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

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid
317.20	1.10	0.0000
317.20	18.70	0.1520
317.20	26.90	0.2420
317.20	34.60	0.3430
317.20	43.00	0.4750
317.20	49.40	0.5960
317.20	55.20	0.7170
317.20	60.30	0.8380
317.20	64.10	0.8990
317.20	67.10	0.9600
317.20	68.90	1.0000
327.20	2.10	0.0000
327.20	14.10	0.0710
327.20	17.20	0.0910
327.20	25.30	0.1410
327.20	33.50	0.2120
327.20	41.50	0.2730
327.20	52.60	0.3940
327.20	60.90	0.4950
327.20	68.80	0.5960
327.20	77.30	0.7070
327.20	84.00	0.8080
327.20	88.50	0.8790
327.20	94.10	0.9600
327.20	97.10	1.0000

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas
317.20	1.10	0.0000
317.20	18.70	0.9370
317.20	26.90	0.9600
317.20	34.60	0.9720
317.20	43.00	0.9810
317.20	49.40	0.9860
317.20	55.20	0.9900
317.20	60.30	0.9940
317.20	64.10	0.9960
317.20	67.10	0.9980
317.20	68.90	1.0000
327.20	2.10	0.0000
327.20	14.10	0.8330
327.20	17.20	0.8660
327.20	25.30	0.9100
327.20	33.50	0.9390
327.20	41.50	0.9520
327.20	52.60	0.9680
327.20	60.90	0.9750
327.20	68.80	0.9810
327.20	77.30	0.9860
327.20	84.00	0.9900
327.20	88.50	0.9930
327.20	94.10	0.9980
327.20	97.10	1.0000

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid
317.20	1.10	0.0000
317.20	18.70	0.1520
317.20	26.90	0.2420
317.20	34.60	0.3430
317.20	43.00	0.4750
317.20	49.40	0.5960
317.20	55.20	0.7170
317.20	60.30	0.8380
317.20	64.10	0.8990
317.20	67.10	0.9600
317.20	68.90	1.0000
327.20	2.10	0.0000
327.20	14.10	0.0710
327.20	17.20	0.0910
327.20	25.30	0.1410
327.20	33.50	0.2120
327.20	41.50	0.2730
327.20	52.60	0.3940
327.20	60.90	0.4950
327.20	68.80	0.5960
327.20	77.30	0.7070
327.20	84.00	0.8080
327.20	88.50	0.8790
327.20	94.10	0.9600
327.20	97.10	1.0000

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas
317.20	1.10	0.0000
317.20	18.70	0.9370
317.20	26.90	0.9600
317.20	34.60	0.9720
317.20	43.00	0.9810
317.20	49.40	0.9860
317.20	55.20	0.9900
317.20	60.30	0.9940
317.20	64.10	0.9960
317.20	67.10	0.9980
317.20	68.90	1.0000
327.20	2.10	0.0000
327.20	14.10	0.8330
327.20	17.20	0.8660
327.20	25.30	0.9100
327.20	33.50	0.9390
327.20	41.50	0.9520
327.20	52.60	0.9680
327.20	60.90	0.9750
327.20	68.80	0.9810
327.20	77.30	0.9860
327.20	84.00	0.9900
327.20	88.50	0.9930
327.20	94.10	0.9980
327.20	97.10	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0105	0.0039
293.15	0.0197	0.0038
293.15	0.0321	0.0036
293.15	0.0401	0.0035
293.15	0.0506	0.0034
293.15	0.0595	0.0033
293.15	0.0699	0.0032
293.15	0.0811	0.0031
293.15	0.0901	0.0030
293.15	0.1042	0.0028
293.15	0.1506	0.0024
293.15	0.2078	0.0021
293.15	0.2520	0.0018
293.15	0.3010	0.0016
293.15	0.3492	0.0014
293.15	0.3996	0.0012
293.15	0.4577	0.0010
293.15	0.4985	0.0009
293.15	0.5512	0.0008
293.15	0.5999	0.0008
293.15	0.6506	0.0007
293.15	0.6986	0.0006
293.15	0.7451	0.0006
293.15	0.7976	0.0005
293.15	0.8534	0.0004
293.15	0.8980	0.0004
293.15	0.9098	0.0004
