Mixture of 1-Propanol + Diisopropyl ether

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1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3
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Datasets

  1. Mole fraction (6)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. n0 - Refractive index (Na D-line) (2)
  4. ρl - Mass density, kg/m3 (6)
  5. csound,fluid - Speed of Sound, m/s (2)
  6. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0252 0.2009
0.0494 0.3211
0.0730 0.4110
0.0968 0.4693
0.1454 0.5734
0.2022 0.6453
0.2707 0.7080
0.3365 0.7435
0.4007 0.7706
0.4629 0.7923
0.5241 0.8087
0.5834 0.8267
0.6420 0.8370
0.6967 0.8506
0.7526 0.8669
0.8062 0.8891
0.8576 0.9126
0.9003 0.9349
0.9354 0.9539
0.9504 0.9634
0.9674 0.9741
0.9832 0.9858

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0199 0.2671
0.0399 0.4090
0.0601 0.5061
0.0799 0.5783
0.1192 0.6847
0.1694 0.7346
0.2294 0.7822
0.2891 0.8133
0.3495 0.8343
0.4090 0.8524
0.4708 0.8659
0.5296 0.8774
0.5902 0.8890
0.6505 0.8974
0.7101 0.9093
0.7685 0.9209
0.8300 0.9372
0.8803 0.9521
0.9179 0.9637
0.9397 0.9709
0.9581 0.9785
0.9804 0.9885

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0545 0.2190
0.0785 0.2985
0.1020 0.3524
0.1330 0.4388
0.1430 0.4769
0.1738 0.5173
0.2038 0.5565
0.2413 0.5983
0.2644 0.6181
0.3055 0.6550
0.3504 0.6846
0.3967 0.7172
0.4490 0.7459
0.5050 0.7692
0.5677 0.7913
0.6673 0.8318
0.7483 0.8560
0.8331 0.8904
0.9177 0.9361

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0252 0.2009
0.0494 0.3211
0.0730 0.4110
0.0968 0.4693
0.1454 0.5734
0.2022 0.6453
0.2707 0.7080
0.3365 0.7435
0.4007 0.7706
0.4629 0.7923
0.5241 0.8087
0.5834 0.8267
0.6420 0.8370
0.6967 0.8506
0.7526 0.8669
0.8062 0.8891
0.8576 0.9126
0.9003 0.9349
0.9354 0.9539
0.9504 0.9634
0.9674 0.9741
0.9832 0.9858

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0199 0.2671
0.0399 0.4090
0.0601 0.5061
0.0799 0.5783
0.1192 0.6847
0.1694 0.7346
0.2294 0.7822
0.2891 0.8133
0.3495 0.8343
0.4090 0.8524
0.4708 0.8659
0.5296 0.8774
0.5902 0.8890
0.6505 0.8974
0.7101 0.9093
0.7685 0.9209
0.8300 0.9372
0.8803 0.9521
0.9179 0.9637
0.9397 0.9709
0.9581 0.9785
0.9804 0.9885

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0545 0.2190
0.0785 0.2985
0.1020 0.3524
0.1330 0.4388
0.1430 0.4769
0.1738 0.5173
0.2038 0.5565
0.2413 0.5983
0.2644 0.6181
0.3055 0.6550
0.3504 0.6846
0.3967 0.7172
0.4490 0.7459
0.5050 0.7692
0.5677 0.7913
0.6673 0.8318
0.7483 0.8560
0.8331 0.8904
0.9177 0.9361

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 7.00
0.0510 11.28
0.1015 14.92
0.1495 17.86
0.1985 20.39
0.2479 22.54
0.2982 24.41
0.2982 24.39
0.3481 25.99
0.3983 27.34
0.4495 28.55
0.4977 29.54
0.4994 29.59
0.5482 30.49
0.5992 31.37
0.6501 32.16
0.7006 32.96
0.7010 32.93
0.7524 33.69
0.8038 34.43
0.8538 35.14
0.9058 35.86
0.9555 36.54
1.0000 37.10

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 7.00
0.0510 11.28
0.1015 14.92
0.1495 17.86
0.1985 20.39
0.2479 22.54
0.2982 24.41
0.2982 24.39
0.3481 25.99
0.3983 27.34
0.4495 28.55
0.4977 29.54
0.4994 29.59
0.5482 30.49
0.5992 31.37
0.6501 32.16
0.7006 32.96
0.7010 32.93
0.7524 33.69
0.8038 34.43
0.8538 35.14
0.9058 35.86
0.9555 36.54
1.0000 37.10

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Refractive index (Na D-line) - Liquid
0.0000 1.3831
0.0602 1.3824
0.1201 1.3815
0.1569 1.381
0.2127 1.3802
0.2472 1.3796
0.2939 1.3787
0.3513 1.3777
0.3835 1.3772
0.4282 1.3764
0.4934 1.3752
0.5267 1.3745
0.5772 1.3736
0.6167 1.3728
0.7267 1.3707
0.7533 1.3702
0.7824 1.3696
0.8325 1.3687
0.8608 1.3681
0.9496 1.3664
1.0000 1.3652

