Mixture of Diisopropyl ether + Ethanol

Datasets

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

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Mole fraction of Diisopropyl ether (1) - Gas
0.0440	0.1540
0.0890	0.2560
0.1430	0.3390
0.1930	0.4030
0.2400	0.4520
0.2870	0.4900
0.3380	0.5230
0.3890	0.5520
0.4400	0.5780
0.4890	0.6040
0.5370	0.6310
0.5980	0.6510
0.6490	0.6750
0.7050	0.7030
0.7570	0.7300
0.8090	0.7600
0.8590	0.7950
0.9070	0.8480
0.9540	0.9150

Mole fraction of Diisopropyl ether (1) [ref]

Fixed		Measured
Mole fraction of Diisopropyl ether (1) - Liquid	Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Gas
0.0630	313.15	0.3590
0.1250	313.15	0.4800
0.1790	313.15	0.5460
0.2230	313.15	0.5850
0.2730	313.15	0.6110
0.3400	313.15	0.6400
0.4200	313.15	0.6630
0.6510	313.15	0.6910
0.7140	313.15	0.7140
0.7260	313.15	0.7260
0.8950	313.15	0.8210
0.0860	323.15	0.3670
0.1680	323.15	0.4990
0.2590	323.15	0.5670
0.3450	323.15	0.6050
0.4160	323.15	0.6250
0.5680	323.15	0.6540
0.6960	323.15	0.6980
0.7060	323.15	0.7170
0.7790	323.15	0.7280
0.8810	323.15	0.7890
0.9450	323.15	0.8620
0.0640	333.15	0.2960
0.1250	333.15	0.4050
0.2350	333.15	0.5180
0.3000	333.15	0.5640
0.3790	333.15	0.5990
0.5210	333.15	0.6230
0.6710	333.15	0.6750
0.6840	333.15	0.6860
0.8100	333.15	0.7020
0.8860	333.15	0.7670
0.9370	333.15	0.8380

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Diisopropyl ether (1) - Liquid	Mole fraction of Diisopropyl ether (1) - Gas
0.0201	0.0995
0.0398	0.1534
0.0596	0.2098
0.0795	0.2604
0.1194	0.3404
0.1694	0.3934
0.2290	0.4571
0.2891	0.4849
0.3492	0.5223
0.4095	0.5568
0.4690	0.5918
0.5292	0.6298
0.5889	0.6653
0.6498	0.6994
0.7099	0.7328
0.7694	0.7669
0.8301	0.8072
0.8804	0.8491
0.9196	0.8841
0.9398	0.9090
0.9606	0.9361
0.9811	0.9621

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Mole fraction of Diisopropyl ether (1) - Gas
0.0440	0.1540
0.0890	0.2560
0.1430	0.3390
0.1930	0.4030
0.2400	0.4520
0.2870	0.4900
0.3380	0.5230
0.3890	0.5520
0.4400	0.5780
0.4890	0.6040
0.5370	0.6310
0.5980	0.6510
0.6490	0.6750
0.7050	0.7030
0.7570	0.7300
0.8090	0.7600
0.8590	0.7950
0.9070	0.8480
0.9540	0.9150

Mole fraction of Diisopropyl ether (1) [ref]

Fixed		Measured
Mole fraction of Diisopropyl ether (1) - Liquid	Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Gas
0.0630	313.15	0.3590
0.1250	313.15	0.4800
0.1790	313.15	0.5460
0.2230	313.15	0.5850
0.2730	313.15	0.6110
0.3400	313.15	0.6400
0.4200	313.15	0.6630
0.6510	313.15	0.6910
0.7140	313.15	0.7140
0.7260	313.15	0.7260
0.8950	313.15	0.8210
0.0860	323.15	0.3670
0.1680	323.15	0.4990
0.2590	323.15	0.5670
0.3450	323.15	0.6050
0.4160	323.15	0.6250
0.5680	323.15	0.6540
0.6960	323.15	0.6980
0.7060	323.15	0.7170
0.7790	323.15	0.7280
0.8810	323.15	0.7890
0.9450	323.15	0.8620
0.0640	333.15	0.2960
0.1250	333.15	0.4050
0.2350	333.15	0.5180
0.3000	333.15	0.5640
0.3790	333.15	0.5990
0.5210	333.15	0.6230
0.6710	333.15	0.6750
0.6840	333.15	0.6860
0.8100	333.15	0.7020
0.8860	333.15	0.7670
0.9370	333.15	0.8380

