Design and sustainability analysis of a combined CO2 mineralization and desalination process

被引:8
作者
Oh, Jaewoo [1 ]
Jung, Dabin [2 ]
Oh, S. H. [1 ]
Roh, Kosan [1 ]
Chung, Jane [3 ]
Han, Jong-In [3 ]
Lee, Jay. H. [1 ]
机构
[1] Korea Adv Inst Sci & Technol, Dept Chem & Biomol Engn, Daejeon 34141, South Korea
[2] LG Chem, R&D Campus Daejeon, Daejeon 34122, South Korea
[3] Korea Adv Inst Sci & Technol, Dept Civil & Environm Engn, Daejeon 34141, South Korea
关键词
Process modeling and identification; Sustainability study; CO2; mineralization; Desalination; Techno-economic analysis; CO2 lifecycle assessment;
D O I
10.1016/j.ifacol.2018.09.259
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
CO2 mineralization sequestrates CO2 in a form of mineral carbonate through chemical reactions of CO2 with metal oxide or alkaline solution. This process is attractive because it has no risk for a leakage of hazardous materials and requires a relatively small area for sequestrating CO2 compared to geological storage. In addition, generated mineral carbonate can be used as useful chemicals if its purity is high enough. One of the recent ideas in CO2 mineralization is integrating it with desalination Mineral ions needed for the CO2 mineralization are separated from seawater, and generated deionized seawater is used as a feed to a desalination process, such as reverse osmosis (RO), to reduce its electric energy load. The goal of this study is to design the proposed process and examine its sustainability. The overall process is designed and simulated using Aspen plus (R) and Matlab. Based on the simulation results, techno-economic analysis (TEA) and CO2 lifecycle assessment (CO2 LCA) are conducted to verify the sustainability. In order to identify the improvement potential of the process, a best scenario study is performed. It turns out that this process can achieve about 230tonne CO2 reduction/yr as well as relative economic benefit of almost lmillion $/yr compared to a benchmark process which comprises the standalone Solvay process and RO. From the best scenario result, it can be concluded that the proposed process has the potential for further investigation as means to reduce the CO2 emission while generating economic benefits. (C) 2018, IFAC (International Federation of Automatic Control) Hosting by Elsevier Ltd. All rights reserved.
引用
收藏
页码:85 / 90
页数:6
相关论文
共 23 条
[1]  
Agency U. E. P., 2010, LIF CYCL ASS LCA
[2]   Electrodeionization: Principles, Strategies and Applications [J].
Alvarado, Lucia ;
Chen, Aicheng .
ELECTROCHIMICA ACTA, 2014, 132 :583-597
[3]  
[Anonymous], 2013, IPCC CLIMATE CHANGE
[4]  
Aspentech, 2008, RAT BAS MOD CO2 CAPT
[5]  
BIO-RAD, AG 50W AG MP 50 CAT
[6]  
Bruckner T., 2014, IPCC WORKING GROUP 3
[7]   REACTOR ANALYSIS OF A CHLOR ALKALI MEMBRANE CELL [J].
CHANDRAN, RR ;
CHIN, DT .
ELECTROCHIMICA ACTA, 1986, 31 (01) :39-50
[8]   Generalized electrolyte-NRTL model for mixed-solvent electrolyte systems [J].
Chen, CC ;
Song, YH .
AICHE JOURNAL, 2004, 50 (08) :1928-1941
[9]   Comparison of adsorption equilibrium models for the study of CL-, NO3- and SO42- removal from aqueous solutions by an anion exchange resin [J].
Dron, Julien ;
Dodi, Alain .
JOURNAL OF HAZARDOUS MATERIALS, 2011, 190 (1-3) :300-307
[10]   Using user models in Matlab® within the Aspen Plus® interface with an Excel® link [J].
Fontalvo, J. .
INGENIERIA E INVESTIGACION, 2014, 34 (02) :39-43