Mixture of 1-Propanol + Propane, 2-methoxy-2-methyl-

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (2)
4. P_c - Critical pressure, kPa (2)
5. P_vap - Vapor or sublimation pressure, kPa (2)
6. n₀ - Refractive index (Na D-line) (2)
7. ρ_l - Mass density, kg/m3 (4)
8. c_sound,fluid - Speed of Sound, m/s (2)
9. T_boil - Boiling temperature at pressure P, K (2)
10. T_c - Critical temperature, K (2)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas
0.0055	0.0277
0.0174	0.0868
0.0291	0.1472
0.0705	0.3079
0.0940	0.3818
0.1547	0.5318
0.1879	0.5932
0.2180	0.6338
0.2498	0.6850
0.2529	0.6790
0.2823	0.7184
0.3192	0.7524
0.3521	0.7754
0.3867	0.8046
0.4254	0.8194
0.4276	0.8260
0.4868	0.8531
0.5416	0.8646
0.5770	0.8772
0.5919	0.8851
0.6618	0.8977
0.7035	0.9131
0.7413	0.9208
0.7710	0.9297
0.8046	0.9394
0.8403	0.9469
0.8672	0.9550
0.9037	0.9655
0.9399	0.9733
0.9657	0.9811

Mole fraction of Propane, 2-methoxy-2-methyl- (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas
0.0055	0.0277
0.0174	0.0868
0.0291	0.1472
0.0705	0.3079
0.0940	0.3818
0.1547	0.5318
0.1879	0.5932
0.2180	0.6338
0.2498	0.6850
0.2529	0.6790
0.2823	0.7184
0.3192	0.7524
0.3521	0.7754
0.3867	0.8046
0.4254	0.8194
0.4276	0.8260
0.4868	0.8531
0.5416	0.8646
0.5770	0.8772
0.5919	0.8851
0.6618	0.8977
0.7035	0.9131
0.7413	0.9208
0.7710	0.9297
0.8046	0.9394
0.8403	0.9469
0.8672	0.9550
0.9037	0.9655
0.9399	0.9733
0.9657	0.9811

