Non-aqueous liquid-liquid phase-change absorbent for capturing carbon dioxide and application of non-aqueous liquid-liquid phase-change absorbent
A carbon dioxide and absorbent technology, applied in the field of non-aqueous liquid-liquid phase-change absorbents, can solve the problems of unfavorable absorbent recycling, slow mass transfer of the absorption system, and difficult pipeline transportation, etc. Sensible heat and latent heat, low corrosion effect
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Embodiment 1
[0033] A non-aqueous liquid-liquid phase-change absorbent for carbon dioxide capture, according to the concentration of hydroxyethylethylenediamine (AEEA) is 0.5mol / L, composite organic solvents dimethyl sulfoxide (DMSO) and pentamethyl The volume ratio of diethylenetriamine (PMDETA) is 6:4, and it is formulated into AEEA-DMSO-PMDETA ternary non-aqueous liquid-liquid phase change absorbent.
[0034] The non-aqueous liquid-liquid phase change absorbent is used to absorb CO with a volume ratio of 5% to 20% in the mixed gas 2 , The absorption temperature is 30℃~60℃.
[0035] After the absorbent is saturated, a liquid-liquid phase transition occurs, and the CO 2 Rich phase and CO 2 The lean phase is separated and regenerated by thermal desorption. The regeneration temperature is 100°C-120°C and the regeneration time is 10min-30min.
Embodiment 2
[0037] A non-aqueous liquid-liquid phase-change absorbent for carbon dioxide capture, except that the concentration of hydroxyethylethylenediamine is 1.5mol / L, and the volume ratio of dimethylsulfoxide and pentamethyldiethylenetriamine is 5: 5, all the other are identical with embodiment 1.
Embodiment 3
[0039] A non-aqueous liquid-liquid phase-change absorbent for carbon dioxide capture, with a concentration of 1 mol / L in addition to hydroxyethylethylenediamine, and a volume ratio of dimethylsulfoxide and pentamethyldiethylenetriamine of 4:6 , all the other are identical with embodiment 1.
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