- Name
- Butane, 1-bromo-
- InChI
- InChI=1S/C4H9Br/c1-2-3-4-5/h2-4H2,1H3
- InChI Key
- MPPPKRYCTPRNTB-UHFFFAOYSA-N
- Formula
- C4H9Br
- SMILES
- CCCCBr
- Mol. Weight (g/mol)
- 137.02
- CAS
- 109-65-9
- Name
- 1-Octanol
- InChI
- InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3
- InChI Key
- KBPLFHHGFOOTCA-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCCCCCO
- Mol. Weight (g/mol)
- 130.23
- CAS
- 111-87-5
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Datasets
- Excess molar enthalpy (molar enthalpy (2)
- Pvap - Vapor or sublimation pressure, kPa (2)
- Excess molar volume, m3/mol (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0250 | 0.3640 |
| 0.0571 | 0.6020 |
| 0.1224 | 0.8400 |
| 0.1949 | 0.9760 |
| 0.2361 | 1.021 |
| 0.2760 | 1.048 |
| 0.3205 | 1.057 |
| 0.3670 | 1.056 |
| 0.4661 | 1.005 |
| 0.5784 | 0.8890 |
| 0.7064 | 0.6920 |
| 0.8484 | 0.4000 |
| 0.9311 | 0.2040 |
Mole fraction of 1-Octanol (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.2
0.4
0.6
0.8
1
0.2
0.4
0.6000000000000001
0.8
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0250 | 0.3640 |
| 0.0571 | 0.6020 |
| 0.1224 | 0.8400 |
| 0.1949 | 0.9760 |
| 0.2361 | 1.021 |
| 0.2760 | 1.048 |
| 0.3205 | 1.057 |
| 0.3670 | 1.056 |
| 0.4661 | 1.005 |
| 0.5784 | 0.8890 |
| 0.7064 | 0.6920 |
| 0.8484 | 0.4000 |
| 0.9311 | 0.2040 |
Mole fraction of 1-Octanol (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.2
0.4
0.6
0.8
1
0.2
0.4
0.6000000000000001
0.8
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 278.15 | 0.1029 | 1.76 |
| 278.15 | 0.1957 | 1.73 |
| 278.15 | 0.2650 | 1.69 |
| 278.15 | 0.3503 | 1.60 |
| 278.15 | 0.4477 | 1.49 |
| 278.15 | 0.5528 | 1.34 |
| 278.15 | 0.6397 | 1.19 |
| 278.15 | 0.7345 | 0.96 |
| 278.15 | 0.8543 | 0.60 |
| 278.15 | 0.9136 | 0.38 |
| 283.15 | 0.1029 | 2.37 |
| 283.15 | 0.1957 | 2.30 |
| 283.15 | 0.2650 | 2.24 |
| 283.15 | 0.3504 | 2.12 |
| 283.15 | 0.4477 | 1.98 |
| 283.15 | 0.5529 | 1.78 |
| 283.15 | 0.6398 | 1.57 |
| 283.15 | 0.7345 | 1.27 |
| 283.15 | 0.8543 | 0.77 |
| 283.15 | 0.9136 | 0.49 |
| 288.15 | 0.1030 | 3.10 |
| 288.15 | 0.1958 | 3.02 |
| 288.15 | 0.2651 | 2.92 |
| 288.15 | 0.3504 | 2.78 |
| 288.15 | 0.4478 | 2.59 |
| 288.15 | 0.5530 | 2.31 |
| 288.15 | 0.6399 | 2.04 |
| 288.15 | 0.7346 | 1.64 |
| 288.15 | 0.8544 | 1.02 |
| 288.15 | 0.9137 | 0.64 |
| 293.15 | 0.1030 | 4.03 |
| 293.15 | 0.1958 | 3.92 |
| 293.15 | 0.2651 | 3.79 |
| 293.15 | 0.3505 | 3.59 |
| 293.15 | 0.4479 | 3.35 |
| 293.15 | 0.5531 | 2.98 |
| 293.15 | 0.6400 | 2.62 |
| 293.15 | 0.7347 | 2.10 |
| 293.15 | 0.8544 | 1.30 |
| 293.15 | 0.9137 | 0.81 |
| 298.15 | 0.1030 | 5.17 |