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Refractive index (Na D-line) - Liquid
0.0000 1.3831
0.0602 1.3824
0.1201 1.3815
0.1569 1.381
0.2127 1.3802
0.2472 1.3796
0.2939 1.3787
0.3513 1.3777
0.3835 1.3772
0.4282 1.3764
0.4934 1.3752
0.5267 1.3745
0.5772 1.3736
0.6167 1.3728
0.7267 1.3707
0.7533 1.3702
0.7824 1.3696
0.8325 1.3687
0.8608 1.3681
0.9496 1.3664
1.0000 1.3652

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0508 794.63
0.0999 789.64
0.2000 779.84
0.2998 770.67
0.3993 762.07
0.4999 754.19
0.6006 746.71
0.7007 739.41
0.8001 732.66
0.9015 725.59
0.9514 722.22

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 796.55
0.0504 790.59
0.0991 785.96
0.2001 775.66
0.2994 766.52
0.4000 757.67
0.5018 749.3
0.6006 741.73
0.6995 734.54
0.7994 727.46
0.8981 720.72
0.9498 717.2
1.0000 713.51

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 799.64
0.0602 793.89
0.1201 787.09
0.1569 783.68
0.2127 778.46
0.2472 775.39
0.2939 771.16
0.3513 766.09
0.3835 763.45
0.4282 759.51
0.4934 754.16
0.5267 751.59
0.5772 747.7
0.6167 744.73
0.7267 736.98
0.7533 735.13
0.7824 733.09
0.8325 729.72
0.8608 727.8
0.9496 721.77
1.0000 718.32

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0508 794.63
0.0999 789.64
0.2000 779.84
0.2998 770.67
0.3993 762.07
0.4999 754.19
0.6006 746.71
0.7007 739.41
0.8001 732.66
0.9015 725.59
0.9514 722.22

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 796.55
0.0504 790.59
0.0991 785.96
0.2001 775.66
0.2994 766.52
0.4000 757.67
0.5018 749.3
0.6006 741.73
0.6995 734.54
0.7994 727.46
0.8981 720.72
0.9498 717.2
1.0000 713.51

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 799.64
0.0602 793.89
0.1201 787.09
0.1569 783.68
0.2127 778.46
0.2472 775.39
0.2939 771.16
0.3513 766.09
0.3835 763.45
0.4282 759.51
0.4934 754.16
0.5267 751.59
0.5772 747.7
0.6167 744.73
0.7267 736.98
0.7533 735.13
0.7824 733.09
0.8325 729.72
0.8608 727.8
0.9496 721.77
1.0000 718.32

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Speed of sound, m/s - Liquid
0.0000 1207.0
0.0602 1189.0
0.1201 1168.0
0.1569 1162.0
0.2127 1147.0
0.2472 1137.0
0.2939 1128.0
0.3513 1113.0
0.3835 1107.0
0.4282 1097.0
0.4934 1083.0
0.5267 1077.0
0.5772 1067.0
0.6167 1060.0
0.7267 1042.0
0.7533 1037.0
0.7824 1033.0
0.8325 1025.0
0.8608 1021.0
0.9496 1006.0
1.0000 997.0

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Speed of sound, m/s - Liquid
0.0000 1207.0
0.0602 1189.0
0.1201 1168.0
0.1569 1162.0
0.2127 1147.0
0.2472 1137.0
0.2939 1128.0
0.3513 1113.0
0.3835 1107.0
0.4282 1097.0
0.4934 1083.0
0.5267 1077.0
0.5772 1067.0
0.6167 1060.0
0.7267 1042.0
0.7533 1037.0
0.7824 1033.0
0.8325 1025.0
0.8608 1021.0
0.9496 1006.0
1.0000 997.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0545 364.78
0.0785 362.78
0.1020 360.96
0.1330 358.82
0.1430 358.09
0.1738 356.27
0.2038 354.80
0.2413 353.19
0.2644 352.44
0.3055 350.98
0.3504 349.72
0.3967 348.53
0.4490 347.46
0.5050 346.50
0.5677 345.52
0.6673 344.20
0.7483 343.27
0.8331 342.48
0.9177 341.86

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Diisopropyl ether (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0545 364.78
0.0785 362.78
0.1020 360.96
0.1330 358.82
0.1430 358.09
0.1738 356.27
0.2038 354.80
0.2413 353.19
0.2644 352.44
0.3055 350.98
0.3504 349.72
0.3967 348.53
0.4490 347.46
0.5050 346.50
0.5677 345.52
0.6673 344.20
0.7483 343.27
0.8331 342.48
0.9177 341.86

Sources