Mixture of 1-Propanol + Butane

Excel

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

Butane

Name
Butane
InChI
InChI=1S/C4H10/c1-3-4-2/h3-4H2,1-2H3
InChI Key
IJDNQMDRQITEOD-UHFFFAOYSA-N
Formula
C4H10
SMILES
CCCC
Mol. Weight (g/mol)
58.12
CAS
106-97-8
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Datasets

  1. Activity coefficient (2)
  2. Henry's Law constant (mole fraction scale), kPa (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)

Activity coefficient of Butane (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of Butane (2) - Liquid
260.05 5.17
280.05 5.06
299.99 5.03
320.05 4.88

Activity coefficient of Butane (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Activity coefficient of Butane (2) - Liquid
260.05 5.17
280.05 5.06
299.99 5.03
320.05 4.88

Henry's Law constant (mole fraction scale), kPa of Butane (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of Butane (2) - Liquid
260.05 309.0
280.05 642.0
299.99 1194.0
320.05 1970.0
340.04 2985.0

Henry's Law constant (mole fraction scale), kPa of Butane (2) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid Henry's Law constant (mole fraction scale), kPa of Butane (2) - Liquid
260.05 309.0
280.05 642.0
299.99 1194.0
320.05 1970.0
340.04 2985.0

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
330.16 0.0000 17.57
330.16 0.0123 47.17
330.16 0.0304 87.87
330.16 0.0490 126.77
330.16 0.8974 574.44
330.16 0.9671 585.54
330.16 0.9876 589.64
330.16 1.0000 592.44
330.17 0.0967 212.96
330.17 0.1440 282.16
330.17 0.1931 340.06
330.17 0.7961 560.34
330.17 0.8462 567.24
330.17 0.9475 582.14
330.18 0.2434 386.95
330.18 0.3439 453.05
330.18 0.3951 476.25
330.18 0.4975 509.35
330.18 0.4990 509.65
330.18 0.5482 520.95
330.18 0.5977 530.45
330.18 0.6469 538.85
330.18 0.6966 546.34
330.18 0.7469 553.54
330.19 0.2937 423.85
330.19 0.4463 494.65

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
330.16 0.0000 17.57
330.16 0.0123 47.17
330.16 0.0304 87.87
330.16 0.0490 126.77
330.16 0.8974 574.44
330.16 0.9671 585.54
330.16 0.9876 589.64
330.16 1.0000 592.44
330.17 0.0967 212.96
330.17 0.1440 282.16
330.17 0.1931 340.06
330.17 0.7961 560.34
330.17 0.8462 567.24
330.17 0.9475 582.14
330.18 0.2434 386.95
330.18 0.3439 453.05
330.18 0.3951 476.25
330.18 0.4975 509.35
330.18 0.4990 509.65
330.18 0.5482 520.95
330.18 0.5977 530.45
330.18 0.6469 538.85
330.18 0.6966 546.34
330.18 0.7469 553.54
330.19 0.2937 423.85
330.19 0.4463 494.65

Sources