Multi-objective optimization using reduced models in conceptual design of a fuel additive production process

被引：55

作者：

Burger, Jakob ^{[1
]}

Hasse, Hans ^{[1
]}

机构：

[1] Univ Kaiserslautern, Lab Engn Thermodynam, D-67663 Kaiserslautern, Germany

来源：

CHEMICAL ENGINEERING SCIENCE | 2013年 / 99卷

关键词：

Multi-objective optimisation; Pareto optimality; Model reduction; infinity/infinity-analysis; Fuel; Hierarchical design; MULTIPLE STEADY-STATES; POLY(OXYMETHYLENE) DIMETHYL ETHERS; MULTICOMPONENT MIXTURES; AZEOTROPIC DISTILLATION; PHASE-EQUILIBRIUM; PLUS WATER; FORMALDEHYDE; PREDICTIONS; TRIOXANE; METHYLAL;

D O I：

10.1016/j.ces.2013.05.049

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Multi-objective optimization is used for the conceptual design of a new industrial process for the production of poly(oxymethylene) dimethyl ethers (OMEs), which are highly interesting environmentally benign fuel additives. A model based on infinity/infinity-analysis is used for the design. Quantitative measures for the separation effort are introduced in infinity/infinity-analysis and used as objectives. Pareto frontiers are determined for different choices of the design variables and objectives. The design point is chosen based on an exploration of Pareto frontiers. For the studied process the specifications of the product, which is a blend of OMEs of different chain length, are not known a priori. The optimization with the reduced model yields the optimal product composition. (C) 2013 Elsevier Ltd. All rights reserved.

引用

页码：118 / 126

页数：9

共 40 条

[1] Optimal design of an autothermal membrane reactor coupling the dehydrogenation of ethylbenzene to styrene with the hydrogenation of nitrobenzene to aniline [J].

Abo-Ghander, Nabeel S. ;

Logist, Filip ;

Grace, John R. ;

Van Impe, Jan F. M. ;

Elnashaie, Said S. E. H. ;

Lim, C. Jim .

CHEMICAL ENGINEERING SCIENCE, 2010, 65 (10) :3113-3127

[2] New experimental results for the vapor-liquid equilibrium of the binary system (trioxane plus water) and the ternary system (formaldehyde plus trioxane plus water) [J].

Albert, M ;

Hasse, H ;

Kuhnert, C ;

Maurer, G .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (04) :1218-1223

[3]

ANDERSSON J, 2000, TECHNICAL REPORT

[4] Decision Support for Process Development in the Chemical Industry [J].

Asprion, Norbert ;

Blagov, Sergej ;

Ryll, Oliver ;

Welke, Richard ;

Winterfeld, Anton ;

Dittel, Agnes ;

Bortz, Michael ;

Kuefer, Karl-Heinz ;

Burger, Jakob ;

Scheithauer, Andreas ;

Hasse, Hans .

ICHEAP-10: 10TH INTERNATIONAL CONFERENCE ON CHEMICAL AND PROCESS ENGINEERING, PTS 1-3, 2011, 24 :301-+

[5] Simultaneous process and control system design for grade transition in styrene polymerization [J].

Asteasuain, M ;

Bandoni, A ;

Sarmoria, C ;

Brandolin, A .

CHEMICAL ENGINEERING SCIENCE, 2006, 61 (10) :3362-3378

[6]

Azapagic A, 2006, CHEM ENG RES DES, V84, P439, DOI [10.1205/cherd05007, 10.1205/cherd.05007]

[7] Multiple steady states in distillation: infinity/infinity Predictions, extensions, and implications for design, synthesis, and simulation [J].

Bekiaris, N ;

Morari, M .

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (11) :4264-4280

[8] Multi-objective design optimization of a natural gas-combined cycle with carbon dioxide capture in a life cycle perspective [J].

Bernier, Etienne ;

Marechal, Francois ;

Samson, Rejean .

ENERGY, 2010, 35 (02) :1121-1128

[9]

Beyerlein R.A., 2001, STUD SURF SCI CATAL, V134, P3, DOI DOI 10.1016/S0167-2991(04)80023-5

[10]

Bhaskar V, 2000, REV CHEM ENG, V16, P1

← 1 2 3 4 →