Mixture of Diisopropyl ether + Cyclohexane, methyl-

Datasets

1. η - Viscosity, Pa*s (2)
2. n₀ - Refractive index (Na D-line) (2)
3. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0008
288.15	0.0502	0.0007
288.15	0.1000	0.0007
288.15	0.1500	0.0007
288.15	0.2000	0.0006
288.15	0.2500	0.0006
288.15	0.3000	0.0006
288.15	0.3500	0.0005
288.15	0.4000	0.0005
288.15	0.4500	0.0005
288.15	0.5000	0.0005
288.15	0.5500	0.0005
288.15	0.6000	0.0004
288.15	0.6500	0.0004
288.15	0.7000	0.0004
288.15	0.7500	0.0004
288.15	0.8000	0.0004
288.15	0.8500	0.0004
288.15	0.9000	0.0004
288.15	0.9500	0.0004
288.15	1.0000	0.0003
298.15	0.0000	0.0007
298.15	0.0502	0.0007
298.15	0.1000	0.0006
298.15	0.1500	0.0006
298.15	0.2000	0.0006
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0004
298.15	0.5000	0.0004
298.15	0.5500	0.0004
298.15	0.6000	0.0004
298.15	0.6500	0.0004
298.15	0.7000	0.0004
298.15	0.7500	0.0004
298.15	0.8000	0.0003
298.15	0.8500	0.0003
298.15	0.9000	0.0003
298.15	0.9500	0.0003
298.15	1.0000	0.0003
308.15	0.0000	0.0006
308.15	0.0502	0.0006
308.15	0.1000	0.0005
308.15	0.1500	0.0005
308.15	0.2000	0.0005
308.15	0.2500	0.0005
308.15	0.3000	0.0004
308.15	0.3500	0.0004
308.15	0.4000	0.0004
308.15	0.4500	0.0004
308.15	0.5000	0.0004
308.15	0.5500	0.0004
308.15	0.6000	0.0004
308.15	0.6500	0.0003
308.15	0.7000	0.0003
308.15	0.7500	0.0003
308.15	0.8000	0.0003
308.15	0.8500	0.0003
308.15	0.9000	0.0003
308.15	0.9500	0.0003
308.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0008
288.15	0.0502	0.0007
288.15	0.1000	0.0007
288.15	0.1500	0.0007
288.15	0.2000	0.0006
288.15	0.2500	0.0006
288.15	0.3000	0.0006
288.15	0.3500	0.0005
288.15	0.4000	0.0005
288.15	0.4500	0.0005
288.15	0.5000	0.0005
288.15	0.5500	0.0005
288.15	0.6000	0.0004
288.15	0.6500	0.0004
288.15	0.7000	0.0004
288.15	0.7500	0.0004
288.15	0.8000	0.0004
288.15	0.8500	0.0004
288.15	0.9000	0.0004
288.15	0.9500	0.0004
288.15	1.0000	0.0003
298.15	0.0000	0.0007
298.15	0.0502	0.0007
298.15	0.1000	0.0006
298.15	0.1500	0.0006
298.15	0.2000	0.0006
298.15	0.2500	0.0005
298.15	0.3000	0.0005
298.15	0.3500	0.0005
298.15	0.4000	0.0005
298.15	0.4500	0.0004
298.15	0.5000	0.0004
298.15	0.5500	0.0004
298.15	0.6000	0.0004
298.15	0.6500	0.0004
298.15	0.7000	0.0004
298.15	0.7500	0.0004
298.15	0.8000	0.0003
298.15	0.8500	0.0003
298.15	0.9000	0.0003
298.15	0.9500	0.0003
298.15	1.0000	0.0003
308.15	0.0000	0.0006
308.15	0.0502	0.0006
308.15	0.1000	0.0005
308.15	0.1500	0.0005
308.15	0.2000	0.0005
308.15	0.2500	0.0005
308.15	0.3000	0.0004
308.15	0.3500	0.0004
308.15	0.4000	0.0004
308.15	0.4500	0.0004
308.15	0.5000	0.0004
308.15	0.5500	0.0004
308.15	0.6000	0.0004
308.15	0.6500	0.0003
308.15	0.7000	0.0003
308.15	0.7500	0.0003
308.15	0.8000	0.0003
308.15	0.8500	0.0003
308.15	0.9000	0.0003
308.15	0.9500	0.0003
308.15	1.0000	0.0003