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0126	0.0021
293.15	0.0219	0.0021
293.15	0.0298	0.0020
293.15	0.0403	0.0019
293.15	0.0500	0.0019
293.15	0.0599	0.0018
293.15	0.0699	0.0018
293.15	0.0798	0.0017
293.15	0.0900	0.0017
293.15	0.1003	0.0016
293.15	0.1495	0.0014
293.15	0.1999	0.0012
293.15	0.2500	0.0011
293.15	0.3003	0.0010
293.15	0.3500	0.0009
293.15	0.4015	0.0008
293.15	0.4585	0.0007
293.15	0.5002	0.0007
293.15	0.5505	0.0006
293.15	0.5994	0.0006
293.15	0.6475	0.0005
293.15	0.7026	0.0005
293.15	0.7536	0.0005
293.15	0.8033	0.0004
293.15	0.8471	0.0004
293.15	0.9007	0.0004
293.15	0.9107	0.0004
293.15	0.9185	0.0004
293.15	0.9282	0.0004
293.15	0.9400	0.0004
293.15	0.9493	0.0004
293.15	0.9599	0.0004
293.15	0.9698	0.0003
293.15	0.9796	0.0003
293.15	0.9882	0.0003
298.15	0.0126	0.0019
298.15	0.0219	0.0018
298.15	0.0298	0.0018
298.15	0.0403	0.0017
298.15	0.0500	0.0017
298.15	0.0599	0.0016
298.15	0.0699	0.0016
298.15	0.0798	0.0016
298.15	0.0900	0.0015
298.15	0.1003	0.0015
298.15	0.1495	0.0013
298.15	0.1999	0.0011
298.15	0.2500	0.0010
298.15	0.3003	0.0009
298.15	0.3500	0.0008
298.15	0.4015	0.0007
298.15	0.4585	0.0006
298.15	0.5002	0.0006
298.15	0.5505	0.0006
298.15	0.5994	0.0005
298.15	0.6475	0.0005
298.15	0.7026	0.0004
298.15	0.7536	0.0004
298.15	0.8033	0.0004
298.15	0.8471	0.0004
298.15	0.9007	0.0004
298.15	0.9107	0.0003
298.15	0.9185	0.0004
298.15	0.9282	0.0003
298.15	0.9400	0.0003
298.15	0.9493	0.0003
298.15	0.9599	0.0003
298.15	0.9698	0.0003
298.15	0.9796	0.0003
298.15	0.9882	0.0003
303.15	0.0126	0.0017
303.15	0.0219	0.0016
303.15	0.0298	0.0016
303.15	0.0403	0.0015
303.15	0.0500	0.0015
303.15	0.0599	0.0015
303.15	0.0699	0.0014
303.15	0.0798	0.0014
303.15	0.0900	0.0013
303.15	0.1003	0.0013
303.15	0.1495	0.0012
303.15	0.1999	0.0010
303.15	0.2500	0.0009
303.15	0.3003	0.0008
303.15	0.3500	0.0007
303.15	0.4015	0.0007
303.15	0.4585	0.0006
303.15	0.5002	0.0006
303.15	0.5505	0.0005
303.15	0.5994	0.0005
303.15	0.6475	0.0004
303.15	0.7026	0.0004
303.15	0.7536	0.0004
303.15	0.8033	0.0004
303.15	0.8471	0.0004
303.15	0.9007	0.0003
303.15	0.9107	0.0003
303.15	0.9185	0.0003
303.15	0.9282	0.0003
303.15	0.9400	0.0003
303.15	0.9493	0.0003
303.15	0.9599	0.0003
303.15	0.9698	0.0003
303.15	0.9796	0.0003
303.15	0.9882	0.0003
308.15	0.0126	0.0015
308.15	0.0219	0.0015
308.15	0.0298	0.0014
308.15	0.0403	0.0014
308.15	0.0500	0.0013
308.15	0.0599	0.0013
308.15	0.0699	0.0013
308.15	0.0798	0.0013
308.15	0.0900	0.0012
308.15	0.1003	0.0012
308.15	0.1495	0.0010
308.15	0.1999	0.0009
308.15	0.2500	0.0008
308.15	0.3003	0.0007
308.15	0.3500	0.0007
308.15	0.4015	0.0006
308.15	0.4585	0.0005
308.15	0.5002	0.0005
308.15	0.5505	0.0005
308.15	0.5994	0.0004
308.15	0.6475	0.0004
308.15	0.7026	0.0004
308.15	0.7536	0.0004
308.15	0.8033	0.0003
308.15	0.8471	0.0003
308.15	0.9007	0.0003
308.15	0.9107	0.0003
308.15	0.9185	0.0003
308.15	0.9282	0.0003
308.15	0.9400	0.0003
308.15	0.9493	0.0003
308.15	0.9599	0.0003
308.15	0.9698	0.0003
308.15	0.9796	0.0003
