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Direct Air Capture of CO(2) Using a Liquid Amine–Solid Carbamic Acid Phase-Separation System Using Diamines Bearing an Aminocyclohexyl Group
[Image: see text] The phase separation between a liquid amine and the solid carbamic acid exhibited >99% CO(2) removal efficiency under a 400 ppm CO(2) flow system using diamines bearing an aminocyclohexyl group. Among them, isophorone diamine [IPDA; 3-(aminomethyl)-3,5,5-trimethylcyclohexylamine...
Autores principales: | , , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American Chemical Society
2022
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10125313/ https://www.ncbi.nlm.nih.gov/pubmed/37101968 http://dx.doi.org/10.1021/acsenvironau.1c00065 |
Sumario: | [Image: see text] The phase separation between a liquid amine and the solid carbamic acid exhibited >99% CO(2) removal efficiency under a 400 ppm CO(2) flow system using diamines bearing an aminocyclohexyl group. Among them, isophorone diamine [IPDA; 3-(aminomethyl)-3,5,5-trimethylcyclohexylamine] exhibited the highest CO(2) removal efficiency. IPDA reacted with CO(2) in a CO(2)/IPDA molar ratio of ≥1 even in H(2)O as a solvent. The captured CO(2) was completely desorbed at 333 K because the dissolved carbamate ion releases CO(2) at low temperatures. The reusability of IPDA under CO(2) adsorption-and-desorption cycles without degradation, the >99% efficiency kept for 100 h under direct air capture conditions, and the high CO(2) capture rate (201 mmol/h for 1 mol of amine) suggest that the phase separation system using IPDA is robust and durable for practical use. |
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