following formulation is taken from "Nonlinear Parameter Estimation: a Case Study Comparison" by L. T. Biegler and J. J. Damiano add quote.

Chemical background

The chemical species are disguised for proprietary reasons and the desired reaction is given by $HA + 2BM \rightarrow AB + HBMH$ , where $AB$ is the desired product. The reactions are described as follows:

Slow Kinetic Reactions:

$\begin{array}{c} M^- + BM \underset{k_{-1}}{\leftarrow} \overset{k_1}{\rightarrow} MBM^- \\ A^- + BM \overset{k_2}{\rightarrow} ABM^- \\ M^- + AB \underset{k_{-3}}{\leftarrow} \overset{k_3}{\rightarrow} ABM^- \end{array}$

Acid-Base Reactions:

$\begin{array}{c} MBMH \leftarrow K_1 \rightarrow MBM^- + H^+ \\ HA \leftarrow K_2 \rightarrow A^- + H^+ \\ HABM \leftarrow K_2 \rightarrow ABM^- + H^+ \end{array}$

In order to devise a model to account for these reactions, it is first necessary to distinguish between the overall concentration of a species and the concentration of its neutral form. Overall concentrations are defined for three components based on neutral and ionic species

$\begin{array}{c} \left[HBMH\right] = \left[ (MBMH)_N \right] + \left[ MBM^- \right] \\ \left[HA\right] = \left[ (HA)_N \right] + \left[ A^- \right] \\ \left[HABM\right] = \left[ (HABM)_N \right] + \left[ ABM^- \right] \end{array}$

Here $[ \ ]$ denotes the concentration of the species in $\operatorname{gmol}/\operatorname{kg}$ . By assuming the rapid acid-base reactions are at equilibrium, the equilibrium constants $K_1,K_2,K_3$ can be defined as

$\begin{array}{c} K_1 = \frac{[MBM^-][H^+]}{[(MBMH)_N]} \\ K_1 = \frac{[A^-][H^+]}{[(HA)_N]} \\ K_1 = \frac{[ABM^-][H^+]}{[(HABM)_N]} \end{array}$

The anionic species may then be represented by

$\begin{array}{cr} \left[MBM^-\right] = \frac{K_1[MBMH]}{K_1 + [H^+]} & \quad (a) \\ \left[A^-\right] = \frac{K_2[HA]}{K_2 + [H^+]} & \quad (b)\\ \left[ABM^-\right] = \frac{K_3[HABM]}{K_3 + [H^+]}& \quad (c) \end{array}$

Material balance equations for the three reactants in the slow kinetic reactions yield:

$\begin{array}{cr} \frac{d[M^-]}{dt} = -k_1 \left[ M^- \right] \left[ BM \right] + k_{-1} \left[ MBM^- \right] - k_3 \left[ M^- \right]\left[ AB \right] + k_{-1} \left[ ABM^- \right] & \quad (d)\\ \frac{d[BM]}{dt} = -k_1 \left[ M^- \right] \left[ BM \right] + k_{-1} \left[ MBM^- \right] - k_2 \left[ A^- \right]\left[ BM \right] & \quad (e)\\ \frac{d[AB]}{dt} = -k_3 \left[ M^- \right] \left[ AB \right] + k_{-3} \left[ ABM^- \right] & \quad (f) \end{array}$

From stoichiometry, rate expressions can also be written for the total species:

$\begin{array}{cr} \frac{d[MBMH]}{dt} = k_1 \left[ M^- \right] \left[ BM \right] + k_{-1} \left[ MBM^- \right] & \quad (g)\\ \frac{d[HA]}{dt} = k_2 \left[ A^- \right] \left[ BM \right] & \quad (h)\\ \frac{d[HABM]}{dt} = k_2 \left[ A^- \right] \left[ BM \right] + k_3 \left[ M^- \right] \left[ AB \right] - k_{-3} \left[ ABM^- \right]& \quad (i) \end{array}$

An electroneutrality constraint gives the hydrogen ion concentration $\left[ H^+ \right]$ as

