Mixture of Ethanol + Diethyl sulfide

Datasets

1. Azeotropic composition: mole fraction (8)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. Vapor or sublimation pressure, kPa (2)

Azeotropic composition: mole fraction of Diethyl sulfide (2) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Diethyl sulfide (2) - Liquid
343.15	0.3720

Azeotropic composition: mole fraction of Diethyl sulfide (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Diethyl sulfide (2) - Liquid
88.40	0.3720

Mole fraction of Diethyl sulfide (2) [ref]

Operational condition: Temperature, K = 343.15 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Mole fraction of Diethyl sulfide (2) - Gas
0.0000	0.0000
0.0240	0.0630
0.0450	0.1070
0.0850	0.1740
0.1410	0.2370
0.2070	0.2880
0.2870	0.3360
0.3890	0.3780
0.5080	0.4220
0.6480	0.4730
0.7990	0.5530
0.9260	0.7140
0.9910	0.9430
1.0000	1.0000

Mole fraction of Diethyl sulfide (2) [ref]

Operational condition: Temperature, K = 343.13 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Mole fraction of Diethyl sulfide (2) - Gas
0.0000	0.0000
0.0270	0.0690
0.0630	0.1390
0.1100	0.2040
0.1480	0.2440
0.2430	0.3170
0.3210	0.3620
0.3680	0.3750
0.4440	0.4070
0.6490	0.4830
0.7610	0.5410
0.9020	0.6600
0.9640	0.8110
0.9790	0.8850
1.0000	1.0000

Azeotropic composition: mole fraction of Diethyl sulfide (2) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Diethyl sulfide (2) - Liquid
343.15	0.3720

Azeotropic composition: mole fraction of Diethyl sulfide (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Diethyl sulfide (2) - Liquid
88.40	0.3720

Mole fraction of Diethyl sulfide (2) [ref]

Operational condition: Temperature, K = 343.15 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Mole fraction of Diethyl sulfide (2) - Gas
0.0000	0.0000
0.0240	0.0630
0.0450	0.1070
0.0850	0.1740
0.1410	0.2370
0.2070	0.2880
0.2870	0.3360
0.3890	0.3780
0.5080	0.4220
0.6480	0.4730
0.7990	0.5530
0.9260	0.7140
0.9910	0.9430
1.0000	1.0000

Mole fraction of Diethyl sulfide (2) [ref]

Operational condition: Temperature, K = 343.13 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Mole fraction of Diethyl sulfide (2) - Gas
0.0000	0.0000
0.0270	0.0690
0.0630	0.1390
0.1100	0.2040
0.1480	0.2440
0.2430	0.3170
0.3210	0.3620
0.3680	0.3750
0.4440	0.4070
0.6490	0.4830
0.7610	0.5410
0.9020	0.6600
0.9640	0.8110
0.9790	0.8850
1.0000	1.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.15 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	72.50
0.0240	75.60
0.0450	78.00
0.0850	81.50
0.1410	84.60
0.2070	86.80
0.2870	88.10
0.3890	88.50
0.5080	87.70
0.6480	85.00
0.7990	79.00
0.9260	66.10
0.9910	52.70
1.0000	50.10

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.15 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	72.50
0.0240	75.60
0.0450	78.00
0.0850	81.50
0.1410	84.60
0.2070	86.80
0.2870	88.10
0.3890	88.50
0.5080	87.70
0.6480	85.00
0.7990	79.00
0.9260	66.10
0.9910	52.70
1.0000	50.10

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.13 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	72.00
0.0270	75.30
0.0630	79.80
0.1100	82.50
0.1480	84.80
0.2430	87.10
0.3210	87.80
0.3680	88.30
0.4440	87.70
0.6490	84.70
0.7610	81.10
0.9020	70.70
0.9640	60.80
0.9790	56.30
1.0000	49.70

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.13 (Liquid)

Mole fraction of Diethyl sulfide (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	72.00
0.0270	75.30
0.0630	79.80
0.1100	82.50
0.1480	84.80
0.2430	87.10
0.3210	87.80
0.3680	88.30
0.4440	87.70
0.6490	84.70
0.7610	81.10
0.9020	70.70
0.9640	60.80
0.9790	56.30
1.0000	49.70

Sources

• Phase equilibria on binary systems containing diethyl sulfide
• An improved static-analytic apparatus for vapor-liquid equilibrium (PTxy) measurement using modified in-situ samplers