Jiří Jaromír Klemeš, Petar Sabev Varbanov and Peng Yen Liew (Editors) Proceedings of the 24th European Symposium on Computer Aided Process Engineering – ESCAPE 24 June 15-18, 2014, Budapest, Hungary. Copyright © 2014 Elsevier B.V. All rights reserved.
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Select which opmal process configuraon under which condions?
Physical model fuel
Pareto froner
offgas
Obj1
Economic parameters
Impact on Pareto Distribuon soluons funcons
Ranking # of mes in top 5
CO2 capture
Decision criteria
1 2
Obj1
Soluons ranking based on probability → Decision-making support
Mulobjecve opmisaon min fobj(x,z) h(x,z)=0 g(x,z)≤0
CO2
air
Energy integraon model (MILP resoluon)
Economic model & LCA model
3
Obj1
fobj(x,z)
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1210
COE with CO2 tax [$/GJe]
80
upper boundary
70 60
base
50 40 Pre-comb BM Selexol
30 20
Post-comb MEA
lower
10 boundary 0 25
30
35
40
45
50
Pre-comb ATR Selexol
55
60
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1211
100
CO2 capture [%]
80 Postijcomb MEA
60 40 Preijcomb BM Selexol
Preijcomb ATR Selexol
20 0 25
30
35
40
45
50
Energy efficiency [%]
55
60
)LJXUH 0XOWLREMHFWLYH RSWLPLVDWLRQ UHVXOWV
CO2 capture [%]
Relative competitiveness
1
100 Post−comb. MEA
90
0.8
80 Pre−comb. ATR Selexol
70
0.6
60 50 40
0.4
30 0.2 0 20
20
Pre−comb. BM Selexol
30
40
50
10 60
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