| 298.15 | 0.1959 | 5.03 |
| 298.15 | 0.2652 | 4.85 |
| 298.15 | 0.3506 | 4.60 |
| 298.15 | 0.4481 | 4.26 |
| 298.15 | 0.5532 | 3.81 |
| 298.15 | 0.6401 | 3.34 |
| 298.15 | 0.7349 | 2.68 |
| 298.15 | 0.8545 | 1.66 |
| 298.15 | 0.9138 | 1.03 |
| 303.15 | 0.1031 | 6.61 |
| 303.15 | 0.1960 | 6.40 |
| 303.15 | 0.2653 | 6.18 |
| 303.15 | 0.3508 | 5.85 |
| 303.15 | 0.4482 | 5.41 |
| 303.15 | 0.5534 | 4.81 |
| 303.15 | 0.6403 | 4.22 |
| 303.15 | 0.7350 | 3.38 |
| 303.15 | 0.8547 | 2.09 |
| 303.15 | 0.9138 | 1.31 |
| 308.15 | 0.1031 | 8.36 |
| 308.15 | 0.1961 | 8.06 |
| 308.15 | 0.2654 | 7.75 |
| 308.15 | 0.3510 | 7.33 |
| 308.15 | 0.4485 | 6.77 |
| 308.15 | 0.5537 | 6.02 |
| 308.15 | 0.6406 | 5.26 |
| 308.15 | 0.7352 | 4.23 |
| 308.15 | 0.8548 | 2.61 |
| 308.15 | 0.9139 | 1.63 |
| 313.15 | 0.1032 | 10.44 |
| 313.15 | 0.1962 | 10.06 |
| 313.15 | 0.2656 | 9.66 |
| 313.15 | 0.3512 | 9.12 |
| 313.15 | 0.4488 | 8.41 |
| 313.15 | 0.5540 | 7.46 |
| 313.15 | 0.6409 | 6.50 |
| 313.15 | 0.7355 | 5.21 |
| 313.15 | 0.8550 | 3.21 |
| 313.15 | 0.9140 | 2.03 |
| 318.15 | 0.1033 | 12.96 |
| 318.15 | 0.1965 | 12.42 |
| 318.15 | 0.2658 | 11.95 |
| 318.15 | 0.3516 | 11.26 |
| 318.15 | 0.4492 | 10.35 |
| 318.15 | 0.5544 | 9.16 |
| 318.15 | 0.6413 | 7.96 |
| 318.15 | 0.7358 | 6.36 |
| 318.15 | 0.8552 | 3.91 |
| 318.15 | 0.9141 | 2.47 |
| 323.15 | 0.1034 | 15.93 |
| 323.15 | 0.1967 | 15.25 |
| 323.15 | 0.2661 | 14.64 |
| 323.15 | 0.3520 | 13.78 |
| 323.15 | 0.4497 | 12.63 |
| 323.15 | 0.5550 | 11.16 |
| 323.15 | 0.6418 | 9.69 |
| 323.15 | 0.7362 | 7.70 |
| 323.15 | 0.8555 | 4.75 |
| 323.15 | 0.9143 | 3.01 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 278.15 | 0.1029 | 1.76 |
| 278.15 | 0.1957 | 1.73 |
| 278.15 | 0.2650 | 1.69 |
| 278.15 | 0.3503 | 1.60 |
| 278.15 | 0.4477 | 1.49 |
| 278.15 | 0.5528 | 1.34 |
| 278.15 | 0.6397 | 1.19 |
| 278.15 | 0.7345 | 0.96 |
| 278.15 | 0.8543 | 0.60 |
| 278.15 | 0.9136 | 0.38 |
| 283.15 | 0.1029 | 2.37 |
| 283.15 | 0.1957 | 2.30 |
| 283.15 | 0.2650 | 2.24 |
| 283.15 | 0.3504 | 2.12 |
| 283.15 | 0.4477 | 1.98 |
| 283.15 | 0.5529 | 1.78 |
| 283.15 | 0.6398 | 1.57 |
| 283.15 | 0.7345 | 1.27 |
| 283.15 | 0.8543 | 0.77 |
| 283.15 | 0.9136 | 0.49 |
| 288.15 | 0.1030 | 3.10 |
| 288.15 | 0.1958 | 3.02 |
| 288.15 | 0.2651 | 2.92 |
| 288.15 | 0.3504 | 2.78 |
| 288.15 | 0.4478 | 2.59 |
| 288.15 | 0.5530 | 2.31 |
| 288.15 | 0.6399 | 2.04 |
| 288.15 | 0.7346 | 1.64 |
| 288.15 | 0.8544 | 1.02 |
| 288.15 | 0.9137 | 0.64 |
| 293.15 | 0.1030 | 4.03 |
| 293.15 | 0.1958 | 3.92 |
| 293.15 | 0.2651 | 3.79 |
| 293.15 | 0.3505 | 3.59 |
| 293.15 | 0.4479 | 3.35 |
| 293.15 | 0.5531 | 2.98 |
| 293.15 | 0.6400 | 2.62 |
