Efficient Absorption of CO2 by Protic-Ionic-Liquid Based Deep Eutectic Solvents

被引:2
作者
Wen, Shuyue [1 ]
Zhang, Xiaomin [1 ,2 ]
Wu, Youting [1 ,2 ]
机构
[1] Nanjing Univ, Sch Chem & Chem Engn, Key Lab Mesoscop Chem MOE, Nanjing 210023, Peoples R China
[2] Nanjing Univ, Inst Green Chem & Engn, Sch Chem & Chem Engn, Suzhou 212013, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
Ionic liquids; Deep eutectic solvent; Carbon dioxide; Rapid absorption; PRESSURE PHASE-BEHAVIOR; CARBON-DIOXIDE; HIGHLY EFFICIENT; ETHYLENE-GLYCOL; CAPTURE; SOLUBILITY; TEMPERATURE; PERFORMANCE; DESIGN; MDEA;
D O I
10.1002/asia.202400234
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Carbon capture, utilization, and storage (CCUS) are among the key technologies to achieve large-scale carbon emission reduction globally. Deep eutectic solvents (DESs) are considered as designable solvents, which has attracted intensive attention for CO2 capture. Here, a series of binary DESs are synthesized through one-step mixing with the starting materials of protic ionic liquid (PIL) and amine. The eutectic behavior was investigated by measuring the melting point of PILs and amine. The saturated vapor of these DESs and industrial MDEA solution were measured and compared. These DESs are investigated to have high absorption capacity (0.1 g & sdot; g(-1) at 1.0 bar and 25 degrees C), superior apparent absorption rate constant (0.381 min(-1) vs 0.012 min(-1) of 70 wt.% MDEA), moderate interaction with CO2 (the enthalpy change is as low as -34.8 kJ & sdot; mol(-1)). The absorption mechanism is also investigated by NMR analysis. Eight absorption/desorption regeneration experiments are carried out to show their reversibility. Considering the advantages, including convenience of synthesis, large absorption capacity, fast absorption rate, and moderate interaction energy as well as good regeneration, these DESs are believed to be as potential CO2 absorbent in practical applications.
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页数:7
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共 83 条
[1]   Novel solvent properties of choline chloride/urea mixtures [J].
Abbott, AP ;
Capper, G ;
Davies, DL ;
Rasheed, RK ;
Tambyrajah, V .
CHEMICAL COMMUNICATIONS, 2003, (01) :70-71
[2]   High-pressure phase behavior of carbon dioxide with imidazolium-based ionic liquids [J].
Aki, SNVK ;
Mellein, BR ;
Saurer, EM ;
Brennecke, JF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2004, 108 (52) :20355-20365
[3]  
Anthony JL, 2005, J PHYS CHEM B, V109, P6366, DOI 10.1021/jp0464041
[4]   Solubilities and thermodynamic properties of gases in the ionic liquid 1-n-butyl-3-methylimidazolium hexafluorophosphate [J].
Anthony, JL ;
Maginn, EJ ;
Brennecke, JF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2002, 106 (29) :7315-7320
[5]  
Arachchige U.S.P.R., 2013, Annual Transactions of the Nordic Rheology Society, V21, P299
[6]   CO2 capture by a task-specific ionic liquid [J].
Bates, ED ;
Mayton, RD ;
Ntai, I ;
Davis, JH .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2002, 124 (06) :926-927
[7]   High-pressure phase behavior of ionic liquid/CO2 systems [J].
Blanchard, LA ;
Gu, ZY ;
Brennecke, JF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2001, 105 (12) :2437-2444
[8]   Green processing using ionic liquids and CO2 [J].
Blanchard, LA ;
Hancu, D ;
Beckman, EJ ;
Brennecke, JF .
NATURE, 1999, 399 (6731) :28-29
[9]   Why is CO2 so soluble in imidazolium-based ionic liquids? [J].
Cadena, C ;
Anthony, JL ;
Shah, JK ;
Morrow, TI ;
Brennecke, JF ;
Maginn, EJ .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2004, 126 (16) :5300-5308
[10]   Kinetics of CO2 desorption from highly concentrated and CO2-loaded methyldiethanolamine aqueous solutions in the range 312-383 K [J].
Cadours, R ;
Bouallou, C ;
Gaunand, A ;
Richon, D .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (12) :5384-5391