Mixture of Butane, 2-ethoxy-2-methyl- + 1-Butanol

Datasets

1. Mole fraction (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Butane, 2-ethoxy-2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Gas
0.0000	358.05	0.0000
0.0740	358.11	0.2730
0.1230	358.11	0.3780
0.1830	358.10	0.4690
0.2250	358.02	0.5180
0.2730	358.02	0.5620
0.3210	358.14	0.5980
0.3640	358.11	0.6260
0.4020	358.10	0.6480
0.4450	358.07	0.6710
0.4720	358.01	0.6840
0.5140	358.14	0.7030
0.5670	358.14	0.7260
0.6110	358.14	0.7450
0.6550	358.13	0.7630
0.6880	358.16	0.7780
0.7230	358.11	0.7930
0.7610	358.05	0.8120
0.8090	358.09	0.8370
0.8560	358.15	0.8650
0.9220	358.16	0.9140
0.9560	358.12	0.9470
1.0000	358.01	1.0000

Mole fraction of Butane, 2-ethoxy-2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Gas
0.0000	358.05	0.0000
0.0740	358.11	0.2730
0.1230	358.11	0.3780
0.1830	358.10	0.4690
0.2250	358.02	0.5180
0.2730	358.02	0.5620
0.3210	358.14	0.5980
0.3640	358.11	0.6260
0.4020	358.10	0.6480
0.4450	358.07	0.6710
0.4720	358.01	0.6840
0.5140	358.14	0.7030
0.5670	358.14	0.7260
0.6110	358.14	0.7450
0.6550	358.13	0.7630
0.6880	358.16	0.7780
0.7230	358.11	0.7930
0.7610	358.05	0.8120
0.8090	358.09	0.8370
0.8560	358.15	0.8650
0.9220	358.16	0.9140
0.9560	358.12	0.9470
1.0000	358.01	1.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1010	0.1192
0.2005	0.2510
0.3022	0.3788
0.4010	0.4850
0.5023	0.5669
0.6005	0.6131
0.7009	0.6157
0.7999	0.5563
0.9020	0.3819

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1010	0.1192
0.2005	0.2510
0.3022	0.3788
0.4010	0.4850
0.5023	0.5669
0.6005	0.6131
0.7009	0.6157
0.7999	0.5563
0.9020	0.3819

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	358.05	27.40
0.0740	358.11	35.50
0.1230	358.11	39.70
0.1830	358.10	43.80
0.2250	358.02	46.30
0.2730	358.02	48.80
0.3210	358.14	51.10
0.3640	358.11	52.80
0.4020	358.10	54.00
0.4450	358.07	55.30
0.4720	358.01	55.90
0.5140	358.14	57.20
0.5670	358.14	58.30
0.6110	358.14	59.20
0.6550	358.13	59.90
0.6880	358.16	60.50
0.7230	358.11	60.90
0.7610	358.05	61.20
0.8090	358.09	61.70
0.8560	358.15	62.00
0.9220	358.16	62.00
0.9560	358.12	61.70
1.0000	358.01	61.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	358.05	27.40
0.0740	358.11	35.50
0.1230	358.11	39.70
0.1830	358.10	43.80
0.2250	358.02	46.30
0.2730	358.02	48.80
0.3210	358.14	51.10
0.3640	358.11	52.80
0.4020	358.10	54.00
0.4450	358.07	55.30
0.4720	358.01	55.90
0.5140	358.14	57.20
0.5670	358.14	58.30
0.6110	358.14	59.20
0.6550	358.13	59.90
0.6880	358.16	60.50
0.7230	358.11	60.90
0.7610	358.05	61.20
0.8090	358.09	61.70
0.8560	358.15	62.00
0.9220	358.16	62.00
0.9560	358.12	61.70
1.0000	358.01	61.00

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
297.70	0.1010	801.0
297.70	0.2005	796.1
297.70	0.4010	786.6
297.70	0.5023	782.0
297.70	0.9020	764.8
297.71	0.3022	791.1
297.71	0.6005	777.5
297.71	0.7009	773.3
297.71	0.7999	769.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
297.70	0.1010	801.0
297.70	0.2005	796.1
297.70	0.4010	786.6
297.70	0.5023	782.0
297.70	0.9020	764.8
297.71	0.3022	791.1
297.71	0.6005	777.5
297.71	0.7009	773.3
297.71	0.7999	769.2

Sources

• Vapor Liquid Equilibria, Excess Enthalpy, and Excess Volume of Binary Mixtures Containing an Alcohol (1-Butanol, 2-Butanol, or 2-Methyl-2-butanol) and 2-Ethoxy-2-methylbutane