Mixture of Diisopropanolamine + Phenol, 3-methyl-

Datasets

1. Mole fraction
2. T_boil(P) - Boiling temperature at pressure P, K

Mole fraction of Phenol, 3-methyl- (2) [ref]

Operational condition: Pressure, kPa = 20 (Liquid)

Mole fraction of Phenol, 3-methyl- (2) - Liquid	Mole fraction of Phenol, 3-methyl- (2) - Gas
1.0000	1.0000
0.9594	0.9968
0.9344	0.9950
0.8969	0.9908
0.8756	0.9894
0.8523	0.9851
0.7965	0.9758
0.7690	0.9698
0.7388	0.9630
0.7075	0.9539
0.6679	0.9405
0.6403	0.9296
0.5566	0.8863
0.5315	0.8661
0.4640	0.8144
0.4489	0.7845
0.3928	0.7358
0.3324	0.6479
0.2675	0.5475
0.2351	0.4821
0.2019	0.4302
0.1593	0.3354
0.1096	0.2403
0.0538	0.1169
0.0000	0.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 20 (Liquid)

Mole fraction of Phenol, 3-methyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	422.28
0.9594	423.66
0.9344	424.57
0.8969	426.04
0.8756	426.73
0.8523	427.67
0.7965	429.36
0.7690	430.78
0.7388	432.07
0.7075	433.64
0.6679	435.36
0.6403	436.28
0.5566	440.37
0.5315	442.27
0.4640	445.56
0.4489	447.15
0.3928	449.56
0.3324	453.46
0.2675	456.27
0.2351	458.82
0.2019	460.09
0.1593	461.87
0.1096	465.01
0.0538	466.45
0.0000	468.25

Sources

• Experimental and Predicted Vapor-Liquid Equilibrium for Diisopropanolamine with m-Cresol and 2,6-Dimethylphenol at 20.0 kPa

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