308.15	0.9882	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0126	0.0021
293.15	0.0219	0.0021
293.15	0.0298	0.0020
293.15	0.0403	0.0019
293.15	0.0500	0.0019
293.15	0.0599	0.0018
293.15	0.0699	0.0018
293.15	0.0798	0.0017
293.15	0.0900	0.0017
293.15	0.1003	0.0016
293.15	0.1495	0.0014
293.15	0.1999	0.0012
293.15	0.2500	0.0011
293.15	0.3003	0.0010
293.15	0.3500	0.0009
293.15	0.4015	0.0008
293.15	0.4585	0.0007
293.15	0.5002	0.0007
293.15	0.5505	0.0006
293.15	0.5994	0.0006
293.15	0.6475	0.0005
293.15	0.7026	0.0005
293.15	0.7536	0.0005
293.15	0.8033	0.0004
293.15	0.8471	0.0004
293.15	0.9007	0.0004
293.15	0.9107	0.0004
293.15	0.9185	0.0004
293.15	0.9282	0.0004
293.15	0.9400	0.0004
293.15	0.9493	0.0004
293.15	0.9599	0.0004
293.15	0.9698	0.0003
293.15	0.9796	0.0003
293.15	0.9882	0.0003
298.15	0.0126	0.0019
298.15	0.0219	0.0018
298.15	0.0298	0.0018
298.15	0.0403	0.0017
298.15	0.0500	0.0017
298.15	0.0599	0.0016
298.15	0.0699	0.0016
298.15	0.0798	0.0016
298.15	0.0900	0.0015
298.15	0.1003	0.0015
298.15	0.1495	0.0013
298.15	0.1999	0.0011
298.15	0.2500	0.0010
298.15	0.3003	0.0009
298.15	0.3500	0.0008
298.15	0.4015	0.0007
298.15	0.4585	0.0006
298.15	0.5002	0.0006
298.15	0.5505	0.0006
298.15	0.5994	0.0005
298.15	0.6475	0.0005
298.15	0.7026	0.0004
298.15	0.7536	0.0004
298.15	0.8033	0.0004
298.15	0.8471	0.0004
298.15	0.9007	0.0004
298.15	0.9107	0.0003
298.15	0.9185	0.0004
298.15	0.9282	0.0003
298.15	0.9400	0.0003
298.15	0.9493	0.0003
298.15	0.9599	0.0003
298.15	0.9698	0.0003
298.15	0.9796	0.0003
298.15	0.9882	0.0003
303.15	0.0126	0.0017
303.15	0.0219	0.0016
303.15	0.0298	0.0016
303.15	0.0403	0.0015
303.15	0.0500	0.0015
303.15	0.0599	0.0015
303.15	0.0699	0.0014
303.15	0.0798	0.0014
303.15	0.0900	0.0013
303.15	0.1003	0.0013
303.15	0.1495	0.0012
303.15	0.1999	0.0010
303.15	0.2500	0.0009
303.15	0.3003	0.0008
303.15	0.3500	0.0007
303.15	0.4015	0.0007
303.15	0.4585	0.0006
303.15	0.5002	0.0006
303.15	0.5505	0.0005
303.15	0.5994	0.0005
303.15	0.6475	0.0004
303.15	0.7026	0.0004
303.15	0.7536	0.0004
303.15	0.8033	0.0004
303.15	0.8471	0.0004
303.15	0.9007	0.0003
303.15	0.9107	0.0003
303.15	0.9185	0.0003
303.15	0.9282	0.0003
303.15	0.9400	0.0003
303.15	0.9493	0.0003
303.15	0.9599	0.0003
303.15	0.9698	0.0003
303.15	0.9796	0.0003
303.15	0.9882	0.0003
308.15	0.0126	0.0015
308.15	0.0219	0.0015
308.15	0.0298	0.0014
308.15	0.0403	0.0014
308.15	0.0500	0.0013
308.15	0.0599	0.0013
308.15	0.0699	0.0013
308.15	0.0798	0.0013
308.15	0.0900	0.0012
308.15	0.1003	0.0012
308.15	0.1495	0.0010
308.15	0.1999	0.0009
308.15	0.2500	0.0008
308.15	0.3003	0.0007
308.15	0.3500	0.0007
308.15	0.4015	0.0006
308.15	0.4585	0.0005
308.15	0.5002	0.0005
308.15	0.5505	0.0005
308.15	0.5994	0.0004
308.15	0.6475	0.0004
308.15	0.7026	0.0004
308.15	0.7536	0.0004
308.15	0.8033	0.0003
308.15	0.8471	0.0003
308.15	0.9007	0.0003
308.15	0.9107	0.0003
308.15	0.9185	0.0003
308.15	0.9282	0.0003
308.15	0.9400	0.0003
308.15	0.9493	0.0003
308.15	0.9599	0.0003
308.15	0.9698	0.0003
308.15	0.9796	0.0003
308.15	0.9882	0.0003

