Mixture of Propane, 2-methoxy-2-methyl- + Methyl Alcohol

Datasets

1. η - Viscosity, Pa*s (2)
2. P_c - Critical pressure, kPa (2)
3. ρ_l - Mass density, kg/m3 (4)
4. T_c - Critical temperature, K (2)

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Viscosity, Pa*s - Liquid
0.0512	0.0005
0.0994	0.0005
0.1991	0.0005
0.3011	0.0005
0.4015	0.0004
0.4993	0.0004
0.6001	0.0004
0.7001	0.0004
0.8007	0.0004
0.8998	0.0004
0.9494	0.0004

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Viscosity, Pa*s - Liquid
0.0512	0.0005
0.0994	0.0005
0.1991	0.0005
0.3011	0.0005
0.4015	0.0004
0.4993	0.0004
0.6001	0.0004
0.7001	0.0004
0.8007	0.0004
0.8998	0.0004
0.9494	0.0004

Critical pressure, kPa [ref]

Mole fraction of Methyl Alcohol (2) - Liquid	Critical pressure, kPa - Liquid
0.0000	3448.00
0.1231	3897.00
0.2007	4152.00
0.3001	4583.00
0.3997	4926.00
0.5003	5281.00
0.6003	5605.00
0.7002	6124.00
0.8001	6648.00
0.9000	7287.00
1.0000	8128.00

Critical pressure, kPa [ref]

Mole fraction of Methyl Alcohol (2) - Liquid	Critical pressure, kPa - Liquid
0.0000	3448.00
0.1231	3897.00
0.2007	4152.00
0.3001	4583.00
0.3997	4926.00
0.5003	5281.00
0.6003	5605.00
0.7002	6124.00
0.8001	6648.00
0.9000	7287.00
1.0000	8128.00

