Cross-Linking Amine-Rich Compounds into High Performing Selective CO2 Absorbents

被引:42
|
作者
Andreoli, Enrico [1 ,2 ]
Dillon, Eoghan P. [1 ]
Cullum, Laurie [1 ]
Alemany, Lawrence B. [1 ,3 ]
Barron, Andrew R. [1 ,2 ,4 ]
机构
[1] Rice Univ, Dept Chem, Houston, TX 77005 USA
[2] Swansea Univ, Coll Engn, Energy Safety Res Inst, Swansea SA2 8PP, W Glam, Wales
[3] Rice Univ, Shared Equipment Author, Houston, TX 77005 USA
[4] Rice Univ, Dept Mat Sci & Nanoengn, Houston, TX 77005 USA
来源
SCIENTIFIC REPORTS | 2014年 / 4卷
关键词
CARBON-DIOXIDE CAPTURE; CHEMICAL-SHIFT STANDARDS; NATURAL-GAS; FLUE-GAS; POLYETHYLENEIMINE; ADSORPTION; SORBENTS; REMOVAL; AIR;
D O I
10.1038/srep07304
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
Amine-based absorbents play a central role in CO2 sequestration and utilization. Amines react selectively with CO2, but a drawback is the unproductive weight of solvent or support in the absorbent. Efforts have focused on metal organic frameworks (MOFs) reaching extremely high CO2 capacity, but limited selectivity to N-2 and CH4, and decreased uptake at higher temperatures. A desirable system would have selectivity (cf. amine) and high capacity (cf. MOF), but also increased adsorption at higher temperatures. Here, we demonstrate a proof-of-concept where polyethyleneimine (PEI) is converted to a high capacity and highly selective CO2 absorbent using buckminsterfullerene (C-60) as a cross-linker. PEI-C-60 (CO2 absorption of 0.14 g/g at 0.1 bar/90 degrees C) is compared to one of the best MOFs, Mg-MOF-74 (0.06 g/g at 0.1 bar/90 degrees C), and does not absorb any measurable amount of CH4 at 50 bar. Thus, PEI-C-60 can perform better than MOFs in the sweetening of natural gas.
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页数:5
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