Robust optimization of a post-combustion CO2 capture absorber column under process uncertainty

被引:20
作者
Cerrillo-Briones, Ilse M. [1 ]
Ricardez-Sandoval, Luis A. [1 ]
机构
[1] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Robust optimization; CO2; capture; Process uncertainty; Process design; MEA ABSORPTION PROCESSES; MODEL-PREDICTIVE CONTROL; CARBON-DIOXIDE; DYNAMIC SIMULATION; OPTIMAL-DESIGN; OPERATION; PLANT; MONOETHANOLAMINE; GAS;
D O I
10.1016/j.cherd.2019.02.020
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This article presents a study on the optimal design and operation of a pilot-scale absorber column in post-combustion CO2 capture in the presence of uncertainty. A mechanistic model describing the behaviour of a post-combustion CO2 absorber column is explicitly considered in the present robust optimization formulation. This formulation takes into account process uncertainty, which will impact the absorber column operation due to seasonal or unexpected changes in the operating policies of a fossil-fired power plant, e.g. changes in the flue gas stream. Different scenarios were assessed in order to evaluate the impact of uncertainty on the optimal process design and operation. The results show that environmental constraints determine the impact of process uncertainty in the operation of the absorber column. Similarly, the operation of the absorber unit may become infeasible even when process design specifications are estimated under limited information on process uncertainty. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:386 / 396
页数:11
相关论文
共 49 条
[1]   MODEL OF VAPOR LIQUID EQUILIBRIA FOR AQUEOUS ACID GAS ALKANOLAMINE SYSTEMS USING THE ELECTROLYTE NRTL EQUATION [J].
AUSTGEN, DM ;
ROCHELLE, GT ;
PENG, X ;
CHEN, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (07) :1060-1073
[2]   Optimal Design of a Postcombustion CO2 Capture Pilot-Scale Plant under Process Uncertainty: A Ranking-Based Approach [J].
Bahakim, Sami S. ;
Ricardez-Sandoval, Luis A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (15) :3879-3892
[3]   Carbon dioxide capture and storage [J].
Benson, Sally M. ;
Orr, Franklin M., Jr. .
MRS BULLETIN, 2008, 33 (04) :303-305
[4]   Distributional Uncertainty Analysis and Robust Optimization in Spatially Heterogeneous Multiscale Process Systems [J].
Chaffart, Donovan ;
Rasoulian, Shabnam ;
Ricardez-Sandoval, Luis A. .
AICHE JOURNAL, 2016, 62 (07) :2374-2390
[5]   CO2 capture using MEA (monoethanolamine) aqueous solution in coal-fired power plants: Modeling and optimization of the absorbing columns [J].
Chu, Fengming ;
Yang, Lijun ;
Du, Xiaoze ;
Yang, Yongping .
ENERGY, 2016, 109 :495-505
[6]   Systematic Optimization-Based Integrated Chemical Product-Process Design Framework [J].
Cignitti, Stefano ;
Mansouri, Seyed Soheil ;
Woodley, John M. ;
Abildskov, Jens .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (02) :677-688
[7]  
Cost P, 2018, CHEMENGINEERING, V122, P80
[8]  
Dugas R.E., 2006, Pilot plant study of carbon dioxide capture by aqueous monoethanolamine
[9]   Modeling of CO2 capture by aqueous monoethanolamine [J].
Freguia, S ;
Rochelle, GT .
AICHE JOURNAL, 2003, 49 (07) :1676-1686
[10]   Optimization of the Design and Operation of an Extractive Distillation System for the Production of Fuel Grade Ethanol Using Glycerol as Entrainer [J].
Garcia-Herreros, Pablo ;
Gomez, Jorge M. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (07) :3977-3985