$\left[ H^+ \right] + \left[ Q^+ \right] = \left[ M^- \right] + \left[ MBM^- \right] + \left[ A^- \right] + \left[ ABM^- \right] \quad \quad (j)$

Based on similarities of reacting species, we assume

$k_3 = k_1, \quad k_{-3} = \frac{1}{2} k_{-1}$

With these assumptions, the three rate constants $k_1,k_2$ and $k_3$ must be estimated. Each of these can be fitted with two adjustable model parameters, assuming an Arrhenius temperature dependence. That is

$\begin{array}{c} k_i = \alpha_i \exp(-E_i /(RT)), \quad i \in \{-1,1,2\} \end{array}$

Here $R$ is the gas constant and $T$ is reaction temperature in Kelvins. The parameter $\alpha_i$ , given in $\operatorname{mol}/( \operatorname{kg} \cdot \operatorname{h})$ , represent the pre-exponential factor and $E_i$ , with unit $\operatorname{cal}/{\operatorname{mol}}$ , is the activation energy.

Mathematical formulation

The chemical processes $(a)-(j)$ can be expressed mathematically as six differential equations and four algebraic equations:

$\begin{array}{lr} \dot{y}_1 = -k_2 y_8 y_2 & \quad (1),(h) \\ \dot{y}_2 = -k_1 y_6 y_2 + k_{-1} y_{10} - k_2 y_8 y_2 & \quad (2),(e) \\ \dot{y}_3 = -k_2 y_8 y_2 + k_1 y_6 y_4 - \frac{1}{2} k_{-1} y_9 & \quad (3),(i) \\ \dot{y}_4 = -k_1 y_6 y_4 + \frac{1}{2} k_{-1} y_9 & \quad (4),(f) \\ \dot{y}_5 = -k_1 y_6 y_2 + k_{-1} y_{10} & \quad (5),(g) \\ \dot{y}_6 = -k_1 (y_6 y_2 + y_6 y_4) + k_{-1} (y_{10} + \frac{1}{2} y_9) & \quad (6),(d) \\ y_7 = -\left[ Q^+ \right] + y_6 + y_8 + y_9 + y_{10} & \quad (7),(j)\\ y_8 = \frac{\theta_8 y_1}{\theta_8 + y_7} & \quad (8),(b)\\ y_9 = \frac{\theta_9 y_3}{\theta_9 + y_7} & \quad (9),(c)\\ y_{10} = \frac{\theta_7 y_5}{\theta_7 + y_7} & \quad (10),(a) \end{array}$

Here the letters in parentheses stand for the corresponding chemical process and the quantity $\left[Q^+\right]$ is a constant during the reaction. The nine parameters form the vector

$\theta = (\alpha_1,E_1,\alpha_2,E_2,\alpha_{-1},E_{-1},K_1,K_2,K_3)$

The predicted concentrations form the vector

$y = (HA,BM,HABM,AB,MBMH,M^-,H^+,A^-,ABM^-,MBM^-)$

Let $f_k(\cdot)$ denote the right hand side of equation $(k)$ for $k=1,\ldots,6$ . We reformulate the last four algebraic equations as differential ones:

$\begin{array}{l r} \dot{y}_7 = f_7 = f_6 + f_8 + f_9 + f_{10} & \quad (7') \\ \dot{y}_8 = f_8 = \frac{\theta_8 f_1 \cdot (\theta_8 + f_7) - \theta_8 y_1 f_7}{(\theta_8 + y_7)^2} & \quad (8') \\ \dot{y}_9 = f_9 = \frac{\theta_9 f_3 \cdot (\theta_9 + f_7) - \theta_9 y_3 f_7}{(\theta_9 + y_7)^2} & \quad (9')\\ \dot{y}_{10} = f_{10} = \frac{\theta_7 f_5 \cdot (\theta_7 + f_7) - \theta_7 y_5 f_7}{(\theta_7 + y_7)^2} & \quad (10') \end{array}$

The right hand sides of $(1)-(6)$ and $(7')-(9')$ are summarized as the vector-valued function $f$ . Moreover, let