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Diisopropyl ether (1) - Liquid	Mole fraction of Diisopropyl ether (1) - Gas
0.0201	0.0995
0.0398	0.1534
0.0596	0.2098
0.0795	0.2604
0.1194	0.3404
0.1694	0.3934
0.2290	0.4571
0.2891	0.4849
0.3492	0.5223
0.4095	0.5568
0.4690	0.5918
0.5292	0.6298
0.5889	0.6653
0.6498	0.6994
0.7099	0.7328
0.7694	0.7669
0.8301	0.8072
0.8804	0.8491
0.9196	0.8841
0.9398	0.9090
0.9606	0.9361
0.9811	0.9621

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	0.0013
288.15	0.0500	0.0012
288.15	0.1000	0.0010
288.15	0.1500	0.0009
288.15	0.2000	0.0009
288.15	0.2500	0.0008
288.15	0.3000	0.0007
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0006
288.15	0.5000	0.0005
288.15	0.5500	0.0005
288.15	0.6000	0.0005
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	0.0011
298.15	0.0500	0.0010
298.15	0.1000	0.0009
298.15	0.1500	0.0008
298.15	0.2000	0.0007
298.15	0.2500	0.0007
298.15	0.3000	0.0006
298.15	0.3500	0.0006
298.15	0.4000	0.0005
298.15	0.4500	0.0005
298.15	0.5000	0.0005
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	0.0009
308.15	0.0500	0.0008
308.15	0.1000	0.0007
308.15	0.1500	0.0007
308.15	0.2000	0.0006
308.15	0.2500	0.0006
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
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 = 100.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0013
288.15	0.0500	0.0012
288.15	0.1000	0.0010
288.15	0.1500	0.0009
288.15	0.2000	0.0008
288.15	0.2500	0.0008
288.15	0.3000	0.0007
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0006
288.15	0.5000	0.0005
288.15	0.5500	0.0005
288.15	0.6000	0.0005
288.15	0.6500	0.0004
288.15	0.7000	0.0004
288.15	0.7499	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	0.0011
298.15	0.0500	0.0010
298.15	0.1000	0.0009
298.15	0.1500	0.0008
298.15	0.2000	0.0007
298.15	0.2500	0.0007
298.15	0.3000	0.0006
298.15	0.3500	0.0006
298.15	0.4000	0.0005
298.15	0.4500	0.0005
298.15	0.5000	0.0005
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	0.7499	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	0.0009
308.15	0.0500	0.0008
308.15	0.1000	0.0007
308.15	0.1500	0.0007
308.15	0.2000	0.0006
308.15	0.2500	0.0006
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
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	0.7499	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	0.0013
288.15	0.0500	0.0012
288.15	0.1000	0.0010
288.15	0.1500	0.0009
288.15	0.2000	0.0009
288.15	0.2500	0.0008
288.15	0.3000	0.0007
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0006
288.15	0.5000	0.0005
288.15	0.5500	0.0005
288.15	0.6000	0.0005
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	0.0011
298.15	0.0500	0.0010
298.15	0.1000	0.0009
298.15	0.1500	0.0008
298.15	0.2000	0.0007
298.15	0.2500	0.0007
298.15	0.3000	0.0006
298.15	0.3500	0.0006
298.15	0.4000	0.0005
298.15	0.4500	0.0005
298.15	0.5000	0.0005
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	0.0009
308.15	0.0500	0.0008
308.15	0.1000	0.0007
308.15	0.1500	0.0007
308.15	0.2000	0.0006
308.15	0.2500	0.0006
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
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 = 100.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0013
288.15	0.0500	0.0012
288.15	0.1000	0.0010
288.15	0.1500	0.0009
288.15	0.2000	0.0008
288.15	0.2500	0.0008
288.15	0.3000	0.0007
288.15	0.3500	0.0006
288.15	0.4000	0.0006
288.15	0.4500	0.0006
288.15	0.5000	0.0005
288.15	0.5500	0.0005
288.15	0.6000	0.0005
288.15	0.6500	0.0004
288.15	0.7000	0.0004
288.15	0.7499	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	0.0011
298.15	0.0500	0.0010
298.15	0.1000	0.0009
298.15	0.1500	0.0008
298.15	0.2000	0.0007
298.15	0.2500	0.0007
298.15	0.3000	0.0006
298.15	0.3500	0.0006
298.15	0.4000	0.0005
298.15	0.4500	0.0005
298.15	0.5000	0.0005
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	0.7499	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	0.0009
308.15	0.0500	0.0008
308.15	0.1000	0.0007
308.15	0.1500	0.0007
308.15	0.2000	0.0006
308.15	0.2500	0.0006
308.15	0.3000	0.0005
308.15	0.3500	0.0005
308.15	0.4000	0.0005
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	0.7499	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