293.15	0.9195	0.0004
293.15	0.9289	0.0004
293.15	0.9419	0.0004
293.15	0.9495	0.0004
293.15	0.9594	0.0004
293.15	0.9688	0.0004
293.15	0.9792	0.0004
293.15	0.9902	0.0004
298.15	0.0105	0.0034
298.15	0.0197	0.0033
298.15	0.0321	0.0031
298.15	0.0401	0.0031
298.15	0.0506	0.0030
298.15	0.0595	0.0029
298.15	0.0699	0.0028
298.15	0.0811	0.0027
298.15	0.0901	0.0026
298.15	0.1042	0.0025
298.15	0.1506	0.0022
298.15	0.2078	0.0018
298.15	0.2520	0.0016
298.15	0.3010	0.0014
298.15	0.3492	0.0013
298.15	0.3996	0.0011
298.15	0.4577	0.0010
298.15	0.4985	0.0009
298.15	0.5512	0.0008
298.15	0.5999	0.0007
298.15	0.6506	0.0006
298.15	0.6986	0.0006
298.15	0.7451	0.0005
298.15	0.7976	0.0005
298.15	0.8534	0.0004
298.15	0.8980	0.0004
298.15	0.9098	0.0004
298.15	0.9195	0.0004
298.15	0.9289	0.0004
298.15	0.9419	0.0004
298.15	0.9495	0.0004
298.15	0.9594	0.0003
298.15	0.9688	0.0003
298.15	0.9792	0.0003
298.15	0.9902	0.0003
303.15	0.0105	0.0029
303.15	0.0197	0.0029
303.15	0.0321	0.0027
303.15	0.0401	0.0027
303.15	0.0506	0.0026
303.15	0.0595	0.0025
303.15	0.0699	0.0024
303.15	0.0811	0.0024
303.15	0.0901	0.0023
303.15	0.1042	0.0022
303.15	0.1506	0.0019
303.15	0.2078	0.0016
303.15	0.2520	0.0015
303.15	0.3010	0.0013
303.15	0.3492	0.0011
303.15	0.3996	0.0010
303.15	0.4577	0.0009
303.15	0.4985	0.0008
303.15	0.5512	0.0007
303.15	0.5999	0.0006
303.15	0.6506	0.0006
303.15	0.6986	0.0005
303.15	0.7451	0.0005
303.15	0.7976	0.0004
303.15	0.8534	0.0004
303.15	0.8980	0.0004
303.15	0.9098	0.0004
303.15	0.9195	0.0003
303.15	0.9289	0.0003
303.15	0.9419	0.0003
303.15	0.9495	0.0003
303.15	0.9594	0.0003
303.15	0.9688	0.0003
303.15	0.9792	0.0003
303.15	0.9902	0.0003
308.15	0.0105	0.0026
308.15	0.0197	0.0025
308.15	0.0321	0.0024
308.15	0.0401	0.0023
308.15	0.0506	0.0023
308.15	0.0595	0.0022
308.15	0.0699	0.0021
308.15	0.0811	0.0021
308.15	0.0901	0.0020
308.15	0.1042	0.0019
308.15	0.1506	0.0017
308.15	0.2078	0.0015
308.15	0.2520	0.0013
308.15	0.3010	0.0012
308.15	0.3492	0.0010
308.15	0.3996	0.0009
308.15	0.4577	0.0008
308.15	0.4985	0.0007
308.15	0.5512	0.0007
308.15	0.5999	0.0006
308.15	0.6506	0.0005
308.15	0.6986	0.0005
308.15	0.7451	0.0004
308.15	0.7976	0.0004
308.15	0.8534	0.0004
308.15	0.8980	0.0003
308.15	0.9098	0.0003
308.15	0.9195	0.0003
308.15	0.9289	0.0003
308.15	0.9419	0.0003
308.15	0.9495	0.0003
308.15	0.9594	0.0003
308.15	0.9688	0.0003
308.15	0.9792	0.0003
308.15	0.9902	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- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0105	0.0039
293.15	0.0197	0.0038
293.15	0.0321	0.0036
293.15	0.0401	0.0035
293.15	0.0506	0.0034
293.15	0.0595	0.0033
293.15	0.0699	0.0032
293.15	0.0811	0.0031
293.15	0.0901	0.0030
293.15	0.1042	0.0028
293.15	0.1506	0.0024
293.15	0.2078	0.0021
293.15	0.2520	0.0018
293.15	0.3010	0.0016
293.15	0.3492	0.0014
293.15	0.3996	0.0012
293.15	0.4577	0.0010
293.15	0.4985	0.0009
293.15	0.5512	0.0008