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

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	0.0000
0.0491	0.0621
0.0997	0.1312
0.1503	0.2011
0.1976	0.2644
0.2472	0.3268
0.2965	0.3829
0.3477	0.4373
0.4008	0.4858
0.4468	0.5197
0.4982	0.5481
0.5486	0.5678
0.5974	0.5759
0.6485	0.5706
0.6977	0.5564
0.7491	0.5255
0.7985	0.4750
0.8494	0.4031
0.8986	0.3082
0.9498	0.1729
1.0000	0.0000

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

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	0.0000
0.0491	0.0621
0.0997	0.1312
0.1503	0.2011
0.1976	0.2644
0.2472	0.3268
0.2965	0.3829
0.3477	0.4373
0.4008	0.4858
0.4468	0.5197
0.4982	0.5481
0.5486	0.5678
0.5974	0.5759
0.6485	0.5706
0.6977	0.5564
0.7491	0.5255
0.7985	0.4750
0.8494	0.4031
0.8986	0.3082
0.9498	0.1729
1.0000	0.0000

Critical pressure, kPa [ref]

Mole fraction of 1-Propanol (1) - Liquid	Critical pressure, kPa - Liquid
0.0000	3448.00
0.1003	3577.00
0.2011	3731.00
0.2999	3880.00
0.3975	4045.00
0.5001	4205.00
0.6007	4390.00
0.7019	4596.00
0.7988	4776.00
0.9000	5002.00
1.0000	5169.00

Critical pressure, kPa [ref]

Mole fraction of 1-Propanol (1) - Liquid	Critical pressure, kPa - Liquid
0.0000	3448.00
0.1003	3577.00
0.2011	3731.00
0.2999	3880.00
0.3975	4045.00
0.5001	4205.00
0.6007	4390.00
0.7019	4596.00
0.7988	4776.00
0.9000	5002.00
1.0000	5169.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	7.00
0.0123	8.34
0.0303	10.22
0.0549	12.72
0.1015	17.18
0.1278	19.56
0.1519	21.60
0.1945	24.94
0.2549	29.17
0.2998	31.98
0.3066	32.36
0.3480	34.70
0.3978	37.18
0.3979	37.24
0.4470	39.49
0.4495	39.65
0.4989	41.72
0.4992	41.77
0.5486	43.71
0.5496	43.77
0.5974	45.55
0.5978	45.58
0.6490	47.39
0.6922	48.89
0.6977	49.09
0.7500	50.86
0.7985	52.49
0.8476	54.19
0.8730	55.07
0.8957	55.90
0.9477	57.85
0.9770	59.01
0.9849	59.29
1.0000	59.92

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	7.00
0.0123	8.34
0.0303	10.22
0.0549	12.72
0.1015	17.18
0.1278	19.56
0.1519	21.60
0.1945	24.94
0.2549	29.17
0.2998	31.98
0.3066	32.36
0.3480	34.70
0.3978	37.18
0.3979	37.24
0.4470	39.49
0.4495	39.65
0.4989	41.72
0.4992	41.77
0.5486	43.71
0.5496	43.77
0.5974	45.55
0.5978	45.58
0.6490	47.39
0.6922	48.89
0.6977	49.09
0.7500	50.86
0.7985	52.49
0.8476	54.19
0.8730	55.07
0.8957	55.90
0.9477	57.85
0.9770	59.01
0.9849	59.29
1.0000	59.92

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3831
0.0584	1.3823
0.0942	1.3819
0.1293	1.3815
0.1923	1.3806
0.2104	1.3802
0.2769	1.3793
0.3348	1.3784
0.3760	1.3774
0.4154	1.3769
0.4663	1.376
0.4881	1.3756
0.5644	1.3742
0.5901	1.3738
0.6768	1.3724
0.7881	1.3703
0.8496	1.3692
0.8918	1.3684
0.9035	1.3681
0.9746	1.3667
1.0000	1.3663

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3831
0.0584	1.3823
0.0942	1.3819
0.1293	1.3815
0.1923	1.3806
0.2104	1.3802
0.2769	1.3793
0.3348	1.3784
0.3760	1.3774
0.4154	1.3769
0.4663	1.376
0.4881	1.3756
0.5644	1.3742
0.5901	1.3738
0.6768	1.3724
0.7881	1.3703
0.8496	1.3692
0.8918	1.3684
0.9035	1.3681
0.9746	1.3667
1.0000	1.3663