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0212	0.0100
0.0437	0.0219
0.0676	0.0377
0.0931	0.0571
0.1204	0.0793
0.1497	0.1050
0.1811	0.1343
0.2150	0.1668
0.2516	0.2020
0.2912	0.2401
0.3343	0.2766
0.3813	0.3183
0.4328	0.3599
0.4894	0.4008
0.5521	0.4341
0.6217	0.4603
0.6995	0.4710
0.7871	0.4411
0.8864	0.3275

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0212	0.0100
0.0437	0.0219
0.0676	0.0377
0.0931	0.0571
0.1204	0.0793
0.1497	0.1050
0.1811	0.1343
0.2150	0.1668
0.2516	0.2020
0.2912	0.2401
0.3343	0.2766
0.3813	0.3183
0.4328	0.3599
0.4894	0.4008
0.5521	0.4341
0.6217	0.4603
0.6995	0.4710
0.7871	0.4411
0.8864	0.3275

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Diisopropyl ether (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0630	313.15	26.73
0.1250	313.15	31.97
0.1790	313.15	34.90
0.2230	313.15	36.78
0.2730	313.15	38.37
0.3400	313.15	40.06
0.4200	313.15	41.10
0.6510	313.15	42.19
0.7140	313.15	42.22
0.7260	313.15	42.45
0.8950	313.15	41.76
0.0860	323.15	44.39
0.1680	323.15	52.56
0.2590	323.15	57.19
0.3450	323.15	59.95
0.4160	323.15	61.26
0.5680	323.15	62.56
0.6960	323.15	63.64
0.7060	323.15	63.52
0.7790	323.15	63.46
0.8810	323.15	61.96
0.9450	323.15	59.51
0.0640	333.15	63.85
0.1250	333.15	72.89
0.2350	333.15	83.06
0.3000	333.15	87.47
0.3790	333.15	89.96
0.5210	333.15	91.68
0.6710	333.15	92.73
0.6840	333.15	92.75
0.8100	333.15	92.67
0.8860	333.15	89.87
0.9370	333.15	85.95

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Diisopropyl ether (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0630	313.15	26.73
0.1250	313.15	31.97
0.1790	313.15	34.90
0.2230	313.15	36.78
0.2730	313.15	38.37
0.3400	313.15	40.06
0.4200	313.15	41.10
0.6510	313.15	42.19
0.7140	313.15	42.22
0.7260	313.15	42.45
0.8950	313.15	41.76
0.0860	323.15	44.39
0.1680	323.15	52.56
0.2590	323.15	57.19
0.3450	323.15	59.95
0.4160	323.15	61.26
0.5680	323.15	62.56
0.6960	323.15	63.64
0.7060	323.15	63.52
0.7790	323.15	63.46
0.8810	323.15	61.96
0.9450	323.15	59.51
0.0640	333.15	63.85
0.1250	333.15	72.89
0.2350	333.15	83.06
0.3000	333.15	87.47
0.3790	333.15	89.96
0.5210	333.15	91.68
0.6710	333.15	92.73
0.6840	333.15	92.75
0.8100	333.15	92.67
0.8860	333.15	89.87
0.9370	333.15	85.95

