Screening of Pure ILs and DESs for CO₂ Separation, N₂O Separation, and H₂S Separation Processes

Table 3

The optimal condition (T_s, P_a), the absorbents amounts (m_abs), and the energy consumption (Q_tot) of the screened absorbents.

Absorbents	CO2 streams	Ts (K)	Pa (bar)	mabs (g∙gX^−1)	Qtot (GJ∙tonX^−1)
[Bmim][DCA]	Effluent gases	299.15–323.15	22.21–178.58	188.41–12.37	1.95–3.16
	Kiln gas	299.15–323.15	12.33–94.60	150.01–10.63	0.99–1.68
	Biomass syngas	299.15–323.15	10.88–97.35	137.70–7.80	0.85–1.39
	Biogas [11]	299.15–323.15	8.75–64.34	124.21–8.64	0.73–1.04
[Eeim][Ac]	Effluent gases	303.15–345.15	29.43–137.96	42.31–8.10	2.48–3.70
	Kiln gas	299.15–345.15	7.81–74.44	141.14–7.33	1.18–2.27
	Biomass syngas	300.15–345.15	8.46–123.37	67.36–5.01	1.10–1.92
	Biogas [11]	299.15–345.15	4.30–59.99	108.11–6.93	0.84–1.82
[Omim][PF6]	High-sulfur natural gas	299.15–323.15	3.97–14.74	290.77–14.72	1.05–1.44
[P66614][FAP]	Adipic acid off-gas	299.15–323.15	6.40–22.71	107.13–6.42	0.65–0.95
[Omim][BF4]	Synthetic ammonia purge [13]	299.15–319.15	3.31–11.06	20.12–257.05	1.05–1.91