| 293.15 | 0.7347 | 2.10 |
| 293.15 | 0.8544 | 1.30 |
| 293.15 | 0.9137 | 0.81 |
| 298.15 | 0.1030 | 5.17 |
| 298.15 | 0.1959 | 5.03 |
| 298.15 | 0.2652 | 4.85 |
| 298.15 | 0.3506 | 4.60 |
| 298.15 | 0.4481 | 4.26 |
| 298.15 | 0.5532 | 3.81 |
| 298.15 | 0.6401 | 3.34 |
| 298.15 | 0.7349 | 2.68 |
| 298.15 | 0.8545 | 1.66 |
| 298.15 | 0.9138 | 1.03 |
| 303.15 | 0.1031 | 6.61 |
| 303.15 | 0.1960 | 6.40 |
| 303.15 | 0.2653 | 6.18 |
| 303.15 | 0.3508 | 5.85 |
| 303.15 | 0.4482 | 5.41 |
| 303.15 | 0.5534 | 4.81 |
| 303.15 | 0.6403 | 4.22 |
| 303.15 | 0.7350 | 3.38 |
| 303.15 | 0.8547 | 2.09 |
| 303.15 | 0.9138 | 1.31 |
| 308.15 | 0.1031 | 8.36 |
| 308.15 | 0.1961 | 8.06 |
| 308.15 | 0.2654 | 7.75 |
| 308.15 | 0.3510 | 7.33 |
| 308.15 | 0.4485 | 6.77 |
| 308.15 | 0.5537 | 6.02 |
| 308.15 | 0.6406 | 5.26 |
| 308.15 | 0.7352 | 4.23 |
| 308.15 | 0.8548 | 2.61 |
| 308.15 | 0.9139 | 1.63 |
| 313.15 | 0.1032 | 10.44 |
| 313.15 | 0.1962 | 10.06 |
| 313.15 | 0.2656 | 9.66 |
| 313.15 | 0.3512 | 9.12 |
| 313.15 | 0.4488 | 8.41 |
| 313.15 | 0.5540 | 7.46 |
| 313.15 | 0.6409 | 6.50 |
| 313.15 | 0.7355 | 5.21 |
| 313.15 | 0.8550 | 3.21 |
| 313.15 | 0.9140 | 2.03 |
| 318.15 | 0.1033 | 12.96 |
| 318.15 | 0.1965 | 12.42 |
| 318.15 | 0.2658 | 11.95 |
| 318.15 | 0.3516 | 11.26 |
| 318.15 | 0.4492 | 10.35 |
| 318.15 | 0.5544 | 9.16 |
| 318.15 | 0.6413 | 7.96 |
| 318.15 | 0.7358 | 6.36 |
| 318.15 | 0.8552 | 3.91 |
| 318.15 | 0.9141 | 2.47 |
| 323.15 | 0.1034 | 15.93 |
| 323.15 | 0.1967 | 15.25 |
| 323.15 | 0.2661 | 14.64 |
| 323.15 | 0.3520 | 13.78 |
| 323.15 | 0.4497 | 12.63 |
| 323.15 | 0.5550 | 11.16 |
| 323.15 | 0.6418 | 9.69 |
| 323.15 | 0.7362 | 7.70 |
| 323.15 | 0.8555 | 4.75 |
| 323.15 | 0.9143 | 3.01 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0702 | 1.0400e-07 |
| 0.1016 | 1.2700e-07 |
| 0.2062 | 1.6700e-07 |
| 0.2980 | 1.8300e-07 |
| 0.3954 | 1.8700e-07 |
| 0.4953 | 1.8200e-07 |
| 0.5976 | 1.6800e-07 |
| 0.6922 | 1.4200e-07 |
| 0.7908 | 1.1100e-07 |
| 0.8530 | 8.1000e-08 |
| 0.8904 | 5.7000e-08 |
Mole fraction of 1-Octanol (2)
Excess molar volume, m3/mol
6.00e-8
8.00e-8
1.00e-7
1.20e-7
1.40e-7
1.60e-7
1.80e-7
0.2
0.4
0.6000000000000001
0.8
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0702 | 1.0400e-07 |
| 0.1016 | 1.2700e-07 |
| 0.2062 | 1.6700e-07 |
| 0.2980 | 1.8300e-07 |
| 0.3954 | 1.8700e-07 |
| 0.4953 | 1.8200e-07 |
| 0.5976 | 1.6800e-07 |
| 0.6922 | 1.4200e-07 |
| 0.7908 | 1.1100e-07 |
| 0.8530 | 8.1000e-08 |
| 0.8904 | 5.7000e-08 |
Mole fraction of 1-Octanol (2)
Excess molar volume, m3/mol
6.00e-8
8.00e-8
1.00e-7
1.20e-7
1.40e-7
1.60e-7
1.80e-7
0.2
0.4
0.6000000000000001
0.8