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Ionic Liquid Mixtures for Direct Air Capture: High CO(2) Permeation Driven by Superior CO(2) Absorption with Lower Absolute Enthalpy

[Image: see text] This paper reports a series of liquid materials suitable for use as high-performance separation membranes in direct air capture. Upon mixing two ionic liquids (ILs), namely N-(2-aminoethyl)ethanolamine-based IL ([AEEA][X]) and 1-ethyl-3-methylimidazolium acetate ([emim][AcO]), the...

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Detalles Bibliográficos
Autores principales: Kohno, Yuki, Kanakubo, Mitsuhiro, Iwaya, Masao, Yamato, Yo, Makino, Takashi
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2022
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9685769/
https://www.ncbi.nlm.nih.gov/pubmed/36440108
http://dx.doi.org/10.1021/acsomega.2c04756
Descripción
Sumario:[Image: see text] This paper reports a series of liquid materials suitable for use as high-performance separation membranes in direct air capture. Upon mixing two ionic liquids (ILs), namely N-(2-aminoethyl)ethanolamine-based IL ([AEEA][X]) and 1-ethyl-3-methylimidazolium acetate ([emim][AcO]), the resulting mixtures with a specific range of their composition showed higher CO(2) absorption rates, larger CO(2) solubilities, and lower absolute enthalpies of CO(2) absorption compared to those of single ILs. NMR spectroscopy of the IL mixture after exposure to (13)CO(2) allowed elucidation of the chemisorbed species, wherein [AEEA][X] reacts with CO(2) to form CO(2)–[AEEA](+) complexes stabilized by hydrogen bonding with acetate anions. Supported IL membranes composed of [AEEA][X]/[emim][AcO] mixtures were then fabricated, and the membrane with a suitable mixing ratio showed a CO(2) permeability of 25,983 Barrer and a CO(2)/N(2) selectivity of 10,059 at 313.2 K and an applied CO(2) partial pressure of 40 Pa without water vapor. These values are higher than those reported for known facilitated transport membranes.