Mixture of Butane, 2-ethoxy-2-methyl- + Amylene hydrate

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	358.12	0.0000
0.1210	358.10	0.2070
0.1610	358.03	0.2580
0.2020	358.02	0.3050
0.2530	358.06	0.3570
0.2960	358.11	0.3950
0.3410	358.11	0.4320
0.3790	358.12	0.4610
0.4170	358.06	0.4890
0.4550	358.02	0.5150
0.4900	358.10	0.5380
0.5260	358.10	0.5620
0.5600	358.09	0.5840
0.5920	358.10	0.6040
0.6220	358.11	0.6240
0.6490	358.10	0.6410
0.7040	358.10	0.6790
0.7330	358.10	0.6990
0.7690	358.13	0.7270
0.8040	358.12	0.7550
0.8370	358.04	0.7840
0.8680	358.03	0.8150
0.8980	358.09	0.8480
0.9330	358.06	0.8910
0.9640	358.09	0.9360
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	358.12	0.0000
0.1210	358.10	0.2070
0.1610	358.03	0.2580
0.2020	358.02	0.3050
0.2530	358.06	0.3570
0.2960	358.11	0.3950
0.3410	358.11	0.4320
0.3790	358.12	0.4610
0.4170	358.06	0.4890
0.4550	358.02	0.5150
0.4900	358.10	0.5380
0.5260	358.10	0.5620
0.5600	358.09	0.5840
0.5920	358.10	0.6040
0.6220	358.11	0.6240
0.6490	358.10	0.6410
0.7040	358.10	0.6790
0.7330	358.10	0.6990
0.7690	358.13	0.7270
0.8040	358.12	0.7550
0.8370	358.04	0.7840
0.8680	358.03	0.8150
0.8980	358.09	0.8480
0.9330	358.06	0.8910
0.9640	358.09	0.9360
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
0.1005	0.2362
0.2006	0.4480
0.3013	0.6323
0.4018	0.7813
0.5013	0.8937
0.6010	0.9611
0.7003	0.9727
0.8011	0.9002
0.9003	0.6636

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
0.1005	0.2362
0.2006	0.4480
0.3013	0.6323
0.4018	0.7813
0.5013	0.8937
0.6010	0.9611
0.7003	0.9727
0.8011	0.9002
0.9003	0.6636

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	358.12	52.80
0.1210	358.10	59.30
0.1610	358.03	60.70
0.2020	358.02	62.20
0.2530	358.06	63.90
0.2960	358.11	65.10
0.3410	358.11	66.10
0.3790	358.12	66.80
0.4170	358.06	67.30
0.4550	358.02	67.60
0.4900	358.10	68.10
0.5260	358.10	68.50
0.5600	358.09	68.60
0.5920	358.10	68.80
0.6220	358.11	68.80
0.6490	358.10	68.80
0.7040	358.10	68.50
0.7330	358.10	68.40
0.7690	358.13	68.10
0.8040	358.12	67.60
0.8370	358.04	66.80
0.8680	358.03	66.10
0.8980	358.09	65.40
0.9330	358.06	64.00
0.9640	358.09	62.80
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	358.12	52.80
0.1210	358.10	59.30
0.1610	358.03	60.70
0.2020	358.02	62.20
0.2530	358.06	63.90
0.2960	358.11	65.10
0.3410	358.11	66.10
0.3790	358.12	66.80
0.4170	358.06	67.30
0.4550	358.02	67.60
0.4900	358.10	68.10
0.5260	358.10	68.50
0.5600	358.09	68.60
0.5920	358.10	68.80
0.6220	358.11	68.80
0.6490	358.10	68.80
0.7040	358.10	68.50
0.7330	358.10	68.40
0.7690	358.13	68.10
0.8040	358.12	67.60
0.8370	358.04	66.80
0.8680	358.03	66.10
0.8980	358.09	65.40
0.9330	358.06	64.00
0.9640	358.09	62.80
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	0.1005	798.8
297.71	0.2006	793.2
297.71	0.3013	788.2
297.71	0.4018	783.4
297.71	0.5013	778.9
297.71	0.6010	774.7
297.71	0.7003	770.9
297.71	0.8011	767.1
297.72	0.9003	763.7

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	0.1005	798.8
297.71	0.2006	793.2
297.71	0.3013	788.2
297.71	0.4018	783.4
297.71	0.5013	778.9
297.71	0.6010	774.7
297.71	0.7003	770.9
297.71	0.8011	767.1
297.72	0.9003	763.7

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