Mixture of 2-Propanol, 2-methyl- + 1,4-Dioxane

Excel

2-Propanol, 2-methyl-

Name
2-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2,3)5/h5H,1-3H3
InChI Key
DKGAVHZHDRPRBM-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)(C)O
Mol. Weight (g/mol)
74.12
CAS
75-65-0

1,4-Dioxane

Name
1,4-Dioxane
InChI
InChI=1S/C4H8O2/c1-2-6-4-3-5-1/h1-4H2
InChI Key
RYHBNJHYFVUHQT-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
C1COCCO1
Mol. Weight (g/mol)
88.11
CAS
123-91-1
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

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

Mole fraction of 1,4-Dioxane (2) [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Pressure, kPa - Gas Mole fraction of 1,4-Dioxane (2) - Gas
0.1256 101.30 0.0890
0.1296 40.00 0.0972
0.2289 101.30 0.1556
0.2298 40.00 0.1765
0.3127 101.30 0.2168
0.3135 40.00 0.2524
0.4051 40.00 0.3228
0.4154 101.30 0.2906
0.5515 40.00 0.4464
0.5524 101.30 0.3956
0.5929 40.00 0.4694
0.5949 101.30 0.4354
0.6530 40.00 0.5177
0.6530 101.30 0.4800
0.7296 101.30 0.5613
0.7406 40.00 0.6013
0.7898 101.30 0.6194
0.7926 40.00 0.6493
0.8227 101.30 0.6645
0.8344 40.00 0.6988
0.8824 101.30 0.7414
0.8872 40.00 0.7747
0.9312 40.00 0.8461
0.9413 101.30 0.8318

Mole fraction of 1,4-Dioxane (2) [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Pressure, kPa - Gas Mole fraction of 1,4-Dioxane (2) - Gas
0.1256 101.30 0.0890
0.1296 40.00 0.0972
0.2289 101.30 0.1556
0.2298 40.00 0.1765
0.3127 101.30 0.2168
0.3135 40.00 0.2524
0.4051 40.00 0.3228
0.4154 101.30 0.2906
0.5515 40.00 0.4464
0.5524 101.30 0.3956
0.5929 40.00 0.4694
0.5949 101.30 0.4354
0.6530 40.00 0.5177
0.6530 101.30 0.4800
0.7296 101.30 0.5613
0.7406 40.00 0.6013
0.7898 101.30 0.6194
0.7926 40.00 0.6493
0.8227 101.30 0.6645
0.8344 40.00 0.6988
0.8824 101.30 0.7414
0.8872 40.00 0.7747
0.9312 40.00 0.8461
0.9413 101.30 0.8318

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mass fraction of 2-Propanol, 2-methyl- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
323.15 0.0000 15.93
323.15 0.0482 17.47
323.15 0.1079 19.20
323.15 0.1534 20.00
323.15 0.2065 20.94
323.15 0.2518 21.60
323.15 0.3126 22.67
323.15 0.3672 23.07
323.15 0.4097 23.60
323.15 0.4611 24.00
323.15 0.5146 24.40
323.15 0.5683 24.53
323.15 0.6224 24.67
323.15 0.6795 24.80
323.15 0.7202 24.93
323.15 0.7728 25.07
323.15 0.8266 25.07
323.15 0.8747 24.93
323.15 0.9231 24.67
323.15 0.9731 24.53
323.15 1.0000 24.40
333.15 0.0000 24.00
333.15 0.0482 26.00
333.15 0.1079 28.00
333.15 0.1534 29.60
333.15 0.2065 30.80
333.15 0.2518 31.73
333.15 0.3126 33.20
333.15 0.3672 34.40
333.15 0.4097 34.93
333.15 0.4611 36.00
333.15 0.5146 36.40
333.15 0.5683 37.06
333.15 0.6224 37.86
333.15 0.6795 38.66
333.15 0.7202 38.93
333.15 0.7728 39.20
333.15 0.8266 39.33
333.15 0.8747 39.46
333.15 0.9231 39.20
333.15 0.9731 39.20
333.15 1.0000 39.06
343.15 0.0000 35.20
343.15 0.0482 37.60
343.15 0.1079 39.73
343.15 0.1534 41.86
343.15 0.2065 44.00
343.15 0.2518 45.86
343.15 0.3126 48.00
343.15 0.3672 49.86
343.15 0.4097 51.33
343.15 0.4611 53.33
343.15 0.5146 54.66
343.15 0.5683 56.26
343.15 0.6224 57.60
343.15 0.6795 58.93
343.15 0.7202 59.60
343.15 0.7728 60.26
343.15 0.8266 61.20
343.15 0.8747 61.33
343.15 0.9231 61.60
343.15 0.9731 61.33
343.15 1.0000 60.93
353.15 0.0000 50.53
353.15 0.0482 53.46
353.15 0.1079 56.93
353.15 0.1534 59.46
353.15 0.2065 62.53
353.15 0.2518 65.33
353.15 0.3126 69.06
353.15 0.3672 72.13
353.15 0.4097 74.53
353.15 0.4611 77.59
353.15 0.5146 80.66
353.15 0.5683 83.19
353.15 0.6224 85.46
353.15 0.6795 87.72
353.15 0.7202 89.12
353.15 0.7728 90.66
353.15 0.8266 91.73
353.15 0.8747 92.53
353.15 0.9231 93.06
353.15 0.9731 92.93
353.15 1.0000 92.26

