Mixture of Monoethanolamine + 2-Propanol, 1-methoxy-

Datasets

1. P_vap - Vapor or sublimation pressure, kPa

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
373.15	1.0000	6.64
373.15	0.9755	7.72
373.15	0.9501	9.41
373.15	0.9271	10.59
373.15	0.9039	12.81
373.15	0.8564	15.55
373.15	0.8077	18.12
373.15	0.7590	20.32
373.15	0.7089	23.04
373.15	0.6581	25.49
373.15	0.6073	27.78
373.15	0.5700	30.32
373.15	0.5575	30.24
373.15	0.5203	32.20
373.15	0.5071	32.85
373.15	0.4692	33.95
373.15	0.4557	34.90
373.15	0.4181	35.76
373.15	0.3661	37.51
373.15	0.3148	39.17
373.15	0.2629	40.93
373.15	0.2109	42.72
373.15	0.1582	44.70
373.15	0.1058	46.67
373.15	0.0791	47.77
373.15	0.0532	48.49
373.15	0.0273	50.07
373.15	0.0000	50.45
423.15	1.0000	51.97
423.15	0.9759	58.49
423.15	0.9508	66.05
423.15	0.9280	72.22
423.15	0.9050	78.71
423.15	0.8577	90.05
423.15	0.8092	97.46
423.15	0.7605	107.11
423.15	0.7103	117.09
423.15	0.6594	127.24
423.15	0.6084	136.45
423.15	0.5706	141.03
423.15	0.5584	146.10
423.15	0.5209	152.74
423.15	0.5078	153.12
423.15	0.4699	160.70
423.15	0.4562	162.07
423.15	0.4189	167.43
423.15	0.3670	174.10
423.15	0.3157	182.52
423.15	0.2638	191.31
423.15	0.2117	198.86
423.15	0.1589	207.68
423.15	0.1064	215.96
423.15	0.0795	221.36
423.15	0.0535	225.12
423.15	0.0275	229.28
423.15	0.0000	232.93

Sources

• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation

Note: These property values are available through the Cheméo API. A free account gives you an access key.