$\begin{array}{l} f_{y,m,n}(\cdot) = \frac{\partial f_m(\cdot)}{\partial y_n}, \quad m,n \in \{1,\ldots,10\} \\ f_{\theta,m,n}(\cdot) = \frac{\partial f_m(\cdot)}{\partial \theta_n}, \quad m \in \{1,\ldots,10\}; \ n\in \{1,\ldots,9\} \end{array}$

Parameters

The initial parameter estimates are:

$\begin{array}{c} \alpha_1 = 2.0 \times 10^{13} \\ E_1 = 2.0 \times 10^{4} \\ \alpha_2 = 2.0 \times 10^{13} \\ E_2 = 2.0 \times 10^{4} \\ \alpha_{-1} = 4.3 \times 10^{15} \\ E_{-1} = 2.0 \times 10^{4} \\ K_1 = 1.0 \times 10^{-17} \\ K_2 = 1.0 \times 10^{-11} \\ K_3 = 1.0 \times 10^{-17} \\ \end{array}$

There are three datasets for different temperatures $T$ , with corresponding starting values

$\begin{array}{lccc} & 40^\circ C & 67^\circ C & 100^\circ C \\ y_1(0) = & 1.7066 & 1.6749 & 1.5608 \\ y_2(0) = & 8.32 & 8.2262 & 8.3546 \\ y_3(0) = & 0.01 & 0.0104 & 0.0082 \\ y_4 (0) = & 0 & 0.0017 & 0.0086 \end{array}$

The initial model conditions in addition to those given in the data sets are:

$\begin{array}{l} y_5 = 0 \\ y_6 = 0.0131 \\ y_7 = \frac{1}{2} \cdot \left( -K_2 + \sqrt{K_2^2 + 4K_2 y_1(0)} \right) \\ y_8 = y_7 \\ y_9 = 0 \\ y_{10} = 0 \end{array}$

Optimal Experimental Design Problem

To be specified.

We are interested in when to measure (with an upper bound $M_i$ on the measuring time for each observable). We define

$\begin{array}{l} f_y(\cdot) \in \mathbb{R}^{10 \times 10} \quad \text{ with } (f_y)_{i,j} = f_{y,i,j}, \\ f_\theta(\cdot) \in \mathbb{R}^{10 \times 9} \quad \text{ with } (f_\theta)_{i,j} = f_{\theta,i,j} \end{array}$

In this approach, we add the so-called sensitivities $G=dy/d\theta$ . For the differential equations this means

$\dot{G}(t) = f_y(y(t),\theta) G(t) + f_\theta(y(t),\theta), \quad G(0) = \frac{\partial y(0)}{\partial \theta}$

Now we formulate the OED problem as described in (Optimal Experimental Design for Universal Differential Equations add quote)

$\begin{array}{lll} \displaystyle \min_{y,G,F,z,w} && \text{trace} \; \left( F^{-1}(t_f) \right) \\ \text{subject to} \\ \quad \dot{y}(t) & = & f(y(t),\theta) \\ \quad \dot{G}(t) & = & f_y(y(t),\theta) G(t) + f_\theta(y(t),\theta) \\ \quad \dot{F}(t) & = & \sum_{i=1}^{n_o} w_i(t)(h^i_y(y(t))G(t))^T(h^i_y(y(t))G(t)) \\ \quad \dot{z}(t) & = & w(t), \\ \quad y(0) & = & y_0 \\ \quad G(0) & = & \frac{\partial y(0)}{\partial \theta} \\ \quad F(0) & = & 0, \\ \quad z(0) & = & 0 \\ \quad w(t) & \in & \mathcal{W} \\ \quad z_i(t_f) & \leq & M_i \end{array}$

Here $h:\mathbb{R}^{10} \rightarrow \mathbb{R}^{n_o}$ is the observed function. The evolution of the symmetric matrix $F: \left[0,t_f \right] \rightarrow \mathbb{R}^{9 \times 9}$ is given by the weighted sum of observability Gramians $h^i_y (y(t)) G(t), \ i = 1,\ldots,n_o$ for each observed function of states. The weights $w_i (t) \in \{0, 1\}, \ i = 1,\ldots,n_o$ are the (binary) sampling decisions, where $w_i (t) = 1$ denotes the decision to perform a measurement at time $t$ .

Miscellaneous and Further Reading

To be specified.

References

To be added.

@@ Line 1: / Line 1: @@
+{{Dimensions
+|nd        = 1
+|nx        = 11
+|nw        = 2
+|nc        = 4
+|nre       = 11
+}}
 The '''DOW Experimental Design problem''' models the OED problem for the parameter estimation problem formulated by the DOW Chemical Co. in 1981. The following formulation is taken from "Nonlinear Parameter Estimation:
 a Case Study Comparison" by L. T. Biegler and J. J. Damiano <span style="color:red">add quote</span>.
-The chemical species are disguised for proprietary reasons and the desired reaction is given by <math>HA + 2BM \rightarrow AB + HBMH</math>, where AB is the desired product. The reactions are described as follows:
+== Chemical background ==
+The chemical species are disguised for proprietary reasons and the desired reaction is given by <math>HA + 2BM \rightarrow AB + HBMH</math>, where <math>AB</math> is the desired product. The reactions are described as follows:
 Slow Kinetic Reactions:
@@ Line 27: / Line 37: @@
 In order to devise a model to account for these reactions, it is
 first necessary to distinguish between the overall concentration of
-a species and the concentration of its neutral form. Overall con-
+a species and the concentration of its neutral form. Overall concentrations are defined for three components based on neutral
-centrations are defined for three components based on neutral
 and ionic species
 <p>
@@ Line 39: / Line 48: @@
 </math>
 </p>
-Here <math>[ \ ]</math> denotes the concentration of the species in <math>gmol/kg</math>.
+Here <math>[ \ ]</math> denotes the concentration of the species in <math>\operatorname{gmol}/\operatorname{kg}</math>.
 By assuming the rapid acid-base reactions are at equilibrium, the equilibrium constants <math>K_1,K_2,K_3</math> can be defined as
 <p>
@@ Line 83: / Line 92: @@
 </math>
 </p>
-An electroneutrality constraint gives the hydrogen ion con-
+An electroneutrality constraint gives the hydrogen ion concentration <math>\left[ H^+ \right]</math> as
-centration <math>\left[ H^+ \right]</math> as
 <p>
   <math>
@@ Line 103: / Line 111: @@
   </math>
 </p>
-Here <math>R</math> is the gas constant, <math>T</math> is reaction temperature in Kelvins and the parameters <math>\alpha_i,E_i</math> represent the pre-exponential factor and activation energy, respectively, for the appropriate rate constant.
+Here <math>R</math> is the gas constant and <math>T</math> is reaction temperature in Kelvins. The parameter <math>\alpha_i</math>, given in <math>\operatorname{mol}/( \operatorname{kg} \cdot \operatorname{h})</math>, represent the pre-exponential factor and <math>E_i</math>, with unit <math>\operatorname{cal}/{\operatorname{mol}}</math>, is the activation energy.
 == Mathematical formulation ==
-The chemical processes <math>(a)-(j)</math> can be expressed mathematically as six differential and four algebraic equations:
+The chemical processes <math>(a)-(j)</math> can be expressed mathematically as six differential equations and four algebraic equations:
 <p>
   <math>
    \begin{array}{lr}
-   \frac{d y_1}{dt} = -k_2 y_8 y_2 & \quad (1),(h) \\
+   \dot{y}_1 = -k_2 y_8 y_2 & \quad (1),(h) \\
-   \frac{d y_2}{dt} = -k_1 y_6 y_2 + k_{-1} y_{10} - k_2 y_8 y_2 & \quad (2),(e) \\
+   \dot{y}_2 = -k_1 y_6 y_2 + k_{-1} y_{10} - k_2 y_8 y_2 & \quad (2),(e) \\
-   \frac{d y_3}{dt} = -k_2 y_8 y_2 + k_1 y_6 y_4 - \frac{1}{2} k_{-1} y_9 & \quad (3),(i) \\
+   \dot{y}_3 = -k_2 y_8 y_2 + k_1 y_6 y_4 - \frac{1}{2} k_{-1} y_9 & \quad (3),(i) \\
-   \frac{d y_4}{dt} = -k_1 y_6 y_4  + \frac{1}{2} k_{-1} y_9 & \quad (4),(f) \\
+   \dot{y}_4 = -k_1 y_6 y_4  + \frac{1}{2} k_{-1} y_9 & \quad (4),(f) \\
-   \frac{d y_5}{dt} = -k_1 y_6 y_2 + k_{-1} y_{10} & \quad (5),(g) \\
+   \dot{y}_5 = -k_1 y_6 y_2 + k_{-1} y_{10} & \quad (5),(g) \\
-   \frac{d y_6}{dt} = -k_1 (y_6 y_2 + y_6 y_4) + k_{-1} (y_{10} + \frac{1}{2} y_9) & \quad (6),(d) \\
+   \dot{y}_6 = -k_1 (y_6 y_2 + y_6 y_4) + k_{-1} (y_{10} + \frac{1}{2} y_9) & \quad (6),(d) \\
    y_7 = -\left[ Q^+ \right] + y_6 + y_8 + y_9 + y_{10} & \quad (7),(j)\\
    y_8 = \frac{\theta_8 y_1}{\theta_8 + y_7} & \quad (8),(b)\\
@@ Line 124: / Line 132: @@
   </math>
 </p>
-Here the letter stands for the corresponding chemical process and the quantity <math>\left[Q^+\right]</math> is a concentration which is assumed to be constant during the reactions.
+Here the letters in parentheses stand for the corresponding chemical process and the quantity <math>\left[Q^+\right]</math> is a constant during the reaction.
 The nine parameters form the vector
 <p>
@@ Line 143: / Line 151: @@
   <math>
    \begin{array}{l r}
-    \frac{d y_7}{dt} = f_7 = f_6 + f_8 + f_9 + f_{10} & \quad (7') \\
+    \dot{y}_7 = f_7 = f_6 + f_8 + f_9 + f_{10} & \quad (7') \\
-    \frac{d y_8}{dt} = f_8 = \frac{\theta_8 f_1 \cdot (\theta_8 + f_7) - \theta_8 y_1 f_7}{(\theta_8 + y_7)^2} & \quad (8') \\
+    \dot{y}_8 = f_8 = \frac{\theta_8 f_1 \cdot (\theta_8 + f_7) - \theta_8 y_1 f_7}{(\theta_8 + y_7)^2} & \quad (8') \\
-    \frac{d y_9}{dt} = f_9 = \frac{\theta_9 f_3 \cdot (\theta_9 + f_7) - \theta_9 y_3 f_7}{(\theta_9 + y_7)^2}  & \quad (9')\\
+    \dot{y}_9 = f_9 = \frac{\theta_9 f_3 \cdot (\theta_9 + f_7) - \theta_9 y_3 f_7}{(\theta_9 + y_7)^2}  & \quad (9')\\
-    \frac{d y_{10}}{dt} = f_{10} = \frac{\theta_7 f_5 \cdot (\theta_7 + f_7) - \theta_7 y_5 f_7}{(\theta_7 + y_7)^2} & \quad (10')
+    \dot{y}_{10} = f_{10} = \frac{\theta_7 f_5 \cdot (\theta_7 + f_7) - \theta_7 y_5 f_7}{(\theta_7 + y_7)^2} & \quad (10')
    \end{array}
   </math>
@@ Line 155: / Line 163: @@
   <math>
    \begin{array}{l}
-   f_{y,m,n}(\cdot) = \frac{\partial f_m(\cdot)}{\partial y_n}, \quad m,n \in \{1,\ldots,6\} \\
+   f_{y,m,n}(\cdot) = \frac{\partial f_m(\cdot)}{\partial y_n}, \quad m,n \in \{1,\ldots,10\} \\
-   f_{\theta,m,n}(\cdot) = \frac{\partial f_m(\cdot)}{\partial y_n}
+   f_{\theta,m,n}(\cdot) = \frac{\partial f_m(\cdot)}{\partial \theta_n}, \quad m \in \{1,\ldots,10\}; \ n\in \{1,\ldots,9\}
    \end{array}
   </math>
 </p>
+== Parameters ==
+The initial parameter estimates are:
+<p>
+ <math>
+  \begin{array}{c}
+   \alpha_1 = 2.0 \times 10^{13} \\
+   E_1 = 2.0 \times 10^{4} \\
+   \alpha_2 = 2.0 \times 10^{13} \\
+   E_2 = 2.0 \times 10^{4} \\
+   \alpha_{-1} = 4.3 \times 10^{15} \\
+   E_{-1} = 2.0 \times 10^{4} \\
+   K_1 = 1.0 \times 10^{-17} \\
+   K_2 = 1.0 \times 10^{-11} \\
+   K_3 = 1.0 \times 10^{-17} \\
+  \end{array}
+ </math>
+</p>
+There are three datasets for different temperatures <math>T</math>, with corresponding starting values
+<p>
+ <math>
+  \begin{array}{lccc}
+   & 40^\circ C & 67^\circ C & 100^\circ C \\
+  y_1(0) = & 1.7066 & 1.6749 & 1.5608 \\
+  y_2(0) = & 8.32 & 8.2262 & 8.3546 \\
+  y_3(0) = & 0.01 & 0.0104 & 0.0082 \\
+  y_4 (0) = & 0 & 0.0017 & 0.0086
+  \end{array}
+ </math>
+</p>
+The initial model conditions in addition to those given in the
+data sets are:
+<p>
+ <math>
+  \begin{array}{l}
+   y_5 = 0 \\
+   y_6 = 0.0131 \\
+   y_7 = \frac{1}{2} \cdot \left( -K_2 + \sqrt{K_2^2 + 4K_2 y_1(0)} \right) \\
+   y_8 = y_7 \\
+   y_9 = 0 \\
+   y_{10} = 0
+  \end{array}
+ </math>
+</p>
+== Optimal Experimental Design Problem ==
+To be specified.
 <!--
@@ Line 243: / Line 299: @@
 are the (binary) sampling decisions, where <math> w_i (t) = 1 </math> denotes the decision to perform a measurement at
 time <math>t</math>.
-== Parameters ==
-The initial parameter estimates are:
-<p>
- <math>
-  \begin{array}{c}
-   \alpha_1 = 2.0 \times 10^{13} \\
-   E_1 = 2.0 \times 10^{4} \\
-   \alpha_2 = 2.0 \times 10^{13} \\
-   E_2 = 2.0 \times 10^{4} \\
-   \alpha_{-1} = 4.3 \times 10^{15} \\
-   E_{-1} = 2.0 \times 10^{4} \\
-   K_1 = 1.0 \times 10^{-17} \\
-   K_2 = 1.0 \times 10^{-11} \\
-   K_3 = 1.0 \times 10^{-17} \\
-  \end{array}
- </math>
-</p>
-The initial model conditions in addition to those given in the
-data sets are:
-<p>
- <math>
-  \begin{array}{l}
-   y_5 = 0 \\
-   y_6 = 0.0131 \\
-   y_7 = \frac{1}{2} \cdot \left( -K_2 + \sqrt{K_2^2 + 4K_2 y_1(0)} \right) \\
-   y_8 = y_7 \\
-   y_9 = 0 \\
-   y_{10} = 0
-  \end{array}
- </math>
-</p>
 == Miscellaneous and Further Reading ==
-The Lotka Volterra fishing problem was introduced by Sebastian Sager in a proceedings paper <bib id="Sager2006" /> and revisited in his PhD thesis <bib id="Sager2005" />. These are also the references to look for more details. The experimental design problem has been described in the habilitation thesis of Sager, <bib id="Sager2011d" />.
+To be specified.
 == References ==
+To be added.
+<!--
 <biblist />
+-->
 <!--List of all categories this page is part of. List characterization of solution behavior, model properties, ore presence of implementation details (e.g., AMPL for AMPL model) here -->

Difference between revisions of "DOW Experimental Design"

Revision as of 12:22, 25 September 2024

Contents

Chemical background

Mathematical formulation

Parameters

Optimal Experimental Design Problem

Miscellaneous and Further Reading

References

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