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0100	790.62
293.15	0.0201	789.69
293.15	0.0301	788.74
293.15	0.0402	787.83
293.15	0.0502	786.96
293.15	0.0601	786.1
293.15	0.0696	785.32
293.15	0.0799	784.47
293.15	0.0888	783.72
293.15	0.1008	782.79
293.15	0.1498	779.11
293.15	0.1945	776.01
293.15	0.2600	771.99
293.15	0.3006	769.58
293.15	0.3482	766.92
293.15	0.3841	765.07
293.15	0.4527	761.67
293.15	0.5004	759.46
293.15	0.5458	757.52
293.15	0.6009	755.29
293.15	0.6459	753.48
293.15	0.7014	751.36
293.15	0.7449	749.75
293.15	0.7986	747.76
293.15	0.8504	745.92
293.15	0.8978	744.27
293.15	0.9091	743.88
293.15	0.9184	743.53
293.15	0.9259	743.26
293.15	0.9379	742.81
293.15	0.9473	742.48
293.15	0.9598	742.06
293.15	0.9706	741.68
293.15	0.9791	741.36
293.15	0.9881	741.04
298.15	0.0100	785.93
298.15	0.0201	785.0
298.15	0.0301	784.01
298.15	0.0402	783.09
298.15	0.0502	782.24
298.15	0.0601	781.36
298.15	0.0696	780.58
298.15	0.0799	779.71
298.15	0.0888	778.95
298.15	0.1008	778.0
298.15	0.1498	774.25
298.15	0.1945	771.13
298.15	0.2600	767.08
298.15	0.3006	764.65
298.15	0.3482	761.97
298.15	0.3841	760.07
298.15	0.4527	756.67
298.15	0.5004	754.42
298.15	0.5458	752.46
298.15	0.6009	750.18
298.15	0.6459	748.37
298.15	0.7014	746.23
298.15	0.7449	744.6
298.15	0.7986	742.58
298.15	0.8504	740.74
298.15	0.8978	739.05
298.15	0.9091	738.66
298.15	0.9184	738.33
298.15	0.9259	738.07
298.15	0.9379	737.6
298.15	0.9473	737.28
298.15	0.9598	736.83
298.15	0.9706	736.46
298.15	0.9791	736.13
298.15	0.9881	735.82
303.15	0.0100	781.19
303.15	0.0201	780.24
303.15	0.0301	779.26
303.15	0.0402	778.32
303.15	0.0502	777.44
303.15	0.0601	776.57
303.15	0.0696	775.75
303.15	0.0799	774.88
303.15	0.0888	774.12
303.15	0.1008	773.16
303.15	0.1498	769.36
303.15	0.1945	766.21
303.15	0.2600	762.1
303.15	0.3006	759.64
303.15	0.3482	756.93
303.15	0.3841	755.01
303.15	0.4527	751.59
303.15	0.5004	749.29
303.15	0.5458	747.32
303.15	0.6009	745.03
303.15	0.6459	743.18
303.15	0.7014	741.01
303.15	0.7449	739.36
303.15	0.7986	737.33
303.15	0.8504	735.47
303.15	0.8978	733.78
303.15	0.9091	733.39
303.15	0.9184	733.04
303.15	0.9259	732.78
303.15	0.9379	732.32
303.15	0.9473	732.0
303.15	0.9598	731.56
303.15	0.9706	731.17
303.15	0.9791	730.85
303.15	0.9881	730.53
308.15	0.0100	776.42
308.15	0.0201	775.46
308.15	0.0301	774.46
308.15	0.0402	773.51
308.15	0.0502	772.61
308.15	0.0601	771.73
308.15	0.0696	770.9
308.15	0.0799	770.02
308.15	0.0888	769.25
308.15	0.1008	768.27
308.15	0.1498	764.43
308.15	0.1945	761.24
308.15	0.2600	757.08
308.15	0.3006	754.59
308.15	0.3482	751.87
308.15	0.3841	749.92
308.15	0.4527	746.45
308.15	0.5004	744.12
308.15	0.5458	742.12
308.15	0.6009	739.81
308.15	0.6459	737.93
308.15	0.7014	735.74
308.15	0.7449	734.07
308.15	0.7986	732.01
308.15	0.8504	730.13
308.15	0.8978	728.43
308.15	0.9091	728.04
308.15	0.9184	727.69
308.15	0.9259	727.43
308.15	0.9379	726.97
308.15	0.9473	726.65
308.15	0.9598	726.21
308.15	0.9706	725.82
308.15	0.9791	725.49
308.15	0.9881	725.18