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mass fraction of 2-Propanol, 2-methyl- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
323.15 0.0000 15.93
323.15 0.0482 17.47
323.15 0.1079 19.20
323.15 0.1534 20.00
323.15 0.2065 20.94
323.15 0.2518 21.60
323.15 0.3126 22.67
323.15 0.3672 23.07
323.15 0.4097 23.60
323.15 0.4611 24.00
323.15 0.5146 24.40
323.15 0.5683 24.53
323.15 0.6224 24.67
323.15 0.6795 24.80
323.15 0.7202 24.93
323.15 0.7728 25.07
323.15 0.8266 25.07
323.15 0.8747 24.93
323.15 0.9231 24.67
323.15 0.9731 24.53
323.15 1.0000 24.40
333.15 0.0000 24.00
333.15 0.0482 26.00
333.15 0.1079 28.00
333.15 0.1534 29.60
333.15 0.2065 30.80
333.15 0.2518 31.73
333.15 0.3126 33.20
333.15 0.3672 34.40
333.15 0.4097 34.93
333.15 0.4611 36.00
333.15 0.5146 36.40
333.15 0.5683 37.06
333.15 0.6224 37.86
333.15 0.6795 38.66
333.15 0.7202 38.93
333.15 0.7728 39.20
333.15 0.8266 39.33
333.15 0.8747 39.46
333.15 0.9231 39.20
333.15 0.9731 39.20
333.15 1.0000 39.06
343.15 0.0000 35.20
343.15 0.0482 37.60
343.15 0.1079 39.73
343.15 0.1534 41.86
343.15 0.2065 44.00
343.15 0.2518 45.86
343.15 0.3126 48.00
343.15 0.3672 49.86
343.15 0.4097 51.33
343.15 0.4611 53.33
343.15 0.5146 54.66
343.15 0.5683 56.26
343.15 0.6224 57.60
343.15 0.6795 58.93
343.15 0.7202 59.60
343.15 0.7728 60.26
343.15 0.8266 61.20
343.15 0.8747 61.33
343.15 0.9231 61.60
343.15 0.9731 61.33
343.15 1.0000 60.93
353.15 0.0000 50.53
353.15 0.0482 53.46
353.15 0.1079 56.93
353.15 0.1534 59.46
353.15 0.2065 62.53
353.15 0.2518 65.33
353.15 0.3126 69.06
353.15 0.3672 72.13
353.15 0.4097 74.53
353.15 0.4611 77.59
353.15 0.5146 80.66
353.15 0.5683 83.19
353.15 0.6224 85.46
353.15 0.6795 87.72
353.15 0.7202 89.12
353.15 0.7728 90.66
353.15 0.8266 91.73
353.15 0.8747 92.53
353.15 0.9231 93.06
353.15 0.9731 92.93
353.15 1.0000 92.26

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0502 791.11
298.15 0.0802 797.29
298.15 0.2164 826.41
298.15 0.2915 843.19
298.15 0.3944 867.16
298.15 0.4960 891.65
298.15 0.5929 915.92
298.15 0.6814 938.8
298.15 0.8029 971.23
298.15 0.8893 995.28
298.15 0.9287 1006.7
313.15 0.0525 776.05
313.15 0.0886 783.75
313.15 0.2051 808.89
313.15 0.2870 827.2
313.15 0.3926 851.46
313.15 0.4938 875.49
313.15 0.5920 899.61
313.15 0.6904 924.78
313.15 0.7994 953.91
313.15 0.8871 978.21
313.15 0.9421 993.91

