SYNTHESIS OF FLEXIBLE THERMALLY INTEGRATED DISTILLATION SEQUENCES

被引：0

作者：

DOUGLAS, PL ^{[1
]}

MALLICK, SK ^{[1
]}

WAGLER, RM ^{[1
]}

机构：

[1] ONTARIO HYDRO,TORONTO,ONTARIO,CANADA

来源：

CHEMICAL ENGINEERING RESEARCH & DESIGN | 1991年 / 69卷 / A6期

关键词：

D O I：

暂无

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A method has been developed to synthesize thermally integrated distillation sequences under conditions of uncertainty. The method minimizes the expected annual cost of the sequence and guarantees feasible operation over the entire uncertain parameter space by using an approach termed 'practical feasibility'. Results are presented which show the effect of uncertainty in feed flowrate, stage efficiency, K-value and heat transfer coefficient on sequence cost and structure for a 5 component light alkane system. The inclusion of uncertainty significantly reduces the cost savings accrued through heat integration because of the increased size of trim reboilers and condensers included to guarantee flexibility.

引用

页码：483 / 491

页数：9

共 50 条

[21] Generalized modular framework for the synthesis of heat integrated distillation column sequences
Centre for Process Systems Engineering, Department of Chemical Engineering, Imperial College London, London, United Kingdom
[J]. 1600, 4678-4701 (September 2005):
[22] Matrix based method for synthesis of main intensified and integrated distillation sequences
Amirhossein Khalili-Garakani
Javad Ivakpour
Norollah Kasiri
[J]. Korean Journal of Chemical Engineering, 2016, 33 : 1134 - 1152
[23] Synthesis of heat-integrated thermally coupled distillation systems for multicomponent separations
Rong, BG
Kraslawski, A
Turunen, I
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (19) : 4329 - 4339
[24] Reactive Thermally Coupled Distillation Sequences: Pareto Front
Yair Miranda-Galindo, Erick
Gabriel Segovia-Hernandez, Juan
Hernandez, Salvador
Gutierrez-Antonio, Claudia
Briones-Ramirez, Abel
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (02) : 926 - 938
[25] Strategies for the robust simulation of thermally coupled distillation sequences
Navarro, Miguel A.
Javaloyes, Juan
Caballero, Jose A.
Grossmann, Ignacio E.
[J]. COMPUTERS & CHEMICAL ENGINEERING, 2012, 36 : 149 - 159
[26] Strategies for the Robust Simulation of Thermally Coupled Distillation Sequences
Navarro, Miguel A.
Caballero, Jose A.
Grossmann, Ignacio E.
[J]. 21ST EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, 2011, 29 : 196 - 200
[27] Design and Optimization of Thermally Coupled Extractive Distillation Sequences
Gutierrez-Guerra, Roberto
Segovia-Hernandez, Juan-Gabriel
Hernandez, Salvador
Bonilla-Petriciolet, Adrian
Hernandez, Hector
[J]. 19TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, 2009, 26 : 189 - 194
[28] Comparison of energy consumptions and total annual costs between heat integrated and thermally linked distillation sequences
Hernández-Gaona, CG
Hernández, S
[J]. CHEMICAL AND BIOCHEMICAL ENGINEERING QUARTERLY, 2004, 18 (02) : 137 - 143
[29] Design of distillation sequences: from conventional to fully thermally coupled distillation systems
Caballero, JA
Grossmann, IE
[J]. COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (11) : 2307 - 2329
[30] A decomposed approach to the synthesis of heat integrated distillation sequences using mathematical programming
Sandoval, S
Zhu, XX
[J]. 1996 ICHEME RESEARCH EVENT - SECOND EUROPEAN CONFERENCE FOR YOUNG RESEARCHERS IN CHEMICAL ENGINEERING, VOLS 1 AND 2, 1996, : 721 - 723

← 1 2 3 4 5 →