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4258
288.15	0.0502	1.4232
288.15	0.1000	1.4201
288.15	0.1500	1.4171
288.15	0.2000	1.4142
288.15	0.2500	1.4113
288.15	0.3000	1.4084
288.15	0.3500	1.4056
288.15	0.4000	1.4028
288.15	0.4500	1.4
288.15	0.5000	1.3972
288.15	0.5500	1.3945
288.15	0.6000	1.3918
288.15	0.6500	1.3891
288.15	0.7000	1.3865
288.15	0.7500	1.3839
288.15	0.8000	1.3814
288.15	0.8500	1.3788
288.15	0.9000	1.3763
288.15	0.9500	1.3738
288.15	1.0000	1.3713
298.15	0.0000	1.4205
298.15	0.0502	1.4176
298.15	0.1000	1.4146
298.15	0.1500	1.4116
298.15	0.2000	1.4086
298.15	0.2500	1.4057
298.15	0.3000	1.4028
298.15	0.3500	1.3999
298.15	0.4000	1.3971
298.15	0.4500	1.3943
298.15	0.5000	1.3915
298.15	0.5500	1.3888
298.15	0.6000	1.3861
298.15	0.6500	1.3835
298.15	0.7000	1.3808
298.15	0.7500	1.3782
298.15	0.8000	1.3757
298.15	0.8500	1.3731
298.15	0.9000	1.3705
298.15	0.9500	1.368
298.15	1.0000	1.3654
308.15	0.0000	1.4154
308.15	0.0502	1.4125
308.15	0.1000	1.4096
308.15	0.1500	1.4066
308.15	0.2000	1.4037
308.15	0.2500	1.4007
308.15	0.3000	1.3978
308.15	0.3500	1.3948
308.15	0.4000	1.392
308.15	0.4500	1.3891
308.15	0.5000	1.3863
308.15	0.5500	1.3836
308.15	0.6000	1.3808
308.15	0.6500	1.3782
308.15	0.7000	1.3755
308.15	0.7500	1.3729
308.15	0.8000	1.3702
308.15	0.8500	1.3677
308.15	0.9000	1.365
308.15	0.9500	1.3624
308.15	1.0000	1.3595

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4258
288.15	0.0502	1.4232
288.15	0.1000	1.4201
288.15	0.1500	1.4171
288.15	0.2000	1.4142
288.15	0.2500	1.4113
288.15	0.3000	1.4084
288.15	0.3500	1.4056
288.15	0.4000	1.4028
288.15	0.4500	1.4
288.15	0.5000	1.3972
288.15	0.5500	1.3945
288.15	0.6000	1.3918
288.15	0.6500	1.3891
288.15	0.7000	1.3865
288.15	0.7500	1.3839
288.15	0.8000	1.3814
288.15	0.8500	1.3788
288.15	0.9000	1.3763
288.15	0.9500	1.3738
288.15	1.0000	1.3713
298.15	0.0000	1.4205
298.15	0.0502	1.4176
298.15	0.1000	1.4146
298.15	0.1500	1.4116
298.15	0.2000	1.4086
298.15	0.2500	1.4057
298.15	0.3000	1.4028
298.15	0.3500	1.3999
298.15	0.4000	1.3971
298.15	0.4500	1.3943
298.15	0.5000	1.3915
298.15	0.5500	1.3888
298.15	0.6000	1.3861
298.15	0.6500	1.3835
298.15	0.7000	1.3808
298.15	0.7500	1.3782
298.15	0.8000	1.3757
298.15	0.8500	1.3731
298.15	0.9000	1.3705
298.15	0.9500	1.368
298.15	1.0000	1.3654
308.15	0.0000	1.4154
308.15	0.0502	1.4125
308.15	0.1000	1.4096
308.15	0.1500	1.4066
308.15	0.2000	1.4037
308.15	0.2500	1.4007
308.15	0.3000	1.3978
308.15	0.3500	1.3948
308.15	0.4000	1.392
308.15	0.4500	1.3891
308.15	0.5000	1.3863
308.15	0.5500	1.3836
308.15	0.6000	1.3808
308.15	0.6500	1.3782
308.15	0.7000	1.3755
308.15	0.7500	1.3729
308.15	0.8000	1.3702
308.15	0.8500	1.3677
308.15	0.9000	1.365
308.15	0.9500	1.3624
308.15	1.0000	1.3595

