DICOPT did find the optimal solution,
BARON performs good
DICOPT:
--- DICOPT: Stopped on NLP worsening
The search was stopped because the objective function
of the NLP subproblems started to deteriorate.
--- DICOPT: Best integer solution found: 167427.657115
--- Restarting execution
--- batchdes.gms(182) 0 Mb
--- Reading solution for model batch
--- Executing after solve: elapsed 0:00:01.000
--- batchdes.gms(194) 3 Mb
*** Status: Normal completion
--- Job batchdes.gms Stop 06/12/11 20:01:05 elapsed 0:00:01.016
BARON:
Solution = 167427.657115 found at node 4
Best possible = 167427.656947
Absolute gap = 0.000167999998666346 optca = 1E-9
Relative gap = 0.00000 optcr = 0
--- Restarting execution
--- batchdes.gms(182) 0 Mb
--- Reading solution for model batch
--- Executing after solve: elapsed 0:00:00.704
--- batchdes.gms(194) 3 Mb
*** Status: Normal completion
--- Job batchdes.gms Stop 06/12/11 20:01:40 elapsed 0:00:00.704
$TITLE Optimal Design for Chemical Batch Processing (BATCHDES,SEQ=119)
$Ontext
A chemical batch process having three processing stages: mixing,
reaction and centrifuge separation, produce two products. This
model is used to determine the number and sizes of units to
operate in parallel at each stage. The resulting model is
nonlinear and mixed integer;
Morari, M, and Grossmann, I E, Eds, Chemical Engineering Optimization
Models with GAMS. Computer Aids for Chemical Engineering Corporation,
1991.
Kocis, G R, and Grossmann, I E, Global Optimization of Nonconvex MINLP
Problems in Process Synthesis. Independent Engineering Chemical
Research 27 (1988), 1407-1421.
$Offtext
Sets i products / a , b /
j stages /mixer, reactor, centrifuge/
k potential number of parallel units / 1 * 3 /
Variables y(k,j) binary variable denoting stage existence
Binary Variables y(k,j) ;
Option optcr=0;
option minlp=baron;
Solve batch using minlp minimizing cost ;
* converting variables into original form
actv(j) = exp(v.l(j)) ;
actb(i) = exp(b.l(i)) ;
acttl(i) = exp(tl.l(i));
actn(j) = exp(n.l(j)) ;
* optimal design
Display actv, actb, acttl, actn ;
$Ontext
A chemical batch process having three processing stages: mixing,
reaction and centrifuge separation, produce two products. This
model is used to determine the number and sizes of units to
operate in parallel at each stage. The resulting model is
nonlinear and mixed integer;
Morari, M, and Grossmann, I E, Eds, Chemical Engineering Optimization
Models with GAMS. Computer Aids for Chemical Engineering Corporation,
1991.
Kocis, G R, and Grossmann, I E, Global Optimization of Nonconvex MINLP
Problems in Process Synthesis. Independent Engineering Chemical
Research 27 (1988), 1407-1421.
$Offtext
Sets i products / a , b /
j stages /mixer, reactor, centrifuge/
k potential number of parallel units / 1 * 3 /
Variables y(k,j) binary variable denoting stage existence
Binary Variables y(k,j) ;
Option optcr=0;
option minlp=baron;
Solve batch using minlp minimizing cost ;
* converting variables into original form
actv(j) = exp(v.l(j)) ;
actb(i) = exp(b.l(i)) ;
acttl(i) = exp(tl.l(i));
actn(j) = exp(n.l(j)) ;
* optimal design
Display actv, actb, acttl, actn ;
没有评论:
发表评论