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Diels-Alder Reaction Experimental Design: Difference between revisions

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  \dot{F}(t) & = & w(t) (h_x(x(t),u(t),p)G(t))^T (h_x(x(t),u(t),p)G(t)) \\
  \dot{F}(t) & = & w(t) (h_x(x(t),u(t),p)G(t))^T (h_x(x(t),u(t),p)G(t)) \\
  \\
  \\
  0.1 & \le & n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 \ + \ n_{a4} \ \cdot \ M_4   , \forall \, t \in I \\
  0.1 & \le & n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 \ + \ n_{a4} \ \cdot \ M_4   \\
  \\
  \\
  10 & \ge & n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 \ + \ n_{a4} \ \cdot \ M_4   , \forall \, t \in I \\
  10 & \ge & n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 \ + \ n_{a4} \ \cdot \ M_4     \\
  \\
  \\
  0.1 & \le & \frac{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 }{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2  \ + \ n_{a4} \ \cdot \ M_4 } , \forall \, t \in I \\
  0.1 & \le & \frac{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 }{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2  \ + \ n_{a4} \ \cdot \ M_4 }   \\
  \\
  \\
  0.7 & \ge & \frac{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 }{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2  \ + \ n_{a4} \ \cdot \ M_4 }  , \forall \, t \in I \\
  0.7 & \ge & \frac{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2 }{ n_{a1} \ \cdot \ M_1 \ + \ n_{a2} \ \cdot \ M_2  \ + \ n_{a4} \ \cdot \ M_4 }  \\
  \\
  \\
  0 & = & \vartheta_{lo}, \forall \, t \in [t_0,2] \\
  0 & = & \vartheta_{lo}, \forall \, t \in [t_0,2] \\

Revision as of 13:07, 4 December 2015

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Model Formulation

Differential equation system:

n1˙(t)=kn1(t)  n2(t)mtot,n2˙(t)=kn1(t)  n2(t)mtot,n2˙(t)=  kn1(t)  n2(t)mtot

Solvent:

n4=na4

Reaction velocity constant:

k=k1  exp(E1R  (1T(t)  1Tref)) + kcat  ccat  exp(λ  t)  exp(EcatR  ( 1T(t)  1Tref))

Total mass:

mtot=n1  M1 + n2  M2 + n3  M3 + n4  M4

Temperature in Kelvin:

T(t)=ϑ(t)+273

The ODE system is summarized to:

x˙(t)=f(x(t),u(t),p)

Optimum Experimental Design Problem

minx,G,F,utrace(F1(ttf))s.t.x˙(t)=f(x(t),u(t),p),h˙(t)=n3(t)  M3mtot  100G˙(t)=fx(x(t),u(t),p)G(t) + fp(x(t),u(t),p)F˙(t)=w(t)(hx(x(t),u(t),p)G(t))T(hx(x(t),u(t),p)G(t))0.1na1  M1 + na2  M2 + na4  M410na1  M1 + na2  M2 + na4  M40.1na1  M1 + na2  M2na1  M1 + na2  M2 + na4  M40.7na1  M1 + na2  M2na1  M1 + na2  M2 + na4  M40=ϑlo,t[t0,2]0=ϑlo+t26(ϑupϑlo),t[2,8]0=ϑup,t[8,tend]x𝒳,u𝒰,pP.


State variables
Name Symbol Initial value (t0)
Molar number 1 n1(t) n1(t0)=na1
Molar number 2 n2(t) n2(t0)=na2
Molar number 3 n3(t) n3(t0)=0
Constants
Name Symbol Value
Molar Mass M1 0.1362
Molar Mass M2 0.09806
Molar Mass M3 0.23426
Molar Mass M4 0.236
Universal gas constant R 8.314
Reference temperature Tref 293
St.dev of measurement error σ 1
Parameters
Name Symbol Value
Steric factor k1 p10.01
Steric factor kkat p20.10
Activation energie E1 p360000
Activation energie Ekat p440000
Catalyst deactivation coefficient λ p50.25

with pj=1, j=1,,5

Control variables
Name Symbol Interval
Initial molar number 1 na1 [0.4,9.0]
Initial molar number 2 na2 [0.4,9.0]
Initial molar number 4 na4 [0.4,9.0]
Concentration of the catalyst ckat [0.0,6.0]
Initial molar number 1 ϑ(t) [20.0,100.0]

Parameters