Thermal degradation of diethanolamine at stripper condition for CO2 capture: Product types and reaction mechanisms

被引:8
作者
Saeed, Idris Mohamed [1 ]
Ali, Brahim Si [2 ]
Jan, Badrul Mohamed [2 ]
Basirun, Wan Jefrey [1 ]
Mazari, Shaukat Ali [3 ]
Birima, Ibrahim Ali Obid [1 ]
机构
[1] Univ Malaya, Fac Sci, Dept Chem, Kuala Lumpur 50603, Malaysia
[2] Univ Malaya, Fac Engn, Dept Chem Engn, Kuala Lumpur 50603, Malaysia
[3] Dawood Univ Engn & Technol, Fac Engn, Dept Chem Engn, MA Jinnah Rd, Karachi 74800, Pakistan
关键词
Diethanolamine; CO2; capture; Degradation; Mechanism; CARBON-DIOXIDE; ABSORPTION; MONOETHANOLAMINE; EMISSIONS; KINETICS;
D O I
10.1016/j.cjche.2018.09.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Amine-based absorption/stripping is one of the promising technology for CO2 capture from natural and industrial gas streams. During the process, amines and CO2 undergo irreversible reactions to produce undesired compounds, which cause corrosion, foaming, increased viscosity and breakdown of equipment, ultimately contributing to the economic loss and environmental pollution. In this study, the thermal degradation of aqueous diethanolamine in the presence and absence of dissolved CO2 was investigated. The experiments were performed in stainless steel cylinders. The results show that thermal degradation in the absence of CO2 was a slow process: triethanolamine, and tris(2-aminoethyl)amine were only the degradation products identified in the mixture In addition, the rate of degradation was very low, only 3% degradation was observed after 4 weeks. But in the presence of CO2, sixteen degradation products were identified, nine of which were new degradation products reported for the first time in this study. The 3-(2-hydroxyethyl)-2-oxazolidinone, 1,4-bis(2-hydroxyethyl) piperazine and triethanolamine were the most abundant degradation products. The remaining DEA concentration after 4 weeks was about 20% of the total amine concentration. The most probable degradation reactions and their mechanisms are also proposed. (C) 2019 The Chemical Industry and Engineering Society of China,and Chemical Industry Press Co., Ltd. Allrights reserved.
引用
收藏
页码:2900 / 2908
页数:9
相关论文
共 37 条
[1]  
Chakma A., 1987, THESIS
[2]  
Choy E. T., 1978, THESIS
[3]  
Davis J. D., 2009, THESIS
[4]   Thermal Degradation of Aqueous Piperazine for CO2 Capture: 2. Product Types and Generation Rates [J].
Freeman, Stephanie Anne ;
Rochelle, Gary Thomas .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (22) :7726-7735
[5]   Development of a mechanistic model for prediction of CO2 capture from gas mixtures by amine solutions in porous membranes [J].
Ghadiri, Mehdi ;
Marjani, Azam ;
Shirazian, Saeed .
ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH, 2017, 24 (16) :14508-14515
[6]   Effect of piperazine on solubility of carbon dioxide using aqueous diethanolamnie [J].
Ghalib, Lubna ;
Ali, Brahim Si ;
Ashri, Wan Mohd ;
Mazari, Shaukat .
FLUID PHASE EQUILIBRIA, 2016, 414 :1-13
[7]   Amine degradation in CO2 capture. I. A review [J].
Gouedard, C. ;
Picq, D. ;
Launay, F. ;
Carrette, P. -L. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2012, 10 :244-270
[8]  
Gunasekaran P., 2012, FACULTY GRADUATE STU
[9]  
Hakka LE, 1968, GAS PROCESSING CANAD, V61, P32
[10]  
Hilliard M., 2008, A predictive thermodynamic model for an aqueous blend of potassium carbonate, piperazine, and monoethanolamine for carbon dioxide capture from flue gas