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	1.3635
288.15	0.0500	1.3657
288.15	0.1000	1.367
288.15	0.1500	1.368
288.15	0.2000	1.3688
288.15	0.2500	1.3695
288.15	0.3000	1.3701
288.15	0.3500	1.3706
288.15	0.4000	1.371
288.15	0.4500	1.3713
288.15	0.5000	1.3716
288.15	0.5500	1.3718
288.15	0.6000	1.3719
288.15	0.6500	1.372
288.15	0.7000	1.372
288.15	0.7500	1.3719
288.15	0.8000	1.3719
288.15	0.8500	1.3718
288.15	0.9000	1.3716
288.15	0.9500	1.3714
288.15	1.0000	1.3713
298.15	0.0000	1.3594
298.15	0.0500	1.361
298.15	0.1000	1.3621
298.15	0.1500	1.3632
298.15	0.2000	1.3639
298.15	0.2500	1.3646
298.15	0.3000	1.3651
298.15	0.3500	1.3655
298.15	0.4000	1.3659
298.15	0.4500	1.3661
298.15	0.5000	1.3663
298.15	0.5500	1.3664
298.15	0.6000	1.3665
298.15	0.6500	1.3665
298.15	0.7000	1.3665
298.15	0.7500	1.3664
298.15	0.8000	1.3663
298.15	0.8500	1.3662
298.15	0.9000	1.366
298.15	0.9500	1.3657
298.15	1.0000	1.3654
308.15	0.0000	1.355
308.15	0.0500	1.3565
308.15	0.1000	1.3576
308.15	0.1500	1.3585
308.15	0.2000	1.3593
308.15	0.2500	1.3598
308.15	0.3000	1.3602
308.15	0.3500	1.3606
308.15	0.4000	1.3608
308.15	0.4500	1.361
308.15	0.5000	1.3611
308.15	0.5500	1.3612
308.15	0.6000	1.3612
308.15	0.6500	1.3612
308.15	0.7000	1.3611
308.15	0.7500	1.361
308.15	0.8000	1.3609
308.15	0.8500	1.3607
308.15	0.9000	1.3604
308.15	0.9500	1.36
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	1.3634
288.15	0.0500	1.365
288.15	0.1000	1.3665
288.15	0.1500	1.3677
288.15	0.2000	1.3686
288.15	0.2500	1.3694
288.15	0.3000	1.37
288.15	0.3500	1.3705
288.15	0.4000	1.3709
288.15	0.4500	1.3712
288.15	0.5000	1.3714
288.15	0.5500	1.3716
288.15	0.6000	1.3717
288.15	0.6500	1.3718
288.15	0.7000	1.3719
288.15	0.7499	1.3719
288.15	0.8000	1.3718
288.15	0.8500	1.3717
288.15	0.9000	1.3715
288.15	0.9500	1.3712
288.15	1.0000	1.3709
298.15	0.0000	1.3592
298.15	0.0500	1.3608
298.15	0.1000	1.3621
298.15	0.1500	1.3631
298.15	0.2000	1.3639
298.15	0.2500	1.3646
298.15	0.3000	1.3651
298.15	0.3500	1.3655
298.15	0.4000	1.3658
298.15	0.4500	1.3661
298.15	0.5000	1.3663
298.15	0.5500	1.3664
298.15	0.6000	1.3665
298.15	0.6500	1.3665
298.15	0.7000	1.3665
298.15	0.7499	1.3664
298.15	0.8000	1.3663
298.15	0.8500	1.3661
298.15	0.9000	1.3659
298.15	0.9500	1.3656
298.15	1.0000	1.3652
308.15	0.0000	1.355
308.15	0.0500	1.3565
308.15	0.1000	1.3576
308.15	0.1500	1.3585
308.15	0.2000	1.3592
308.15	0.2500	1.3598
308.15	0.3000	1.3602
308.15	0.3500	1.3605
308.15	0.4000	1.3608
308.15	0.4500	1.3609
308.15	0.5000	1.361
308.15	0.5500	1.3611
308.15	0.6000	1.3611
308.15	0.6500	1.3611
308.15	0.7000	1.361
308.15	0.7499	1.3608
308.15	0.8000	1.3607
308.15	0.8500	1.3604
308.15	0.9000	1.3602
308.15	0.9500	1.3599
308.15	1.0000	1.3594

