Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K van Miltenburg, J.C.; Gabrielová, H.; Růžička, K.; Journal of Chemical & Engineering Data 2003, 48, 1323-1331
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Molar heat capacity at saturation pressure
- Methodology: VADIAC:UFactor:2
- Phase(s): Liquid
- Substances:
Data
| T (K) | Cpsat (J mol-1 K-1) |
| 260.72 | 276.51 |
| 283.19 | 293.87 |
| 285.63 | 296.0 |
| 292.88 | 303.04 |
| 295.28 | 305.54 |
| 297.66 | 307.64 |
| 300.98 | 311.08 |
| 302.16 | 312.05 |
| 304.21 | 314.16 |
| 306.25 | 316.36 |
| 308.28 | 318.62 |
| 263.26 | 278.28 |
| 310.30 | 320.94 |
| 312.31 | 323.19 |
| 314.32 | 325.48 |
| 316.31 | 327.65 |
| 318.29 | 329.87 |
| 320.27 | 332.17 |
| 322.24 | 334.52 |
| 324.20 | 336.75 |
| 326.16 | 339.1 |
| 328.10 | 341.4 |
| 265.79 | 279.96 |
| 330.05 | 343.52 |
| 331.98 | 345.75 |
| 333.90 | 348.22 |
| 335.82 | 350.3 |
| 337.73 | 352.81 |
| 339.63 | 354.92 |
| 341.53 | 356.95 |
| 343.41 | 359.19 |
| 345.29 | 361.35 |
| 347.17 | 363.47 |
| 268.30 | 281.74 |
| 349.03 | 365.55 |
| 350.89 | 367.72 |
| 352.74 | 369.8 |
| 354.59 | 371.63 |
| 356.43 | 373.69 |
| 358.26 | 375.61 |
| 360.09 | 377.59 |
| 361.91 | 379.46 |
| 363.73 | 381.3 |
| 365.54 | 383.13 |
| 270.80 | 283.47 |
| 367.34 | 384.79 |
| 369.14 | 386.39 |
| 370.94 | 387.9 |
| 372.73 | 389.69 |
| 374.51 | 391.32 |
| 376.30 | 393.1 |
| 378.07 | 394.44 |
| 379.85 | 395.86 |
| 381.62 | 397.23 |
| 383.38 | 398.77 |
| 273.30 | 285.37 |
| 385.15 | 400.21 |
| 386.92 | 401.56 |
| 388.68 | 402.87 |
| 390.44 | 404.11 |
| 392.19 | 405.29 |
| 393.95 | 406.53 |
| 395.70 | 407.67 |
| 397.45 | 408.64 |
| 275.79 | 287.38 |
| 278.27 | 289.49 |
| 280.73 | 291.59 |
73; 1-octanol; 00046