293.15	0.5999	0.0008
293.15	0.6506	0.0007
293.15	0.6986	0.0006
293.15	0.7451	0.0006
293.15	0.7976	0.0005
293.15	0.8534	0.0004
293.15	0.8980	0.0004
293.15	0.9098	0.0004
293.15	0.9195	0.0004
293.15	0.9289	0.0004
293.15	0.9419	0.0004
293.15	0.9495	0.0004
293.15	0.9594	0.0004
293.15	0.9688	0.0004
293.15	0.9792	0.0004
293.15	0.9902	0.0004
298.15	0.0105	0.0034
298.15	0.0197	0.0033
298.15	0.0321	0.0031
298.15	0.0401	0.0031
298.15	0.0506	0.0030
298.15	0.0595	0.0029
298.15	0.0699	0.0028
298.15	0.0811	0.0027
298.15	0.0901	0.0026
298.15	0.1042	0.0025
298.15	0.1506	0.0022
298.15	0.2078	0.0018
298.15	0.2520	0.0016
298.15	0.3010	0.0014
298.15	0.3492	0.0013
298.15	0.3996	0.0011
298.15	0.4577	0.0010
298.15	0.4985	0.0009
298.15	0.5512	0.0008
298.15	0.5999	0.0007
298.15	0.6506	0.0006
298.15	0.6986	0.0006
298.15	0.7451	0.0005
298.15	0.7976	0.0005
298.15	0.8534	0.0004
298.15	0.8980	0.0004
298.15	0.9098	0.0004
298.15	0.9195	0.0004
298.15	0.9289	0.0004
298.15	0.9419	0.0004
298.15	0.9495	0.0004
298.15	0.9594	0.0003
298.15	0.9688	0.0003
298.15	0.9792	0.0003
298.15	0.9902	0.0003
303.15	0.0105	0.0029
303.15	0.0197	0.0029
303.15	0.0321	0.0027
303.15	0.0401	0.0027
303.15	0.0506	0.0026
303.15	0.0595	0.0025
303.15	0.0699	0.0024
303.15	0.0811	0.0024
303.15	0.0901	0.0023
303.15	0.1042	0.0022
303.15	0.1506	0.0019
303.15	0.2078	0.0016
303.15	0.2520	0.0015
303.15	0.3010	0.0013
303.15	0.3492	0.0011
303.15	0.3996	0.0010
303.15	0.4577	0.0009
303.15	0.4985	0.0008
303.15	0.5512	0.0007
303.15	0.5999	0.0006
303.15	0.6506	0.0006
303.15	0.6986	0.0005
303.15	0.7451	0.0005
303.15	0.7976	0.0004
303.15	0.8534	0.0004
303.15	0.8980	0.0004
303.15	0.9098	0.0004
303.15	0.9195	0.0003
303.15	0.9289	0.0003
303.15	0.9419	0.0003
303.15	0.9495	0.0003
303.15	0.9594	0.0003
303.15	0.9688	0.0003
303.15	0.9792	0.0003
303.15	0.9902	0.0003
308.15	0.0105	0.0026
308.15	0.0197	0.0025
308.15	0.0321	0.0024
308.15	0.0401	0.0023
308.15	0.0506	0.0023
308.15	0.0595	0.0022
308.15	0.0699	0.0021
308.15	0.0811	0.0021
308.15	0.0901	0.0020
308.15	0.1042	0.0019
308.15	0.1506	0.0017
308.15	0.2078	0.0015
308.15	0.2520	0.0013
308.15	0.3010	0.0012
308.15	0.3492	0.0010
308.15	0.3996	0.0009
308.15	0.4577	0.0008
308.15	0.4985	0.0007
308.15	0.5512	0.0007
308.15	0.5999	0.0006
308.15	0.6506	0.0005
308.15	0.6986	0.0005
308.15	0.7451	0.0004
308.15	0.7976	0.0004
308.15	0.8534	0.0004
308.15	0.8980	0.0003
308.15	0.9098	0.0003
308.15	0.9195	0.0003
308.15	0.9289	0.0003
308.15	0.9419	0.0003
308.15	0.9495	0.0003
308.15	0.9594	0.0003
308.15	0.9688	0.0003
308.15	0.9792	0.0003
308.15	0.9902	0.0003

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	0.0105	813.89
293.15	0.0197	813.34
293.15	0.0321	812.56
293.15	0.0401	812.06
293.15	0.0506	811.39
293.15	0.0595	810.83
293.15	0.0699	810.18
293.15	0.0811	809.49
293.15	0.0901	808.93
293.15	0.1042	808.03
293.15	0.1506	805.02
293.15	0.2078	801.27
293.15	0.2520	798.32