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3573
0.0495	1.3585
0.0994	1.3599
0.2002	1.3615
0.2997	1.3623
0.4003	1.3633
0.5012	1.3631
0.6012	1.3628
0.7018	1.3622
0.8040	1.3625
0.8996	1.3621
0.9505	1.363
1.0000	1.3642

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	1.3635
288.15	0.0500	1.3657
288.15	0.1000	1.367
288.15	0.1500	1.368
288.15	0.2000	1.3688
288.15	0.2500	1.3695
288.15	0.3000	1.3701
288.15	0.3500	1.3706
288.15	0.4000	1.371
288.15	0.4500	1.3713
288.15	0.5000	1.3716
288.15	0.5500	1.3718
288.15	0.6000	1.3719
288.15	0.6500	1.372
288.15	0.7000	1.372
288.15	0.7500	1.3719
288.15	0.8000	1.3719
288.15	0.8500	1.3718
288.15	0.9000	1.3716
288.15	0.9500	1.3714
288.15	1.0000	1.3713
298.15	0.0000	1.3594
298.15	0.0500	1.361
298.15	0.1000	1.3621
298.15	0.1500	1.3632
298.15	0.2000	1.3639
298.15	0.2500	1.3646
298.15	0.3000	1.3651
298.15	0.3500	1.3655
298.15	0.4000	1.3659
298.15	0.4500	1.3661
298.15	0.5000	1.3663
298.15	0.5500	1.3664
298.15	0.6000	1.3665
298.15	0.6500	1.3665
298.15	0.7000	1.3665
298.15	0.7500	1.3664
298.15	0.8000	1.3663
298.15	0.8500	1.3662
298.15	0.9000	1.366
298.15	0.9500	1.3657
298.15	1.0000	1.3654
308.15	0.0000	1.355
308.15	0.0500	1.3565
308.15	0.1000	1.3576
308.15	0.1500	1.3585
308.15	0.2000	1.3593
308.15	0.2500	1.3598
308.15	0.3000	1.3602
308.15	0.3500	1.3606
308.15	0.4000	1.3608
308.15	0.4500	1.361
308.15	0.5000	1.3611
308.15	0.5500	1.3612
308.15	0.6000	1.3612
308.15	0.6500	1.3612
308.15	0.7000	1.3611
308.15	0.7500	1.361
308.15	0.8000	1.3609
308.15	0.8500	1.3607
308.15	0.9000	1.3604
308.15	0.9500	1.36
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	1.3634
288.15	0.0500	1.365
288.15	0.1000	1.3665
288.15	0.1500	1.3677
288.15	0.2000	1.3686
288.15	0.2500	1.3694
288.15	0.3000	1.37
288.15	0.3500	1.3705
288.15	0.4000	1.3709
288.15	0.4500	1.3712
288.15	0.5000	1.3714
288.15	0.5500	1.3716
288.15	0.6000	1.3717
288.15	0.6500	1.3718
288.15	0.7000	1.3719
288.15	0.7499	1.3719
288.15	0.8000	1.3718
288.15	0.8500	1.3717
288.15	0.9000	1.3715
288.15	0.9500	1.3712
288.15	1.0000	1.3709
298.15	0.0000	1.3592
298.15	0.0500	1.3608
298.15	0.1000	1.3621
298.15	0.1500	1.3631
298.15	0.2000	1.3639
298.15	0.2500	1.3646
298.15	0.3000	1.3651
298.15	0.3500	1.3655
298.15	0.4000	1.3658
298.15	0.4500	1.3661
298.15	0.5000	1.3663
298.15	0.5500	1.3664
298.15	0.6000	1.3665
298.15	0.6500	1.3665
298.15	0.7000	1.3665
298.15	0.7499	1.3664
298.15	0.8000	1.3663
298.15	0.8500	1.3661
298.15	0.9000	1.3659
298.15	0.9500	1.3656
298.15	1.0000	1.3652
308.15	0.0000	1.355
308.15	0.0500	1.3565
308.15	0.1000	1.3576
308.15	0.1500	1.3585
308.15	0.2000	1.3592
308.15	0.2500	1.3598
308.15	0.3000	1.3602
308.15	0.3500	1.3605
308.15	0.4000	1.3608
308.15	0.4500	1.3609
308.15	0.5000	1.361
308.15	0.5500	1.3611
308.15	0.6000	1.3611
308.15	0.6500	1.3611
308.15	0.7000	1.361
308.15	0.7499	1.3608
308.15	0.8000	1.3607
308.15	0.8500	1.3604
308.15	0.9000	1.3602
308.15	0.9500	1.3599
308.15	1.0000	1.3594