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0126	802.92
293.15	0.0219	802.2
293.15	0.0298	801.64
293.15	0.0403	800.81
293.15	0.0500	800.12
293.15	0.0599	799.4
293.15	0.0699	798.72
293.15	0.0798	798.25
293.15	0.0900	797.26
293.15	0.1003	796.41
293.15	0.1495	793.03
293.15	0.1999	789.56
293.15	0.2500	786.15
293.15	0.3003	782.74
293.15	0.3500	779.47
293.15	0.4015	776.15
293.15	0.4585	772.51
293.15	0.5002	769.91
293.15	0.5505	766.88
293.15	0.5994	763.94
293.15	0.6475	761.06
293.15	0.7026	757.85
293.15	0.7536	754.92
293.15	0.8033	752.01
293.15	0.8471	749.51
293.15	0.9007	746.4
293.15	0.9107	745.77
293.15	0.9185	745.32
293.15	0.9282	744.76
293.15	0.9400	744.07
293.15	0.9493	743.55
293.15	0.9599	742.94
293.15	0.9698	742.37
293.15	0.9796	741.82
293.15	0.9882	741.32
298.15	0.0126	798.92
298.15	0.0219	798.21
298.15	0.0298	797.61
298.15	0.0403	796.7
298.15	0.0500	796.03
298.15	0.0599	795.34
298.15	0.0699	794.62
298.15	0.0798	794.12
298.15	0.0900	793.05
298.15	0.1003	792.28
298.15	0.1495	788.85
298.15	0.1999	785.28
298.15	0.2500	781.8
298.15	0.3003	778.33
298.15	0.3500	774.99
298.15	0.4015	771.6
298.15	0.4585	767.88
298.15	0.5002	765.22
298.15	0.5505	762.1
298.15	0.5994	759.14
298.15	0.6475	756.21
298.15	0.7026	752.93
298.15	0.7536	749.92
298.15	0.8033	747.01
298.15	0.8471	744.41
298.15	0.9007	741.27
298.15	0.9107	740.64
298.15	0.9185	740.18
298.15	0.9282	739.61
298.15	0.9400	738.91
298.15	0.9493	738.35
298.15	0.9599	737.74
298.15	0.9698	737.19
298.15	0.9796	736.64
298.15	0.9882	736.14
303.15	0.0126	794.86
303.15	0.0219	794.13
303.15	0.0298	793.53
303.15	0.0403	792.61
303.15	0.0500	791.93
303.15	0.0599	791.21
303.15	0.0699	790.47
303.15	0.0798	789.92
303.15	0.0900	788.85
303.15	0.1003	788.08
303.15	0.1495	784.61
303.15	0.1999	780.94
303.15	0.2500	777.38
303.15	0.3003	773.84
303.15	0.3500	770.45
303.15	0.4015	766.99
303.15	0.4585	763.21
303.15	0.5002	760.49
303.15	0.5505	757.3
303.15	0.5994	754.28
303.15	0.6475	751.27
303.15	0.7026	747.92
303.15	0.7536	744.86
303.15	0.8033	741.89
303.15	0.8471	739.24
303.15	0.9007	736.06
303.15	0.9107	735.41
303.15	0.9185	734.94
303.15	0.9282	734.37
303.15	0.9400	733.65
303.15	0.9493	733.09
303.15	0.9599	732.47
303.15	0.9698	731.91
303.15	0.9796	731.35
303.15	0.9882	730.84
308.15	0.0126	790.76
308.15	0.0219	790.02
308.15	0.0298	789.4
308.15	0.0403	788.45
308.15	0.0500	787.77
308.15	0.0599	787.04
308.15	0.0699	786.28
308.15	0.0798	785.72
308.15	0.0900	784.63
308.15	0.1003	783.85
308.15	0.1495	780.3
308.15	0.1999	776.55
308.15	0.2500	772.92
308.15	0.3003	769.32
308.15	0.3500	765.85
308.15	0.4015	762.32
308.15	0.4585	758.45
308.15	0.5002	755.68
308.15	0.5505	752.42
308.15	0.5994	749.34
308.15	0.6475	746.28
308.15	0.7026	742.86
308.15	0.7536	739.74
308.15	0.8033	736.72
308.15	0.8471	734.04
308.15	0.9007	730.79
308.15	0.9107	730.13
308.15	0.9185	729.65
308.15	0.9282	729.07
308.15	0.9400	728.34
308.15	0.9493	727.78
308.15	0.9599	727.15
308.15	0.9698	726.58
308.15	0.9796	726.01
308.15	0.9882	725.49

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	799.64
0.0584	795.35
0.0942	792.82
0.1293	790.29
0.1923	786.06
0.2104	784.45
0.2769	779.97
0.3348	776.07
0.3760	773.56
0.4154	770.88
0.4663	767.49
0.4881	766.16
0.5644	761.34
0.5901	759.75
0.6768	754.54
0.7881	747.98
0.8496	744.33
0.8918	741.7
0.9035	741.17
0.9746	737.03
1.0000	735.56

