- Name
- 1-Butene
- InChI
- InChI=1S/C4H8/c1-3-4-2/h3H,1,4H2,2H3
- InChI Key
- VXNZUUAINFGPBY-UHFFFAOYSA-N
- Formula
- C4H8
- SMILES
- C=CCC
- Mol. Weight (g/mol)
- 56.11
- CAS
- 106-98-9
- Name
- 1-Butanol
- InChI
- InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
- InChI Key
- LRHPLDYGYMQRHN-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CCCCO
- Mol. Weight (g/mol)
- 74.12
- CAS
- 71-36-3
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Datasets
- Activity coefficient (2)
- Henry's Law constant (mole fraction scale), kPa (2)
- Pvap - Vapor or sublimation pressure, kPa (2)
Activity coefficient of 1-Butene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of 1-Butene (1) - Liquid |
|---|---|
| 250.01 | 3.5 |
| 270.00 | 3.4 |
| 290.01 | 3.4 |
| 310.00 | 3.3 |
| 330.00 | 3.2 |
Activity coefficient of 1-Butene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of 1-Butene (1) - Liquid |
|---|---|
| 250.01 | 3.5 |
| 270.00 | 3.4 |
| 290.01 | 3.4 |
| 310.00 | 3.3 |
| 330.00 | 3.2 |
Henry's Law constant (mole fraction scale), kPa of 1-Butene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of 1-Butene (1) - Liquid |
|---|---|
| 250.01 | 168.0 |
| 270.00 | 372.0 |
| 290.01 | 731.0 |
| 310.00 | 1260.0 |
| 330.00 | 1970.0 |
Henry's Law constant (mole fraction scale), kPa of 1-Butene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of 1-Butene (1) - Liquid |
|---|---|
| 250.01 | 168.0 |
| 270.00 | 372.0 |
| 290.01 | 731.0 |
| 310.00 | 1260.0 |
| 330.00 | 1970.0 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butene (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 318.40 | 0.0000 | 3.60 |
| 318.40 | 0.0156 | 27.20 |
| 318.40 | 0.0341 | 53.80 |
| 318.40 | 0.0518 | 78.30 |
| 318.40 | 0.0990 | 138.60 |
| 318.40 | 0.1469 | 192.50 |
| 318.40 | 0.1964 | 241.10 |
| 318.40 | 0.4976 | 416.20 |
| 318.40 | 0.4977 | 416.30 |
| 318.40 | 0.5468 | 431.00 |
| 318.40 | 0.5961 | 443.70 |
| 318.40 | 0.6451 | 454.70 |
| 318.40 | 0.6946 | 464.60 |
| 318.40 | 0.7441 | 473.60 |
| 318.40 | 0.7942 | 482.20 |
| 318.40 | 0.8446 | 490.50 |
| 318.40 | 0.8942 | 498.60 |
| 318.40 | 0.9470 | 508.20 |
| 318.40 | 0.9671 | 512.90 |
| 318.40 | 0.9759 | 515.40 |
| 318.40 | 0.9874 | 519.40 |
| 318.40 | 1.0000 | 525.80 |
| 318.41 | 0.2461 | 283.20 |
| 318.41 | 0.2958 | 319.20 |
| 318.41 | 0.3456 | 349.80 |
| 318.41 | 0.3966 | 376.10 |
| 318.41 | 0.4472 | 398.00 |
| 364.49 | 0.3917 | 943.20 |
| 364.49 | 0.7903 | 1306.10 |
| 364.50 | 0.4439 | 1009.70 |
| 364.50 | 0.5445 | 1116.50 |
| 364.51 | 0.5928 | 1159.80 |
| 364.51 | 0.7399 | 1271.50 |
| 364.51 | 0.8412 | 1342.70 |
