SDS Volume
Volume 57. Ethene, p 255
Source Publication
Lebedeva, E. S.; Kashirina, A. S.; Grokholskaya, V. P.; Ref. Zh. Khim. Abstr. 1971, No. 138777, 92-100.
Conditions:
Room Temp:
323.15 - 423.15
$\pu{K}$
Pressure:
1.013 - 11.73
$\pu{MPa}$
Compiler:
Methodology:
Experiments are described in [1]. A steel vessel was used along with a heating block, thermostat and pressure gauge for measuring the P - T - x data. Approximate Henry's constants and ethene solubilities, corresponding to a gas partial pressure of 101.3 kPa were calculated by the compiler for pressures to 2.9 MPa at 50 °C, and 5.0 MPa at 100 °C and 150 °C.
At 50 °C: H = 1900 atm; $x_{1}$ = 0.00053
At 100 °C: H = 408.5 atm; $x_{1}$ = 0.0029
At 150 °C: H = 272 atm; $x_{1}$ = 0.0037
Sample Information:
- Ethene. Source and purity not specified.
- Bromochloromethane. Source and purity not specified. Densities and vapor pressures given in paper. Approximate equation for vapor pressures (compiler) based on data given: $\log (P/\pu{atm}) = 4.4726 - 1521.3/(T/\pu{K}$)
Measurement Errors:
Ambient temperature: δT/K = ±0.1 (authors)
Mass concentration (m/v) (1): δx1/x1 = ±2% (compiler)
Methodology Citation
1 Lebedeva, E. S.; Khodeva, S. M.; Zh. Fiz. Khim. 1961, 35, 2608.
System Components:
- Ethene, $\ce{ C2H4 }$; [74-85-1] NIST WebBook
- Bromochloromethane, $\ce{ CH2BrCl }$; [74-97-5] NIST WebBook
Experimental Data
Only interpolated or smoothed data above, given in this paper.
| $T$ (°C) | $y_{1}$ | $x_{1}$ | $P$ ($\pu{MPa}$) |
|---|---|---|---|
| 50 | 0.920 | 5 x 10-3 | 1.0131 |
| 50 | 0.940 | 0.010 | 2.0271 |
| 50 | 0.950 | 0.015 | 3.0401 |
| 50 | 0.955 | 0.040 | 4.0531 |
| 50 | 0.945 | 0.280 | 5.0661 |
| 50 | - | 0.900 | 5.6941 |
| 100 | 0.740 | 0.020 | 1.0131 |
| 100 | 0.835 | 0.040 | 2.0271 |
| 100 | 0.885 | 0.065 | 3.0401 |
| 100 | 0.890 | 0.110 | 4.0531 |
| 100 | 0.900 | 0.160 | 5.0661 |
| 100 | 0.905 | 0.210 | 6.0801 |
| 100 | 0.900 | 0.250 | 7.0931 |
| 100 | 0.895 | 0.310 | 8.1061 |
| 100 | 0.880 | 0.380 | 9.1191 |
| 100 | 0.845 | 0.500 | 10.321 |
| 100 | - | 0.770 | 10.791 |
| 150 | 0.410 | 5 x 10-3 | 1.0131 |
| 150 | 0.410 | 0.040 | 2.0271 |
| 150 | 0.595 | 0.065 | 3.0401 |
| 150 | 0.670 | 0.100 | 4.0531 |
| 150 | 0.725 | 0.130 | 5.0661 |
| 150 | 0.750 | 0.165 | 6.0801 |
| 150 | 0.775 | 0.205 | 7.0931 |
| 150 | 0.790 | 0.250 | 8.1061 |
| 150 | 0.790 | 0.305 | 9.1191 |
| 150 | 0.780 | 0.375 | 10.321 |
| 150 | 0.725 | 0.470 | 11.151 |
| 150 | - | 0.620 | 11.731 |
(1) Calculated by the compiler.
(2) Critical conditions.