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0512	782.5
0.0994	779.0
0.1991	771.4
0.3011	765.4
0.4015	760.2
0.4993	755.7
0.6001	751.6
0.7001	747.7
0.8007	744.1
0.8998	740.3
0.9494	738.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0100	790.62
293.15	0.0201	789.69
293.15	0.0301	788.74
293.15	0.0402	787.83
293.15	0.0502	786.96
293.15	0.0601	786.1
293.15	0.0696	785.32
293.15	0.0799	784.47
293.15	0.0888	783.72
293.15	0.1008	782.79
293.15	0.1498	779.11
293.15	0.1945	776.01
293.15	0.2600	771.99
293.15	0.3006	769.58
293.15	0.3482	766.92
293.15	0.3841	765.07
293.15	0.4527	761.67
293.15	0.5004	759.46
293.15	0.5458	757.52
293.15	0.6009	755.29
293.15	0.6459	753.48
293.15	0.7014	751.36
293.15	0.7449	749.75
293.15	0.7986	747.76
293.15	0.8504	745.92
293.15	0.8978	744.27
293.15	0.9091	743.88
293.15	0.9184	743.53
293.15	0.9259	743.26
293.15	0.9379	742.81
293.15	0.9473	742.48
293.15	0.9598	742.06
293.15	0.9706	741.68
293.15	0.9791	741.36
293.15	0.9881	741.04
298.15	0.0100	785.93
298.15	0.0201	785.0
298.15	0.0301	784.01
298.15	0.0402	783.09
298.15	0.0502	782.24
298.15	0.0601	781.36
298.15	0.0696	780.58
298.15	0.0799	779.71
298.15	0.0888	778.95
298.15	0.1008	778.0
298.15	0.1498	774.25
298.15	0.1945	771.13
298.15	0.2600	767.08
298.15	0.3006	764.65
298.15	0.3482	761.97
298.15	0.3841	760.07
298.15	0.4527	756.67
298.15	0.5004	754.42
298.15	0.5458	752.46
298.15	0.6009	750.18
298.15	0.6459	748.37
298.15	0.7014	746.23
298.15	0.7449	744.6
298.15	0.7986	742.58
298.15	0.8504	740.74
298.15	0.8978	739.05
298.15	0.9091	738.66
298.15	0.9184	738.33
298.15	0.9259	738.07
298.15	0.9379	737.6
298.15	0.9473	737.28
298.15	0.9598	736.83
298.15	0.9706	736.46
298.15	0.9791	736.13
298.15	0.9881	735.82
303.15	0.0100	781.19
303.15	0.0201	780.24
303.15	0.0301	779.26
303.15	0.0402	778.32
303.15	0.0502	777.44
303.15	0.0601	776.57
303.15	0.0696	775.75
303.15	0.0799	774.88
303.15	0.0888	774.12
303.15	0.1008	773.16
303.15	0.1498	769.36
303.15	0.1945	766.21
303.15	0.2600	762.1
303.15	0.3006	759.64
303.15	0.3482	756.93
303.15	0.3841	755.01
303.15	0.4527	751.59
303.15	0.5004	749.29
303.15	0.5458	747.32
303.15	0.6009	745.03
303.15	0.6459	743.18
303.15	0.7014	741.01
303.15	0.7449	739.36
303.15	0.7986	737.33
303.15	0.8504	735.47
303.15	0.8978	733.78
303.15	0.9091	733.39
303.15	0.9184	733.04
303.15	0.9259	732.78
303.15	0.9379	732.32
303.15	0.9473	732.0
303.15	0.9598	731.56
303.15	0.9706	731.17
303.15	0.9791	730.85
303.15	0.9881	730.53
308.15	0.0100	776.42
308.15	0.0201	775.46
308.15	0.0301	774.46
308.15	0.0402	773.51
308.15	0.0502	772.61
308.15	0.0601	771.73
308.15	0.0696	770.9
308.15	0.0799	770.02
308.15	0.0888	769.25
308.15	0.1008	768.27
308.15	0.1498	764.43
308.15	0.1945	761.24
308.15	0.2600	757.08
308.15	0.3006	754.59
308.15	0.3482	751.87
308.15	0.3841	749.92
308.15	0.4527	746.45
308.15	0.5004	744.12
308.15	0.5458	742.12
308.15	0.6009	739.81
308.15	0.6459	737.93
308.15	0.7014	735.74
308.15	0.7449	734.07
308.15	0.7986	732.01
308.15	0.8504	730.13
308.15	0.8978	728.43
308.15	0.9091	728.04
308.15	0.9184	727.69
308.15	0.9259	727.43
308.15	0.9379	726.97
308.15	0.9473	726.65
308.15	0.9598	726.21
308.15	0.9706	725.82
308.15	0.9791	725.49
308.15	0.9881	725.18

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0512	782.5
0.0994	779.0
0.1991	771.4
0.3011	765.4
0.4015	760.2
0.4993	755.7
0.6001	751.6
0.7001	747.7
0.8007	744.1
0.8998	740.3
0.9494	738.5

Critical temperature, K [ref]

Mole fraction of Methyl Alcohol (2) - Liquid	Critical temperature, K - Liquid
0.0000	497.00
0.1231	492.00
0.2007	491.00
0.3001	490.40
0.3997	489.20
0.5003	489.80
0.6003	491.90
0.7002	493.60
0.8001	497.70
0.9000	503.50
1.0000	512.30

Critical temperature, K [ref]

Mole fraction of Methyl Alcohol (2) - Liquid	Critical temperature, K - Liquid
0.0000	497.00
0.1231	492.00
0.2007	491.00
0.3001	490.40
0.3997	489.20
0.5003	489.80
0.6003	491.90
0.7002	493.60
0.8001	497.70
0.9000	503.50
1.0000	512.30

Sources

• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K