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3573
0.0495	1.3585
0.0994	1.3599
0.2002	1.3615
0.2997	1.3623
0.4003	1.3633
0.5012	1.3631
0.6012	1.3628
0.7018	1.3622
0.8040	1.3625
0.8996	1.3621
0.9505	1.363
1.0000	1.3642

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
0.1072	774.5
0.2007	766.1
0.3086	757.6
0.4030	751.0
0.4811	746.0
0.6142	738.3
0.6993	733.8
0.7432	731.7
0.7863	729.6
0.8965	724.4
0.9129	723.6

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	793.6
288.15	0.0500	788.3
288.15	0.1000	783.4
288.15	0.1500	778.8
288.15	0.2000	774.7
288.15	0.2500	770.7
288.15	0.3000	766.9
288.15	0.3500	763.3
288.15	0.4000	760.0
288.15	0.4500	756.9
288.15	0.5000	753.8
288.15	0.5500	751.0
288.15	0.6000	748.3
288.15	0.6500	745.7
288.15	0.7000	743.2
288.15	0.7500	740.7
288.15	0.8000	738.3
288.15	0.8500	735.8
288.15	0.9000	733.5
288.15	0.9500	731.1
288.15	1.0000	729.0
298.15	0.0000	785.2
298.15	0.0500	779.8
298.15	0.1000	774.8
298.15	0.1500	770.0
298.15	0.2000	765.7
298.15	0.2500	761.4
298.15	0.3000	757.5
298.15	0.3500	753.9
298.15	0.4000	750.4
298.15	0.4500	747.1
298.15	0.5000	744.1
298.15	0.5500	741.2
298.15	0.6000	738.4
298.15	0.6500	735.8
298.15	0.7000	733.2
298.15	0.7500	730.7
298.15	0.8000	728.3
298.15	0.8500	725.8
298.15	0.9000	723.4
298.15	0.9500	720.9
298.15	1.0000	718.6
308.15	0.0000	776.5
308.15	0.0500	771.0
308.15	0.1000	765.8
308.15	0.1500	760.9
308.15	0.2000	756.4
308.15	0.2500	752.0
308.15	0.3000	747.9
308.15	0.3500	744.2
308.15	0.4000	740.7
308.15	0.4500	737.3
308.15	0.5000	734.1
308.15	0.5500	731.1
308.15	0.6000	728.3
308.15	0.6500	725.6
308.15	0.7000	723.0
308.15	0.7500	720.5
308.15	0.8000	718.0
308.15	0.8500	715.5
308.15	0.9000	713.1
308.15	0.9500	710.6
308.15	1.0000	707.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	793.74
288.15	0.0500	788.65
288.15	0.1000	783.6
288.15	0.1500	779.02
288.15	0.2000	774.89
288.15	0.2500	770.69
288.15	0.3000	766.92
288.15	0.3500	763.36
288.15	0.4000	760.02
288.15	0.4500	756.93
288.15	0.5000	753.87
288.15	0.5500	750.98
288.15	0.6000	748.29
288.15	0.6500	745.73
288.15	0.7000	743.19
288.15	0.7499	740.73
288.15	0.8000	738.4
288.15	0.8500	735.94
288.15	0.9000	733.6
288.15	0.9500	731.15
288.15	1.0000	729.09
298.15	0.0000	785.17
298.15	0.0500	779.96
298.15	0.1000	774.78
298.15	0.1500	770.05
298.15	0.2000	765.79
298.15	0.2500	761.45
298.15	0.3000	757.63
298.15	0.3500	753.93
298.15	0.4000	750.47
298.15	0.4500	747.28
298.15	0.5000	744.13
298.15	0.5500	741.18
298.15	0.6000	738.39
298.15	0.6500	735.73
298.15	0.7000	733.1
298.15	0.7499	730.59
298.15	0.8000	728.19
298.15	0.8500	725.76
298.15	0.9000	723.36
298.15	0.9500	720.98
298.15	1.0000	718.7
308.15	0.0000	776.49
308.15	0.0500	771.13
308.15	0.1000	765.84
308.15	0.1500	760.98
308.15	0.2000	756.58
308.15	0.2500	752.16
308.15	0.3000	748.12
308.15	0.3500	744.32
308.15	0.4000	740.76
308.15	0.4500	737.5
308.15	0.5000	734.3
308.15	0.5500	731.25
308.15	0.6000	728.37
308.15	0.6500	725.59
308.15	0.7000	722.86
308.15	0.7499	720.23
308.15	0.8000	717.79
308.15	0.8500	715.31
308.15	0.9000	712.89
308.15	0.9500	710.53
308.15	1.0000	708.12

