A new process for the capture of CO2 and reduction of water salinity

被引:66
作者
El-Naas, Muftah H. [1 ]
Mohammad, Ameera F. [2 ]
Suleiman, Mabruk I. [3 ]
Al Musharfy, Mohamed [3 ]
Al-Marzouqi, Ali H. [2 ]
机构
[1] Qatar Univ, Coll Engn, Gas Proc Ctr, Doha, Qatar
[2] UAE Univ, Chem & Petr Engn Dept, Al Ain, U Arab Emirates
[3] Takreer Res Ctr, Abu Dhabi, U Arab Emirates
关键词
CO2; capture; Water desalination; Solvay process; Sodium bicarbonate; Reject brine; ENERGY REQUIREMENT; ABSORPTION; OPTIMIZATION; AMMONIA;
D O I
10.1016/j.desal.2017.02.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The present work evaluates a new process for the capture of CO2 and the reduction of water salinity. It is based on the Solvay process without the use of ammonia and involves the reaction of CO2 with saline water such as reject brine in the presence of calcium hydroxide. The effects of operating parameters such as reaction temperature, water pH and reaction stoichiometry on CO2 capture efficiency and sodium removal were examined for both traditional and modified Solvay process. The optimum conditions for maximum CO2 capture efficiency and sodium removal were determined using response surface methodology and were found to be at temperature of 20 C-omicron and a pH of greater than 10 for both processes. At the optimum conditions, CO2 capture of 86% and 99% and sodium removal of 29% and 35% were achieved for the traditional Solvay and the Modified process, respectively. The water pH was found to be a key parameter in the effectiveness of the reaction process; higher pH leads to better process performance in both CO2 capture efficiency and sodium removal. The experimental results clearly illustrated that the Modified Solvay process is superior in terms of CO2 capture efficiency, sodium removal and energy consumption. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:69 / 75
页数:7
相关论文
共 39 条
[1]  
[Anonymous], 2007, TRANSPORT PHENOMENA
[2]   Optimization of multi-stage membrane systems for CO2 capture from flue gas [J].
Arias, Ana M. ;
Mussati, Miguel C. ;
Mores, Patricia L. ;
Scenna, Nicolas J. ;
Caballero, Jose A. ;
Mussati, Sergio F. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2016, 53 :371-390
[3]   Removal of CO2 greenhouse gas by ammonia scrubbing [J].
Bai, HL ;
Yeh, AC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (06) :2490-2493
[4]  
Bennaceur K., 2014, Future Energy, VSecond, P583, DOI 10.1016/B978-0-08-099424-6.00026-0
[5]  
Borseth K. E. T., 2007, Method for Desalination of Water and Removal of Carbon Dioxide From Exhaust Gases, Patent No. [US/2007/7309440 B2, 20077309440]
[6]  
Constantz B. R., 2011, Desalination Methods and Systems That Include Carbonate Compound Precipitation, Patent No. [US/2010/7744761 B2, 20107744761]
[7]  
Earnshaw A., 1996, CHEM ELEMENTS
[8]  
El-Naas M. H, 2011, REJECT BRINE MANAGEM
[9]   A combined approach for the management of desalination reject brine and capture of CO2 [J].
El-Naas, Muftah H. ;
Al-Marzouqi, Ali H. ;
Chaalal, Omar .
DESALINATION, 2010, 251 (1-3) :70-74
[10]   Effect of CO2 purity on energy requirement of CO2 capture processes [J].
Goto, Kazuya ;
Kazama, Shingo ;
Furukawa, Atsuyoshi ;
Serizawa, Masahiro ;
Aramaki, Satoshi ;
Shoji, Kazuo .
GHGT-11, 2013, 37 :806-812