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0502 791.11
298.15 0.0802 797.29
298.15 0.2164 826.41
298.15 0.2915 843.19
298.15 0.3944 867.16
298.15 0.4960 891.65
298.15 0.5929 915.92
298.15 0.6814 938.8
298.15 0.8029 971.23
298.15 0.8893 995.28
298.15 0.9287 1006.7
313.15 0.0525 776.05
313.15 0.0886 783.75
313.15 0.2051 808.89
313.15 0.2870 827.2
313.15 0.3926 851.46
313.15 0.4938 875.49
313.15 0.5920 899.61
313.15 0.6904 924.78
313.15 0.7994 953.91
313.15 0.8871 978.21
313.15 0.9421 993.91

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0502 1133.5
298.15 0.0802 1139.5
298.15 0.2164 1166.2
298.15 0.2915 1180.4
298.15 0.3944 1201.4
298.15 0.4960 1222.4
298.15 0.5929 1243.8
298.15 0.6814 1264.1
298.15 0.8029 1293.2
298.15 0.8893 1315.3
298.15 0.9287 1325.5
313.15 0.0525 1069.8
313.15 0.0886 1078.1
313.15 0.2051 1102.3
313.15 0.2870 1118.9
313.15 0.3926 1139.9
313.15 0.4938 1160.8
313.15 0.5920 1181.6
313.15 0.6904 1202.7
313.15 0.7994 1227.9
313.15 0.8871 1250.3
313.15 0.9421 1264.2

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0502 1133.5
298.15 0.0802 1139.5
298.15 0.2164 1166.2
298.15 0.2915 1180.4
298.15 0.3944 1201.4
298.15 0.4960 1222.4
298.15 0.5929 1243.8
298.15 0.6814 1264.1
298.15 0.8029 1293.2
298.15 0.8893 1315.3
298.15 0.9287 1325.5
313.15 0.0525 1069.8
313.15 0.0886 1078.1
313.15 0.2051 1102.3
313.15 0.2870 1118.9
313.15 0.3926 1139.9
313.15 0.4938 1160.8
313.15 0.5920 1181.6
313.15 0.6904 1202.7
313.15 0.7994 1227.9
313.15 0.8871 1250.3
313.15 0.9421 1264.2

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
26.66 0.0000 335.85
26.66 0.0482 333.95
26.66 0.1079 331.65
26.66 0.1534 330.35
26.66 0.2065 329.55
26.66 0.2518 328.65
26.66 0.3126 327.85
26.66 0.3672 327.05
26.66 0.4097 326.25
26.66 0.4611 325.75
26.66 0.5146 325.45
26.66 0.5683 325.05
26.66 0.6224 324.85
26.66 0.6795 324.75
26.66 0.7202 324.65
26.66 0.7728 324.55
26.66 0.8266 324.45
26.66 0.8747 324.45
26.66 0.9231 324.75
26.66 0.9731 324.95
26.66 1.0000 325.05
53.33 0.0000 354.65
53.33 0.0482 352.75
53.33 0.1079 350.65
53.33 0.1534 349.25
53.33 0.2065 347.85
53.33 0.2518 346.75
53.33 0.3126 345.45
53.33 0.3672 344.45
53.33 0.4097 343.75
53.33 0.4611 343.05
53.33 0.5146 342.35
53.33 0.5683 341.65
53.33 0.6224 341.15
53.33 0.6795 340.75
53.33 0.7202 340.35
53.33 0.7728 340.25
53.33 0.8266 339.85
53.33 0.8747 339.75
53.33 0.9231 339.65
53.33 0.9731 339.95
53.33 1.0000 340.05
79.99 0.0000 366.95
79.99 0.0482 364.85
79.99 0.1079 362.75
79.99 0.1534 361.35
79.99 0.2065 359.85
79.99 0.2518 358.65
79.99 0.3126 357.25
79.99 0.3672 356.15
79.99 0.4097 355.45
79.99 0.4611 354.55
79.99 0.5146 353.65
79.99 0.5683 352.95
79.99 0.6224 352.25
79.99 0.6795 351.65
79.99 0.7202 351.25
79.99 0.7728 350.85
79.99 0.8266 350.35
79.99 0.8747 350.15
79.99 0.9231 349.75
79.99 0.9731 349.65
79.99 1.0000 349.75
101.33 0.0000 374.45
101.33 0.0482 372.55
101.33 0.1079 370.45
101.33 0.1534 368.95
101.33 0.2065 367.35
101.33 0.2518 366.15
101.33 0.3126 364.55
101.33 0.3672 363.15
101.33 0.4097 362.35
101.33 0.4611 361.05
101.33 0.5146 360.15
101.33 0.5683 359.15
101.33 0.6224 358.35
101.33 0.6795 357.45
101.33 0.7202 356.95
101.33 0.7728 356.35
101.33 0.8266 355.85
101.33 0.8747 355.55
101.33 0.9231 355.35
101.33 0.9731 355.25
101.33 1.0000 355.55

