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) |
| 241.56 | 234.91 |
| 258.71 | 243.5 |
| 260.59 | 244.66 |
| 262.46 | 245.74 |
| 264.33 | 246.95 |
| 266.19 | 248.18 |
| 268.04 | 249.42 |
| 269.89 | 250.62 |
| 271.74 | 251.77 |
| 273.58 | 253.3 |
| 275.41 | 254.82 |
| 243.49 | 235.74 |
| 277.24 | 256.14 |
| 279.06 | 257.48 |
| 280.87 | 259.09 |
| 282.68 | 260.54 |
| 284.48 | 261.95 |
| 286.27 | 263.46 |
| 288.06 | 265.02 |
| 289.84 | 266.66 |
| 291.61 | 268.18 |
| 293.38 | 270.14 |
| 245.41 | 236.4 |
| 295.13 | 271.58 |
| 296.89 | 273.08 |
| 298.63 | 274.82 |
| 300.38 | 276.64 |
| 302.11 | 278.13 |
| 303.83 | 279.76 |
| 305.55 | 281.48 |
| 307.27 | 283.15 |
| 308.97 | 284.94 |
| 310.67 | 286.86 |
| 247.33 | 237.15 |
| 312.17 | 287.58 |
| 312.48 | 287.74 |
| 313.47 | 289.53 |
| 315.15 | 291.13 |
| 316.82 | 292.75 |
| 318.49 | 294.51 |
| 320.15 | 296.14 |
| 321.81 | 297.32 |
| 323.47 | 298.29 |
| 325.13 | 300.22 |
| 249.24 | 238.27 |
| 326.77 | 304.1 |
| 328.40 | 306.16 |
| 330.02 | 307.87 |
| 331.64 | 309.45 |
| 333.25 | 311.37 |
| 334.86 | 313.07 |
| 336.46 | 315.09 |
| 338.06 | 316.8 |
| 339.65 | 318.31 |
| 341.23 | 320.04 |
| 251.15 | 239.26 |
| 342.81 | 321.74 |
| 344.38 | 323.31 |
| 345.95 | 325.06 |
| 347.51 | 326.69 |
| 349.06 | 328.33 |
| 350.62 | 329.86 |
| 352.17 | 331.49 |
| 353.71 | 333.02 |
| 355.25 | 334.62 |
| 356.78 | 336.3 |
| 253.05 | 240.26 |
| 358.30 | 337.67 |
| 363.71 | 342.83 |
| 365.22 | 344.07 |
| 366.73 | 345.59 |
| 368.24 | 346.84 |
| 369.74 | 347.99 |
| 254.94 | 241.3 |
| 256.83 | 242.37 |
216; 1-heptanol; 00114