| 364.52 | 0.0000 | 36.30 |
| 364.52 | 0.0931 | 333.00 |
| 364.52 | 0.1394 | 458.90 |
| 364.52 | 0.2374 | 684.90 |
| 364.52 | 0.2884 | 782.20 |
| 364.52 | 0.3394 | 867.40 |
| 364.52 | 0.4969 | 1069.50 |
| 364.52 | 0.6413 | 1199.40 |
| 364.52 | 0.6900 | 1236.20 |
| 364.52 | 0.8926 | 1382.50 |
| 364.52 | 0.9447 | 1432.10 |
| 364.52 | 0.9680 | 1460.60 |
| 364.52 | 0.9796 | 1477.30 |
| 364.53 | 0.0124 | 79.00 |
| 364.53 | 0.0299 | 138.60 |
| 364.53 | 0.0473 | 194.00 |
| 364.53 | 0.1883 | 578.30 |
| 364.53 | 0.4960 | 1068.70 |
| 364.53 | 0.9897 | 1492.90 |
| 364.53 | 1.0000 | 1509.40 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butene (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 318.40 | 0.0000 | 3.60 |
| 318.40 | 0.0156 | 27.20 |
| 318.40 | 0.0341 | 53.80 |
| 318.40 | 0.0518 | 78.30 |
| 318.40 | 0.0990 | 138.60 |
| 318.40 | 0.1469 | 192.50 |
| 318.40 | 0.1964 | 241.10 |
| 318.40 | 0.4976 | 416.20 |
| 318.40 | 0.4977 | 416.30 |
| 318.40 | 0.5468 | 431.00 |
| 318.40 | 0.5961 | 443.70 |
| 318.40 | 0.6451 | 454.70 |
| 318.40 | 0.6946 | 464.60 |
| 318.40 | 0.7441 | 473.60 |
| 318.40 | 0.7942 | 482.20 |
| 318.40 | 0.8446 | 490.50 |
| 318.40 | 0.8942 | 498.60 |
| 318.40 | 0.9470 | 508.20 |
| 318.40 | 0.9671 | 512.90 |
| 318.40 | 0.9759 | 515.40 |
| 318.40 | 0.9874 | 519.40 |
| 318.40 | 1.0000 | 525.80 |
| 318.41 | 0.2461 | 283.20 |
| 318.41 | 0.2958 | 319.20 |
| 318.41 | 0.3456 | 349.80 |
| 318.41 | 0.3966 | 376.10 |
| 318.41 | 0.4472 | 398.00 |
| 364.49 | 0.3917 | 943.20 |
| 364.49 | 0.7903 | 1306.10 |
| 364.50 | 0.4439 | 1009.70 |
| 364.50 | 0.5445 | 1116.50 |
| 364.51 | 0.5928 | 1159.80 |
| 364.51 | 0.7399 | 1271.50 |
| 364.51 | 0.8412 | 1342.70 |
| 364.52 | 0.0000 | 36.30 |
| 364.52 | 0.0931 | 333.00 |
| 364.52 | 0.1394 | 458.90 |
| 364.52 | 0.2374 | 684.90 |
| 364.52 | 0.2884 | 782.20 |
| 364.52 | 0.3394 | 867.40 |
| 364.52 | 0.4969 | 1069.50 |
| 364.52 | 0.6413 | 1199.40 |
| 364.52 | 0.6900 | 1236.20 |
| 364.52 | 0.8926 | 1382.50 |
| 364.52 | 0.9447 | 1432.10 |
| 364.52 | 0.9680 | 1460.60 |
| 364.52 | 0.9796 | 1477.30 |
| 364.53 | 0.0124 | 79.00 |
| 364.53 | 0.0299 | 138.60 |
| 364.53 | 0.0473 | 194.00 |
| 364.53 | 0.1883 | 578.30 |
| 364.53 | 0.4960 | 1068.70 |
| 364.53 | 0.9897 | 1492.90 |
| 364.53 | 1.0000 | 1509.40 |
Sources
- Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene and 1,3-Butadiene in 1-Butanol and 2-Butanol at (250 to 330) K
- Vapor-Liquid Equilibrium for 1-Butanol + 1-Butene at (318.4 and 364.5) K and Vapor-Liquid Equilibrium of 1-Butanol + 2-Methylpropane, + n-Butane and 1-Butene + 2-Methylpropane at 318.4 K