Datasets
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Lower consolute composition: mole fraction
-
Heat capacity at constant pressure per volume, J/K/m3 (2)
-
Lower consolute temperature, K (2)
Lower consolute composition: mole fraction of Nanofin (1)
[ref]
| Lower consolute composition: mole fraction of Nanofin (1) - Liquid mixture 1 |
| 0.0550 |
Heat capacity at constant pressure per volume, J/K/m3
[ref]
Operational condition: Mole fraction =
0.055 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Heat capacity at constant pressure per volume, J/K/m3 - Liquid mixture 1 |
| 264.00 |
4559000.00 |
| 264.47 |
4560000.00 |
| 264.95 |
4546000.00 |
| 265.42 |
4529000.00 |
| 265.90 |
4518000.00 |
| 266.37 |
4505000.00 |
| 266.84 |
4492000.00 |
| 267.32 |
4480000.00 |
| 267.79 |
4471000.00 |
| 268.26 |
4448000.00 |
| 268.74 |
4442000.00 |
| 269.21 |
4429000.00 |
| 269.68 |
4420000.00 |
| 270.16 |
4409000.00 |
| 270.63 |
4398000.00 |
| 271.10 |
4391000.00 |
| 271.58 |
4375000.00 |
| 272.05 |
4367000.00 |
| 272.52 |
4356000.00 |
| 273.00 |
4342000.00 |
| 273.47 |
4341000.00 |
| 273.94 |
4336000.00 |
| 274.42 |
4322000.00 |
| 274.89 |
4313000.00 |
| 275.36 |
4305000.00 |
| 275.84 |
4293000.00 |
| 276.31 |
4289000.00 |
| 276.78 |
4278000.00 |
| 277.25 |
4274000.00 |
| 277.73 |
4266000.00 |
| 278.20 |
4260000.00 |
| 278.68 |
4252000.00 |
| 279.15 |
4250000.00 |
| 279.62 |
4239000.00 |
| 280.10 |
4237000.00 |
| 280.57 |
4227000.00 |
| 281.04 |
4227000.00 |
| 281.51 |
4221000.00 |
| 281.99 |
4216000.00 |
| 282.46 |
4215000.00 |
| 282.94 |
4208000.00 |
| 283.41 |
4206000.00 |
| 283.88 |
4199000.00 |
| 284.36 |
4195000.00 |
| 284.83 |
4191000.00 |
| 285.30 |
4189000.00 |
| 285.77 |
4182000.00 |
| 286.25 |
4178000.00 |
| 286.72 |
4177000.00 |
| 287.19 |
4174000.00 |
| 287.67 |
4174000.00 |
| 288.14 |
4172000.00 |
| 288.61 |
4170000.00 |
| 289.09 |
4171000.00 |
| 289.56 |
4167000.00 |
| 290.03 |
4166000.00 |
| 290.51 |
4165000.00 |
| 290.98 |
4166000.00 |
| 291.45 |
4165000.00 |
| 291.93 |
4166000.00 |
| 292.60 |
4164000.00 |
| 292.81 |
4147000.00 |
| 293.02 |
4141000.00 |
| 293.23 |
4164000.00 |
| 293.45 |
4134000.00 |
| 293.66 |
4144000.00 |
| 293.87 |
4164000.00 |
| 294.08 |
4166000.00 |
| 294.30 |
4164000.00 |
| 294.51 |
4144000.00 |
| 294.72 |
4183000.00 |
| 294.93 |
4155000.00 |
| 295.14 |
4142000.00 |
| 295.36 |
4144000.00 |
| 295.57 |
4153000.00 |
| 295.78 |
4178000.00 |
| 295.99 |
4155000.00 |
| 296.20 |
4175000.00 |
| 296.42 |
4213000.00 |
| 296.63 |
4189000.00 |
| 296.84 |
4188000.00 |
| 297.06 |
4228000.00 |
| 297.27 |
4210000.00 |
| 297.48 |
4217000.00 |
| 297.69 |
4232000.00 |
| 297.90 |
4249000.00 |
| 298.12 |
4247000.00 |
| 298.33 |
4277000.00 |
| 298.54 |
4280000.00 |
| 298.75 |
4295000.00 |
| 298.96 |
4312000.00 |
| 299.18 |
4375000.00 |
| 299.39 |
4534000.00 |
Heat capacity at constant pressure per volume, J/K/m3
[ref]
Operational conditions:
- Pressure, kPa = 102.6 (Liquid)
- Mole fraction = 0.055 (Liquid)
| Temperature, K - Liquid |
Heat capacity at constant pressure per volume, J/K/m3 - Liquid |
| 299.60 |
5314000.00 |
| 299.81 |
5077000.00 |
| 300.03 |
5010000.00 |
| 300.24 |
4873000.00 |
| 300.45 |
4815000.00 |
| 300.66 |
4801000.00 |
| 300.88 |
4772000.00 |
| 301.09 |
4785000.00 |
| 301.30 |
4742000.00 |
| 301.51 |
4632000.00 |
| 301.73 |
4641000.00 |
| 301.94 |
4672000.00 |
| 302.15 |
4625000.00 |
| 302.36 |
4675000.00 |
| 302.57 |
4597000.00 |
| 302.79 |
4600000.00 |
| 303.00 |
4544000.00 |
| 303.21 |
4578000.00 |
| 303.42 |
4592000.00 |
| 303.64 |
4555000.00 |
| 303.85 |
4564000.00 |
| 304.06 |
4532000.00 |
| 304.27 |
4520000.00 |
| 304.49 |
4530000.00 |
| 304.70 |
4519000.00 |
| 304.91 |
4468000.00 |
| 305.12 |
4514000.00 |
| 305.33 |
4463000.00 |
| 305.55 |
4423000.00 |
| 305.76 |
4443000.00 |
Lower consolute temperature, K
[ref]
| Lower consolute temperature, K - Liquid mixture 1 |
| 299.48 |
Lower consolute temperature, K
[ref]
| Lower consolute temperature, K - Liquid mixture 1 |
| 299.16 |
Sources