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 101.30 355.50
0.1256 101.30 356.28
0.1296 40.00 334.21
0.2289 101.30 357.13
0.2298 40.00 334.90
0.3127 101.30 358.01
0.3135 40.00 335.07
0.4051 40.00 335.74
0.4154 101.30 359.38
0.5515 40.00 337.05
0.5524 101.30 360.82
0.5929 40.00 337.83
0.5949 101.30 361.78
0.6530 40.00 338.55
0.6530 101.30 362.57
0.7296 101.30 363.71
0.7406 40.00 339.63
0.7898 101.30 365.03
0.7926 40.00 340.61
0.8227 101.30 365.83
0.8344 40.00 341.41
0.8824 101.30 368.12
0.8872 40.00 341.99
0.9312 40.00 343.98
0.9413 101.30 370.84
1.0000 101.30 374.56

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
26.66 0.0000 335.85
26.66 0.0482 333.95
26.66 0.1079 331.65
26.66 0.1534 330.35
26.66 0.2065 329.55
26.66 0.2518 328.65
26.66 0.3126 327.85
26.66 0.3672 327.05
26.66 0.4097 326.25
26.66 0.4611 325.75
26.66 0.5146 325.45
26.66 0.5683 325.05
26.66 0.6224 324.85
26.66 0.6795 324.75
26.66 0.7202 324.65
26.66 0.7728 324.55
26.66 0.8266 324.45
26.66 0.8747 324.45
26.66 0.9231 324.75
26.66 0.9731 324.95
26.66 1.0000 325.05
53.33 0.0000 354.65
53.33 0.0482 352.75
53.33 0.1079 350.65
53.33 0.1534 349.25
53.33 0.2065 347.85
53.33 0.2518 346.75
53.33 0.3126 345.45
53.33 0.3672 344.45
53.33 0.4097 343.75
53.33 0.4611 343.05
53.33 0.5146 342.35
53.33 0.5683 341.65
53.33 0.6224 341.15
53.33 0.6795 340.75
53.33 0.7202 340.35
53.33 0.7728 340.25
53.33 0.8266 339.85
53.33 0.8747 339.75
53.33 0.9231 339.65
53.33 0.9731 339.95
53.33 1.0000 340.05
79.99 0.0000 366.95
79.99 0.0482 364.85
79.99 0.1079 362.75
79.99 0.1534 361.35
79.99 0.2065 359.85
79.99 0.2518 358.65
79.99 0.3126 357.25
79.99 0.3672 356.15
79.99 0.4097 355.45
79.99 0.4611 354.55
79.99 0.5146 353.65
79.99 0.5683 352.95
79.99 0.6224 352.25
79.99 0.6795 351.65
79.99 0.7202 351.25
79.99 0.7728 350.85
79.99 0.8266 350.35
79.99 0.8747 350.15
79.99 0.9231 349.75
79.99 0.9731 349.65
79.99 1.0000 349.75
101.33 0.0000 374.45
101.33 0.0482 372.55
101.33 0.1079 370.45
101.33 0.1534 368.95
101.33 0.2065 367.35
101.33 0.2518 366.15
101.33 0.3126 364.55
101.33 0.3672 363.15
101.33 0.4097 362.35
101.33 0.4611 361.05
101.33 0.5146 360.15
101.33 0.5683 359.15
101.33 0.6224 358.35
101.33 0.6795 357.45
101.33 0.7202 356.95
101.33 0.7728 356.35
101.33 0.8266 355.85
101.33 0.8747 355.55
101.33 0.9231 355.35
101.33 0.9731 355.25
101.33 1.0000 355.55

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 101.30 355.50
0.1256 101.30 356.28
0.1296 40.00 334.21
0.2289 101.30 357.13
0.2298 40.00 334.90
0.3127 101.30 358.01
0.3135 40.00 335.07
0.4051 40.00 335.74
0.4154 101.30 359.38
0.5515 40.00 337.05
0.5524 101.30 360.82
0.5929 40.00 337.83
0.5949 101.30 361.78
0.6530 40.00 338.55
0.6530 101.30 362.57
0.7296 101.30 363.71
0.7406 40.00 339.63
0.7898 101.30 365.03
0.7926 40.00 340.61
0.8227 101.30 365.83
0.8344 40.00 341.41
0.8824 101.30 368.12
0.8872 40.00 341.99
0.9312 40.00 343.98
0.9413 101.30 370.84
1.0000 101.30 374.56

Sources