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	773.4
288.15	0.0502	771.3
288.15	0.1000	768.9
288.15	0.1500	766.6
288.15	0.2000	764.3
288.15	0.2500	761.9
288.15	0.3000	759.6
288.15	0.3500	757.4
288.15	0.4000	755.1
288.15	0.4500	752.8
288.15	0.5000	750.6
288.15	0.5500	748.4
288.15	0.6000	746.2
288.15	0.6500	743.9
288.15	0.7000	741.7
288.15	0.7500	739.6
288.15	0.8000	737.4
288.15	0.8500	735.3
288.15	0.9000	733.1
288.15	0.9500	731.0
288.15	1.0000	729.0
298.15	0.0000	765.0
298.15	0.0502	762.5
298.15	0.1000	760.1
298.15	0.1500	757.7
298.15	0.2000	755.3
298.15	0.2500	752.9
298.15	0.3000	750.5
298.15	0.3500	748.1
298.15	0.4000	745.8
298.15	0.4500	743.4
298.15	0.5000	741.1
298.15	0.5500	738.8
298.15	0.6000	736.5
298.15	0.6500	734.2
298.15	0.7000	731.9
298.15	0.7500	729.6
298.15	0.8000	727.3
298.15	0.8500	725.1
298.15	0.9000	722.9
298.15	0.9500	720.6
298.15	1.0000	718.6
308.15	0.0000	756.3
308.15	0.0502	753.8
308.15	0.1000	751.3
308.15	0.1500	748.8
308.15	0.2000	746.3
308.15	0.2500	743.8
308.15	0.3000	741.3
308.15	0.3500	738.9
308.15	0.4000	736.4
308.15	0.4500	734.0
308.15	0.5000	731.6
308.15	0.5500	729.2
308.15	0.6000	726.8
308.15	0.6500	724.4
308.15	0.7000	722.0
308.15	0.7500	719.6
308.15	0.8000	717.3
308.15	0.8500	714.9
308.15	0.9000	712.6
308.15	0.9500	710.3
308.15	1.0000	707.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	773.4
288.15	0.0502	771.3
288.15	0.1000	768.9
288.15	0.1500	766.6
288.15	0.2000	764.3
288.15	0.2500	761.9
288.15	0.3000	759.6
288.15	0.3500	757.4
288.15	0.4000	755.1
288.15	0.4500	752.8
288.15	0.5000	750.6
288.15	0.5500	748.4
288.15	0.6000	746.2
288.15	0.6500	743.9
288.15	0.7000	741.7
288.15	0.7500	739.6
288.15	0.8000	737.4
288.15	0.8500	735.3
288.15	0.9000	733.1
288.15	0.9500	731.0
288.15	1.0000	729.0
298.15	0.0000	765.0
298.15	0.0502	762.5
298.15	0.1000	760.1
298.15	0.1500	757.7
298.15	0.2000	755.3
298.15	0.2500	752.9
298.15	0.3000	750.5
298.15	0.3500	748.1
298.15	0.4000	745.8
298.15	0.4500	743.4
298.15	0.5000	741.1
298.15	0.5500	738.8
298.15	0.6000	736.5
298.15	0.6500	734.2
298.15	0.7000	731.9
298.15	0.7500	729.6
298.15	0.8000	727.3
298.15	0.8500	725.1
298.15	0.9000	722.9
298.15	0.9500	720.6
298.15	1.0000	718.6
308.15	0.0000	756.3
308.15	0.0502	753.8
308.15	0.1000	751.3
308.15	0.1500	748.8
308.15	0.2000	746.3
308.15	0.2500	743.8
308.15	0.3000	741.3
308.15	0.3500	738.9
308.15	0.4000	736.4
308.15	0.4500	734.0
308.15	0.5000	731.6
308.15	0.5500	729.2
308.15	0.6000	726.8
308.15	0.6500	724.4
308.15	0.7000	722.0
308.15	0.7500	719.6
308.15	0.8000	717.3
308.15	0.8500	714.9
308.15	0.9000	712.6
308.15	0.9500	710.3
308.15	1.0000	707.9

Sources

• Densities and Viscosities for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and Methylcyclohexane