293.15	0.3010	795.01
293.15	0.3492	791.65
293.15	0.3996	788.14
293.15	0.4577	784.0
293.15	0.4985	781.06
293.15	0.5512	777.21
293.15	0.5999	773.61
293.15	0.6506	769.72
293.15	0.6986	766.04
293.15	0.7451	762.49
293.15	0.7976	758.12
293.15	0.8534	753.55
293.15	0.8980	749.74
293.15	0.9098	748.75
293.15	0.9195	747.92
293.15	0.9289	747.1
293.15	0.9419	745.96
293.15	0.9495	745.29
293.15	0.9594	744.4
293.15	0.9688	743.56
293.15	0.9792	742.63
293.15	0.9902	741.63
298.15	0.0105	810.25
298.15	0.0197	809.68
298.15	0.0321	808.89
298.15	0.0401	808.37
298.15	0.0506	807.69
298.15	0.0595	807.12
298.15	0.0699	806.45
298.15	0.0811	805.73
298.15	0.0901	805.14
298.15	0.1042	804.23
298.15	0.1506	801.2
298.15	0.2078	797.36
298.15	0.2520	794.34
298.15	0.3010	790.96
298.15	0.3492	787.57
298.15	0.3996	783.99
298.15	0.4577	779.75
298.15	0.4985	776.76
298.15	0.5512	772.8
298.15	0.5999	769.09
298.15	0.6506	765.16
298.15	0.6986	761.39
298.15	0.7451	757.72
298.15	0.7976	753.3
298.15	0.8534	748.61
298.15	0.8980	744.73
298.15	0.9098	743.7
298.15	0.9195	742.85
298.15	0.9289	742.01
298.15	0.9419	740.85
298.15	0.9495	740.17
298.15	0.9594	739.28
298.15	0.9688	738.42
298.15	0.9792	737.46
298.15	0.9902	736.44
303.15	0.0105	806.55
303.15	0.0197	805.95
303.15	0.0321	805.15
303.15	0.0401	804.63
303.15	0.0506	803.93
303.15	0.0595	803.35
303.15	0.0699	802.67
303.15	0.0811	801.94
303.15	0.0901	801.33
303.15	0.1042	800.41
303.15	0.1506	797.3
303.15	0.2078	793.4
303.15	0.2520	790.33
303.15	0.3010	786.88
303.15	0.3492	783.41
303.15	0.3996	779.75
303.15	0.4577	775.42
303.15	0.4985	772.36
303.15	0.5512	768.33
303.15	0.5999	764.55
303.15	0.6506	760.51
303.15	0.6986	756.67
303.15	0.7451	752.92
303.15	0.7976	748.39
303.15	0.8534	743.59
303.15	0.8980	739.63
303.15	0.9098	738.59
303.15	0.9195	737.72
303.15	0.9289	736.85
303.15	0.9419	735.67
303.15	0.9495	734.96
303.15	0.9594	734.04
303.15	0.9688	733.17
303.15	0.9792	732.2
303.15	0.9902	731.16
308.15	0.0105	802.82
308.15	0.0197	802.2
308.15	0.0321	801.39
308.15	0.0401	800.86
308.15	0.0506	800.15
308.15	0.0595	799.56
308.15	0.0699	798.87
308.15	0.0811	798.11
308.15	0.0901	797.5
308.15	0.1042	796.55
308.15	0.1506	793.39
308.15	0.2078	789.41
308.15	0.2520	786.28
308.15	0.3010	782.75
308.15	0.3492	779.21
308.15	0.3996	775.48
308.15	0.4577	771.06
308.15	0.4985	767.93
308.15	0.5512	763.81
308.15	0.5999	759.95
308.15	0.6506	755.83
308.15	0.6986	751.9
308.15	0.7451	748.06
308.15	0.7976	743.42
308.15	0.8534	738.51
308.15	0.8980	734.47
308.15	0.9098	733.41
308.15	0.9195	732.53
308.15	0.9289	731.64
308.15	0.9419	730.43
308.15	0.9495	729.72
308.15	0.9594	728.78
308.15	0.9688	727.88
308.15	0.9792	726.89
308.15	0.9902	725.83

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	0.0105	813.89
293.15	0.0197	813.34
293.15	0.0321	812.56
293.15	0.0401	812.06
293.15	0.0506	811.39
293.15	0.0595	810.83
293.15	0.0699	810.18
293.15	0.0811	809.49
