Study on the Regeneration of Basic Aluminum Sulfate SO2-Rich Solution by Vacuum Desorption

被引:17
作者
Chen, Min [1 ]
Deng, Xianhe [1 ]
He, Feiqiang [1 ]
机构
[1] South China Univ Technol, Dept Chem & Chem Engn, Guangzhou 510640, Guangdong, Peoples R China
关键词
TRANSPORT MEMBRANE MODULE; FLUE-GAS DESULFURIZATION; ABSORPTION; SO2; CO2; PERMEATION; TECHNOLOGY; ULTRASOUND; SEPARATION; CARBONATE;
D O I
10.1021/acs.energyfuels.6b01110
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Basic aluminum sulfate (BAS) wet flue gas desulfurization (FGD) is a promising renewable process used to remove sulfur dioxide (SO2) from flue gas, in which the regeneration of BAS SO2-loaded solution is of great importance for the reuse of BAS solution. In this paper, a novel regeneration method by vacuum desorption was developed to achieve superior regeneration performance for a BAS-rich solution. The operating parameter effect on SO2 desorption performance was thoroughly investigated in a lab-scale reactor. The experimental results demonstrated that the great decrease of pressure could significantly improve the regeneration performance, and high desorption temperature was favorable for SO2 desorption. Furthermore, it is worth determining the optimum components of a BAS-rich solution and initial sulfite concentration, considering the contradiction between the SO2 absorption performance and the regeneration performance. The increase of stirring speed in the liquid had a considerable positive effect on SO2 desorption efficiency. In addition, through a simple comparison with direct heating regeneration, it indicates that the utilization of vacuum regeneration could have the potential to improve the regeneration rate and lower the total energy consumption. Finally, the recycling experiments of the absorption desorption process show that the BAS solution could be reused successfully to capture SO2 from flue gas by vacuum regeneration, while SO2 absorption efficiency would decrease to below 90% after 11 cycles, attributed to the inevitable oxidation of byproduct in the desulfurization process.
引用
收藏
页码:8469 / 8478
页数:10
相关论文
共 32 条
[1]  
Barwasser J., 1943, U.S. Patent, Patent No. [2,311,202A, 2311202]
[2]   Removal of SO2 from Flue Gas Using Basic Aluminum Sulfate Solution with the Byproduct Oxidation Inhibition by Ethylene Glycol [J].
Chen, Min ;
Deng, Xianhe ;
He, Feigiang .
ENERGY & FUELS, 2016, 30 (02) :1183-1191
[3]  
Earl C., 1974, U.S. Patent, Patent No. [3,790,660 A, 3790660]
[4]   Influence of viscosity and surface tension on performance of gas-liquid contactors with ejector type gas distributor [J].
Elgozali, A ;
Linek, V ;
Fialová, M ;
Wein, O ;
Zahradník, J .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (15) :2987-2994
[5]   CO2 desorption from rich alkanolamine solution by using membrane vacuum regeneration technology [J].
Fang, Mengxiang ;
Wang, Zhen ;
Yan, Shuiping ;
Cen, Qigang ;
Luo, Zhongyang .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2012, 9 :507-521
[6]   Carbon dioxide recovery from post-combustion processes: Can gas permeation membranes compete with absorption? [J].
Favre, Eric .
JOURNAL OF MEMBRANE SCIENCE, 2007, 294 (1-2) :50-59
[7]   Reversible physical absorption of SO2 by ionic liquids [J].
Huang, Jun ;
Riisager, Anders ;
Wasserscheid, Peter ;
Fehrmann, Rasmus .
CHEMICAL COMMUNICATIONS, 2006, (38) :4027-4029
[8]   Comparative Study of the Solubilities of SO2 in Five Low Volatile Organic Solvents (Sulfolane, Ethylene Glycol, Propylene Carbonate, N-Methylimidazole, and N-Methylpyrrolidone) [J].
Huang, Kuan ;
Xia, Shuang ;
Zhang, Xiao-Min ;
Chen, Yong-Le ;
Wu, You-Ting ;
Hu, Xing-Bang .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2014, 59 (04) :1202-1212
[9]   Evaluation of energy consumption for separation of CO2 in flue gas by hollow fiber facilitated transport membrane module with permeation of amine solution [J].
Matsumiya, N ;
Teramoto, M ;
Kitada, S ;
Matsuyama, H .
SEPARATION AND PURIFICATION TECHNOLOGY, 2005, 46 (1-2) :26-32
[10]  
Midkiff L. A., 1979, POWER, V6, P103