Experimental study on phase change solvents in CO2 capture by NMR spectroscopy

被引:92
作者
Ciftja, Arlinda F. [1 ]
Hartono, Ardi [1 ]
Svendsen, Hallvard F. [1 ]
机构
[1] Norwegian Univ Sci & Technol, N-7491 Trondheim, Norway
关键词
Absorbents; Phases change solvents; Blended systems; NMR; VAPOR-LIQUID-EQUILIBRIA; AMINO-ACID SALTS; CARBON-DIOXIDE; AQUEOUS-SOLUTIONS; ABSORPTION; MONOETHANOLAMINE; METHYLDIETHANOLAMINE; ALKANOLAMINES; SOLUBILITY; MIXTURES;
D O I
10.1016/j.ces.2013.08.036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
2-(Diethylamino)ethanol (DEEA) and 3-(Methylamino) propylamine (MAPA) in combination may represent a promising absorbent system for CO2 capture due to high CO2 loading capacity, high equilibrium temperature sensitivity, low energy requirement for regeneration and relatively high reaction rate. Three different systems: DEEA-CO2-H2O; MAPA-CO2-H2O and DEEA-MAPA-CO2-H2O were studied quantitatively by NMR spectroscopy and the data are reported in the present work. The main products quantified for these systems are: carbonate-bicarbonate for the DEEA-CO2-H2O system; primary, secondary carbamate, dicarbamate for the MAPA-CO2-H2O system, and primary/secondary carbamate, dicarbamate, carbonate/bicarbonate in blended DEEA-MAPA-CO2-H2O. The special:ion data of the three systems were measured and reported in the present work. The blended system of 5 M DEEA-2 M MAPA can form two liquid phases after being loaded with CO2 and both phases were analyzed quantitatively by NMR spectroscopy. The experimental data shows that the lower phase is rich in CO2 and MAPA while the upper phase was lean in CO2 and rich in DEEA. The ratio DEEA-MAPA in the lower phase increases with increasing partial pressure whereas tot the upper phase the opposite is true. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:378 / 386
页数:9
相关论文
共 39 条
[1]   Physical and Chemical Properties of DMX™ Solvents [J].
Aleixo, Marco ;
Prigent, Monique ;
Gibert, Alexendre ;
Porcheron, Fabien ;
Mokbel, Ilham ;
Jose, Jacques ;
Jacquin, Marc .
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 :148-155
[2]  
[Anonymous], EM GAP REP
[3]  
[Anonymous], THESIS NORWEGIAN U S
[4]   Investigation of amine amino acid salts for carbon dioxide absorption [J].
Aronu, Ugochukwu E. ;
Svendsen, Hallvard F. ;
Hoff, Karl Anders .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2010, 4 (05) :771-775
[5]   Heat of Absorption of CO2 in Aqueous Solutions of DEEA, MAPA and their Mixture [J].
Arshad, Muhammad Waseem ;
von Solms, Nicolas ;
Thomsen, Kaj ;
Svendsen, Hallvard Fjosne .
GHGT-11, 2013, 37 :1532-1542
[6]  
Astarita G, 1983, GAS TREATING CHEM SO
[7]   MODEL OF VAPOR-LIQUID-EQUILIBRIA FOR AQUEOUS ACID GAS-ALKANOLAMINE SYSTEMS .2. REPRESENTATION OF H2S AND CO2 SOLUBILITY IN AQUEOUS MDEA AND CO2 SOLUBILITY IN AQUEOUS MIXTURES OF MDEA WITH MEA OR DEA [J].
AUSTGEN, DM ;
ROCHELLE, GT ;
CHEN, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (03) :543-555
[8]   A 13C NMR investigation of CO2 absorption and desorption in aqueous 2,2′-iminodiethanol and N-methyl-2,2′-iminodiethanol [J].
Barzagli, Francesco ;
Mani, Fabrizio ;
Peruzzini, Maurizio .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2011, 5 (03) :448-456
[9]   Continuous cycles of CO2 absorption and amine regeneration with aqueous alkanolamines: a comparison of the efficiency between pure and blended DEA, MDEA and AMP solutions by 13C NMR spectroscopy [J].
Barzagli, Francesco ;
Mani, Fabrizio ;
Peruzzini, Maurizio .
ENERGY & ENVIRONMENTAL SCIENCE, 2010, 3 (06) :772-779
[10]   Thermodynamics of piperazine/methyldiethanolamine/water/carbon dioxide [J].
Bishnoi, S ;
Rochelle, GT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (03) :604-612