293.15	0.0901	808.93
293.15	0.1042	808.03
293.15	0.1506	805.02
293.15	0.2078	801.27
293.15	0.2520	798.32
293.15	0.3010	795.01
293.15	0.3492	791.65
293.15	0.3996	788.14
293.15	0.4577	784.0
293.15	0.4985	781.06
293.15	0.5512	777.21
293.15	0.5999	773.61
293.15	0.6506	769.72
293.15	0.6986	766.04
293.15	0.7451	762.49
293.15	0.7976	758.12
293.15	0.8534	753.55
293.15	0.8980	749.74
293.15	0.9098	748.75
293.15	0.9195	747.92
293.15	0.9289	747.1
293.15	0.9419	745.96
293.15	0.9495	745.29
293.15	0.9594	744.4
293.15	0.9688	743.56
293.15	0.9792	742.63
293.15	0.9902	741.63
298.15	0.0105	810.25
298.15	0.0197	809.68
298.15	0.0321	808.89
298.15	0.0401	808.37
298.15	0.0506	807.69
298.15	0.0595	807.12
298.15	0.0699	806.45
298.15	0.0811	805.73
298.15	0.0901	805.14
298.15	0.1042	804.23
298.15	0.1506	801.2
298.15	0.2078	797.36
298.15	0.2520	794.34
298.15	0.3010	790.96
298.15	0.3492	787.57
298.15	0.3996	783.99
298.15	0.4577	779.75
298.15	0.4985	776.76
298.15	0.5512	772.8
298.15	0.5999	769.09
298.15	0.6506	765.16
298.15	0.6986	761.39
298.15	0.7451	757.72
298.15	0.7976	753.3
298.15	0.8534	748.61
298.15	0.8980	744.73
298.15	0.9098	743.7
298.15	0.9195	742.85
298.15	0.9289	742.01
298.15	0.9419	740.85
298.15	0.9495	740.17
298.15	0.9594	739.28
298.15	0.9688	738.42
298.15	0.9792	737.46
298.15	0.9902	736.44
303.15	0.0105	806.55
303.15	0.0197	805.95
303.15	0.0321	805.15
303.15	0.0401	804.63
303.15	0.0506	803.93
303.15	0.0595	803.35
303.15	0.0699	802.67
303.15	0.0811	801.94
303.15	0.0901	801.33
303.15	0.1042	800.41
303.15	0.1506	797.3
303.15	0.2078	793.4
303.15	0.2520	790.33
303.15	0.3010	786.88
303.15	0.3492	783.41
303.15	0.3996	779.75
303.15	0.4577	775.42
303.15	0.4985	772.36
303.15	0.5512	768.33
303.15	0.5999	764.55
303.15	0.6506	760.51
303.15	0.6986	756.67
303.15	0.7451	752.92
303.15	0.7976	748.39
303.15	0.8534	743.59
303.15	0.8980	739.63
303.15	0.9098	738.59
303.15	0.9195	737.72
303.15	0.9289	736.85
303.15	0.9419	735.67
303.15	0.9495	734.96
303.15	0.9594	734.04
303.15	0.9688	733.17
303.15	0.9792	732.2
303.15	0.9902	731.16
308.15	0.0105	802.82
308.15	0.0197	802.2
308.15	0.0321	801.39
308.15	0.0401	800.86
308.15	0.0506	800.15
308.15	0.0595	799.56
308.15	0.0699	798.87
308.15	0.0811	798.11
308.15	0.0901	797.5
308.15	0.1042	796.55
308.15	0.1506	793.39
308.15	0.2078	789.41
308.15	0.2520	786.28
308.15	0.3010	782.75
308.15	0.3492	779.21
308.15	0.3996	775.48
308.15	0.4577	771.06
308.15	0.4985	767.93
308.15	0.5512	763.81
308.15	0.5999	759.95
308.15	0.6506	755.83
308.15	0.6986	751.9
308.15	0.7451	748.06
308.15	0.7976	743.42
308.15	0.8534	738.51
308.15	0.8980	734.47
308.15	0.9098	733.41
308.15	0.9195	732.53
308.15	0.9289	731.64
308.15	0.9419	730.43
308.15	0.9495	729.72
308.15	0.9594	728.78
308.15	0.9688	727.88
308.15	0.9792	726.89
308.15	0.9902	725.83

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
• Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas