Mixture of 2-Propanol, 2-methyl- + 1-Propene, 2-methyl-

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-Propene, 2-methyl-

Name
1-Propene, 2-methyl-
InChI
InChI=1S/C4H8/c1-4(2)3/h1H2,2-3H3
InChI Key
VQTUBCCKSQIDNK-UHFFFAOYSA-N
Formula
C4H8
SMILES
C=C(C)C
Mol. Weight (g/mol)
56.11
CAS
115-11-7
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. Activity coefficient (2)
  2. Henry's Law constant (mole fraction scale), kPa (2)
  3. Pvap - Vapor or sublimation pressure, kPa (4)

Activity coefficient of 1-Propene, 2-methyl- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1-Propene, 2-methyl- (2) - Liquid
300.00 3.06
310.00 2.92
320.00 2.77
330.00 2.63

Activity coefficient of 1-Propene, 2-methyl- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of 1-Propene, 2-methyl- (2) - Liquid
300.00 3.06
310.00 2.92
320.00 2.77
330.00 2.63

Henry's Law constant (mole fraction scale), kPa of 1-Propene, 2-methyl- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of 1-Propene, 2-methyl- (2) - Liquid
300.00 894.0
310.00 1120.0
320.00 1370.0
330.00 1630.0

Henry's Law constant (mole fraction scale), kPa of 1-Propene, 2-methyl- (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of 1-Propene, 2-methyl- (2) - Liquid
300.00 894.0
310.00 1120.0
320.00 1370.0
330.00 1630.0

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propene, 2-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
313.12 0.2947 250.96
313.12 0.3478 278.36
313.12 0.3998 302.46
313.12 0.4519 324.36
313.12 0.4729 332.56
313.12 0.4902 339.16
313.12 0.5038 344.26
313.12 0.5472 358.46
313.12 0.9885 465.15
313.12 1.0000 469.75
313.13 0.0000 13.77
313.13 0.0132 28.87
313.13 0.0371 55.07
313.13 0.0866 103.47
313.13 0.1368 146.57
313.13 0.1898 186.16
313.13 0.2423 220.56
313.13 0.4983 342.66
313.13 0.5966 373.25
313.13 0.6464 386.95
313.13 0.6964 399.75
313.13 0.7473 411.75
313.13 0.7976 422.85
313.13 0.8484 433.45
313.13 0.8987 443.65
313.13 0.9483 454.15
322.75 0.5516 454.35
322.75 0.6000 473.55
322.75 0.6485 491.45
322.76 0.7508 525.35
322.76 0.7999 540.05
322.76 0.8508 554.54
322.76 0.9008 568.84
322.77 0.0286 62.57
322.77 0.3396 345.96
322.77 0.3916 376.85
322.77 0.4419 403.95
322.77 0.4933 429.05
322.77 0.5028 433.25
322.77 0.5350 447.85
322.77 0.6974 508.15
322.77 0.9517 584.64
322.78 0.0000 23.07
322.78 0.0390 76.17
322.78 0.2423 278.06
322.78 0.2915 314.16
322.78 0.9917 600.74
322.79 0.0887 134.87
322.79 0.1389 187.56
322.79 0.1871 232.56
322.79 1.0000 605.14

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propene, 2-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
364.50 0.0491 267.10
364.50 0.0970 379.10
364.50 0.1923 575.20
364.50 0.3939 900.10
364.51 0.0304 220.90
364.51 0.2415 664.60
364.51 0.3423 826.70
364.51 0.9690 1509.00
364.51 0.9903 1534.20
364.52 0.0000 142.70
364.52 0.0132 177.20
364.52 0.1455 483.10
364.52 0.2916 748.60
364.52 0.4462 969.30
364.52 0.4976 1031.90
364.52 0.4991 1035.60
364.52 0.5472 1090.30
364.52 0.5952 1141.80
364.52 0.6442 1192.10
364.52 0.6933 1239.90
364.52 0.7429 1286.70
364.52 0.8440 1380.50
364.52 0.8953 1430.20
364.52 0.9473 1484.20
364.52 0.9779 1519.50
364.52 1.0000 1546.30
364.53 0.7932 1333.40

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propene, 2-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
313.12 0.2947 250.96
313.12 0.3478 278.36
313.12 0.3998 302.46
313.12 0.4519 324.36
313.12 0.4729 332.56
313.12 0.4902 339.16
313.12 0.5038 344.26
313.12 0.5472 358.46
313.12 0.9885 465.15
313.12 1.0000 469.75
313.13 0.0000 13.77
313.13 0.0132 28.87
313.13 0.0371 55.07
313.13 0.0866 103.47
313.13 0.1368 146.57
313.13 0.1898 186.16
313.13 0.2423 220.56
313.13 0.4983 342.66
313.13 0.5966 373.25
313.13 0.6464 386.95
313.13 0.6964 399.75
313.13 0.7473 411.75
313.13 0.7976 422.85
313.13 0.8484 433.45
313.13 0.8987 443.65
313.13 0.9483 454.15
322.75 0.5516 454.35
322.75 0.6000 473.55
322.75 0.6485 491.45
322.76 0.7508 525.35
322.76 0.7999 540.05
322.76 0.8508 554.54
322.76 0.9008 568.84
322.77 0.0286 62.57
322.77 0.3396 345.96
322.77 0.3916 376.85
322.77 0.4419 403.95
322.77 0.4933 429.05
322.77 0.5028 433.25
322.77 0.5350 447.85
322.77 0.6974 508.15
322.77 0.9517 584.64
322.78 0.0000 23.07
322.78 0.0390 76.17
322.78 0.2423 278.06
322.78 0.2915 314.16
322.78 0.9917 600.74
322.79 0.0887 134.87
322.79 0.1389 187.56
322.79 0.1871 232.56
322.79 1.0000 605.14

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propene, 2-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
364.50 0.0491 267.10
364.50 0.0970 379.10
364.50 0.1923 575.20
364.50 0.3939 900.10
364.51 0.0304 220.90
364.51 0.2415 664.60
364.51 0.3423 826.70
364.51 0.9690 1509.00
364.51 0.9903 1534.20
364.52 0.0000 142.70
364.52 0.0132 177.20
364.52 0.1455 483.10
364.52 0.2916 748.60
364.52 0.4462 969.30
364.52 0.4976 1031.90
364.52 0.4991 1035.60
364.52 0.5472 1090.30
364.52 0.5952 1141.80
364.52 0.6442 1192.10
364.52 0.6933 1239.90
364.52 0.7429 1286.70
364.52 0.8440 1380.50
364.52 0.8953 1430.20
364.52 0.9473 1484.20
364.52 0.9779 1519.50
364.52 1.0000 1546.30
364.53 0.7932 1333.40

Sources