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0126	802.92
293.15	0.0219	802.2
293.15	0.0298	801.64
293.15	0.0403	800.81
293.15	0.0500	800.12
293.15	0.0599	799.4
293.15	0.0699	798.72
293.15	0.0798	798.25
293.15	0.0900	797.26
293.15	0.1003	796.41
293.15	0.1495	793.03
293.15	0.1999	789.56
293.15	0.2500	786.15
293.15	0.3003	782.74
293.15	0.3500	779.47
293.15	0.4015	776.15
293.15	0.4585	772.51
293.15	0.5002	769.91
293.15	0.5505	766.88
293.15	0.5994	763.94
293.15	0.6475	761.06
293.15	0.7026	757.85
293.15	0.7536	754.92
293.15	0.8033	752.01
293.15	0.8471	749.51
293.15	0.9007	746.4
293.15	0.9107	745.77
293.15	0.9185	745.32
293.15	0.9282	744.76
293.15	0.9400	744.07
293.15	0.9493	743.55
293.15	0.9599	742.94
293.15	0.9698	742.37
293.15	0.9796	741.82
293.15	0.9882	741.32
298.15	0.0126	798.92
298.15	0.0219	798.21
298.15	0.0298	797.61
298.15	0.0403	796.7
298.15	0.0500	796.03
298.15	0.0599	795.34
298.15	0.0699	794.62
298.15	0.0798	794.12
298.15	0.0900	793.05
298.15	0.1003	792.28
298.15	0.1495	788.85
298.15	0.1999	785.28
298.15	0.2500	781.8
298.15	0.3003	778.33
298.15	0.3500	774.99
298.15	0.4015	771.6
298.15	0.4585	767.88
298.15	0.5002	765.22
298.15	0.5505	762.1
298.15	0.5994	759.14
298.15	0.6475	756.21
298.15	0.7026	752.93
298.15	0.7536	749.92
298.15	0.8033	747.01
298.15	0.8471	744.41
298.15	0.9007	741.27
298.15	0.9107	740.64
298.15	0.9185	740.18
298.15	0.9282	739.61
298.15	0.9400	738.91
298.15	0.9493	738.35
298.15	0.9599	737.74
298.15	0.9698	737.19
298.15	0.9796	736.64
298.15	0.9882	736.14
303.15	0.0126	794.86
303.15	0.0219	794.13
303.15	0.0298	793.53
303.15	0.0403	792.61
303.15	0.0500	791.93
303.15	0.0599	791.21
303.15	0.0699	790.47
303.15	0.0798	789.92
303.15	0.0900	788.85
303.15	0.1003	788.08
303.15	0.1495	784.61
303.15	0.1999	780.94
303.15	0.2500	777.38
303.15	0.3003	773.84
303.15	0.3500	770.45
303.15	0.4015	766.99
303.15	0.4585	763.21
303.15	0.5002	760.49
303.15	0.5505	757.3
303.15	0.5994	754.28
303.15	0.6475	751.27
303.15	0.7026	747.92
303.15	0.7536	744.86
303.15	0.8033	741.89
303.15	0.8471	739.24
303.15	0.9007	736.06
303.15	0.9107	735.41
303.15	0.9185	734.94
303.15	0.9282	734.37
303.15	0.9400	733.65
303.15	0.9493	733.09
303.15	0.9599	732.47
303.15	0.9698	731.91
303.15	0.9796	731.35
303.15	0.9882	730.84
308.15	0.0126	790.76
308.15	0.0219	790.02
308.15	0.0298	789.4
308.15	0.0403	788.45
308.15	0.0500	787.77
308.15	0.0599	787.04
308.15	0.0699	786.28
308.15	0.0798	785.72
308.15	0.0900	784.63
308.15	0.1003	783.85
308.15	0.1495	780.3
308.15	0.1999	776.55
308.15	0.2500	772.92
308.15	0.3003	769.32
308.15	0.3500	765.85
308.15	0.4015	762.32
308.15	0.4585	758.45
308.15	0.5002	755.68
308.15	0.5505	752.42
308.15	0.5994	749.34
308.15	0.6475	746.28
308.15	0.7026	742.86
308.15	0.7536	739.74
308.15	0.8033	736.72
308.15	0.8471	734.04
308.15	0.9007	730.79
308.15	0.9107	730.13
308.15	0.9185	729.65
308.15	0.9282	729.07
308.15	0.9400	728.34
308.15	0.9493	727.78
308.15	0.9599	727.15
308.15	0.9698	726.58
308.15	0.9796	726.01
308.15	0.9882	725.49

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	799.64
0.0584	795.35
0.0942	792.82
0.1293	790.29
0.1923	786.06
0.2104	784.45
0.2769	779.97
0.3348	776.07
0.3760	773.56
0.4154	770.88
0.4663	767.49
0.4881	766.16
0.5644	761.34
0.5901	759.75
0.6768	754.54
0.7881	747.98
0.8496	744.33
0.8918	741.7
0.9035	741.17
0.9746	737.03
1.0000	735.56

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1207.0
0.0584	1196.0
0.0942	1190.0
0.1293	1184.0
0.1923	1173.0
0.2104	1168.0
0.2769	1156.0
0.3348	1146.0
0.3760	1139.0
0.4154	1132.0
0.4663	1123.0
0.4881	1119.0
0.5644	1107.0
0.5901	1102.0
0.6768	1089.0
0.7881	1072.0
0.8496	1062.0
0.8918	1056.0
0.9035	1054.0
0.9746	1042.0
1.0000	1037.0

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1207.0
0.0584	1196.0
0.0942	1190.0
0.1293	1184.0
0.1923	1173.0
0.2104	1168.0
0.2769	1156.0
0.3348	1146.0
0.3760	1139.0
0.4154	1132.0
0.4663	1123.0
0.4881	1119.0
0.5644	1107.0
0.5901	1102.0
0.6768	1089.0
0.7881	1072.0
0.8496	1062.0
0.8918	1056.0
0.9035	1054.0
0.9746	1042.0
1.0000	1037.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0055	369.54
0.0174	368.12
0.0291	366.67
0.0705	362.26
0.0940	359.74
0.1547	354.78
0.1879	352.31
0.2180	350.49
0.2498	348.77
0.2529	348.26
0.2823	346.93
0.3192	345.14
0.3521	343.81
0.3867	342.19
0.4254	340.94
0.4276	340.18
0.4868	338.76
0.5416	337.55
0.5770	336.56
0.5919	335.99
0.6618	334.67
0.7035	333.75
0.7413	333.05
0.7710	332.34
0.8046	331.67
0.8403	331.00
0.8672	330.46
0.9037	329.81
0.9399	329.13
0.9657	328.68

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0055	369.54
0.0174	368.12
0.0291	366.67
0.0705	362.26
0.0940	359.74
0.1547	354.78
0.1879	352.31
0.2180	350.49
0.2498	348.77
0.2529	348.26
0.2823	346.93
0.3192	345.14
0.3521	343.81
0.3867	342.19
0.4254	340.94
0.4276	340.18
0.4868	338.76
0.5416	337.55
0.5770	336.56
0.5919	335.99
0.6618	334.67
0.7035	333.75
0.7413	333.05
0.7710	332.34
0.8046	331.67
0.8403	331.00
0.8672	330.46
0.9037	329.81
0.9399	329.13
0.9657	328.68

Critical temperature, K [ref]

Mole fraction of 1-Propanol (1) - Liquid	Critical temperature, K - Liquid
0.0000	497.00
0.1003	498.20
0.2011	501.20
0.2999	503.80
0.3975	507.30
0.5001	510.70
0.6007	515.10
0.7019	520.50
0.7988	524.10
0.9000	531.30
1.0000	536.80

Critical temperature, K [ref]

Mole fraction of 1-Propanol (1) - Liquid	Critical temperature, K - Liquid
0.0000	497.00
0.1003	498.20
0.2011	501.20
0.2999	503.80
0.3975	507.30
0.5001	510.70
0.6007	515.10
0.7019	520.50
0.7988	524.10
0.9000	531.30
1.0000	536.80

Sources

• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• 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
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing 1,1-Dimethylethyl Methyl Ether, 1-Propanol, and Hexane at T ) 313.15 K
• Isobaric Vapor-Liquid Equilibria at 101.32 kPa and Densities, Speeds of Sound, and Refractive Indices at 298.15 K for MTBE or DIPE or TAME + 1-Propanol Binary Systems