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	781.99
0.0495	776.55
0.0994	771.45
0.2002	762.41
0.2997	754.04
0.4003	746.63
0.5012	740.01
0.6012	734.1
0.7018	728.75
0.8040	723.6
0.8996	718.96
0.9505	716.37
1.0000	713.78

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
0.1072	774.5
0.2007	766.1
0.3086	757.6
0.4030	751.0
0.4811	746.0
0.6142	738.3
0.6993	733.8
0.7432	731.7
0.7863	729.6
0.8965	724.4
0.9129	723.6

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	793.6
288.15	0.0500	788.3
288.15	0.1000	783.4
288.15	0.1500	778.8
288.15	0.2000	774.7
288.15	0.2500	770.7
288.15	0.3000	766.9
288.15	0.3500	763.3
288.15	0.4000	760.0
288.15	0.4500	756.9
288.15	0.5000	753.8
288.15	0.5500	751.0
288.15	0.6000	748.3
288.15	0.6500	745.7
288.15	0.7000	743.2
288.15	0.7500	740.7
288.15	0.8000	738.3
288.15	0.8500	735.8
288.15	0.9000	733.5
288.15	0.9500	731.1
288.15	1.0000	729.0
298.15	0.0000	785.2
298.15	0.0500	779.8
298.15	0.1000	774.8
298.15	0.1500	770.0
298.15	0.2000	765.7
298.15	0.2500	761.4
298.15	0.3000	757.5
298.15	0.3500	753.9
298.15	0.4000	750.4
298.15	0.4500	747.1
298.15	0.5000	744.1
298.15	0.5500	741.2
298.15	0.6000	738.4
298.15	0.6500	735.8
298.15	0.7000	733.2
298.15	0.7500	730.7
298.15	0.8000	728.3
298.15	0.8500	725.8
298.15	0.9000	723.4
298.15	0.9500	720.9
298.15	1.0000	718.6
308.15	0.0000	776.5
308.15	0.0500	771.0
308.15	0.1000	765.8
308.15	0.1500	760.9
308.15	0.2000	756.4
308.15	0.2500	752.0
308.15	0.3000	747.9
308.15	0.3500	744.2
308.15	0.4000	740.7
308.15	0.4500	737.3
308.15	0.5000	734.1
308.15	0.5500	731.1
308.15	0.6000	728.3
308.15	0.6500	725.6
308.15	0.7000	723.0
308.15	0.7500	720.5
308.15	0.8000	718.0
308.15	0.8500	715.5
308.15	0.9000	713.1
308.15	0.9500	710.6
308.15	1.0000	707.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	793.74
288.15	0.0500	788.65
288.15	0.1000	783.6
288.15	0.1500	779.02
288.15	0.2000	774.89
288.15	0.2500	770.69
288.15	0.3000	766.92
288.15	0.3500	763.36
288.15	0.4000	760.02
288.15	0.4500	756.93
288.15	0.5000	753.87
288.15	0.5500	750.98
288.15	0.6000	748.29
288.15	0.6500	745.73
288.15	0.7000	743.19
288.15	0.7499	740.73
288.15	0.8000	738.4
288.15	0.8500	735.94
288.15	0.9000	733.6
288.15	0.9500	731.15
288.15	1.0000	729.09
298.15	0.0000	785.17
298.15	0.0500	779.96
298.15	0.1000	774.78
298.15	0.1500	770.05
298.15	0.2000	765.79
298.15	0.2500	761.45
298.15	0.3000	757.63
298.15	0.3500	753.93
298.15	0.4000	750.47
298.15	0.4500	747.28
298.15	0.5000	744.13
298.15	0.5500	741.18
298.15	0.6000	738.39
298.15	0.6500	735.73
298.15	0.7000	733.1
298.15	0.7499	730.59
298.15	0.8000	728.19
298.15	0.8500	725.76
298.15	0.9000	723.36
298.15	0.9500	720.98
298.15	1.0000	718.7
308.15	0.0000	776.49
308.15	0.0500	771.13
308.15	0.1000	765.84
308.15	0.1500	760.98
308.15	0.2000	756.58
308.15	0.2500	752.16
308.15	0.3000	748.12
308.15	0.3500	744.32
308.15	0.4000	740.76
308.15	0.4500	737.5
308.15	0.5000	734.3
308.15	0.5500	731.25
308.15	0.6000	728.37
308.15	0.6500	725.59
308.15	0.7000	722.86
308.15	0.7499	720.23
308.15	0.8000	717.79
308.15	0.8500	715.31
308.15	0.9000	712.89
308.15	0.9500	710.53
308.15	1.0000	708.12

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	781.99
0.0495	776.55
0.0994	771.45
0.2002	762.41
0.2997	754.04
0.4003	746.63
0.5012	740.01
0.6012	734.1
0.7018	728.75
0.8040	723.6
0.8996	718.96
0.9505	716.37
1.0000	713.78

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0440	348.29
0.0890	345.76
0.1430	343.73
0.1930	342.15
0.2400	341.00
0.2870	340.08
0.3380	339.34
0.3890	338.80
0.4400	338.34
0.4890	337.97
0.5370	337.67
0.5980	337.47
0.6490	337.35
0.7050	337.31
0.7570	337.37
0.8090	337.58
0.8590	337.97
0.9070	338.73
0.9540	339.92

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0440	348.29
0.0890	345.76
0.1430	343.73
0.1930	342.15
0.2400	341.00
0.2870	340.08
0.3380	339.34
0.3890	338.80
0.4400	338.34
0.4890	337.97
0.5370	337.67
0.5980	337.47
0.6490	337.35
0.7050	337.31
0.7570	337.37
0.8090	337.58
0.8590	337.97
0.9070	338.73
0.9540	339.92

Sources

• Vapor liquid equilibria for binary and ternary mixtures of diisopropyl ether, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
• Volumetric properties of binary and ternary mixtures of diisopropyl ether, a,a,a-trifluorotoluene, 2,2,2-trifluoroethanol, and ethanol at a temperature 298.15 K and pressure 101 kPa
• Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
• Densities and Viscosities for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and Methylcyclohexane
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
• Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Molar Volumes, Refractive Indices, and Excess Molar Enthalpies at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane