SDS Volume

Volume 57. Ethene, p 96

Source Publication

Simon, F.; Lukacs, J.; Magy. Asvanyolaj-Foldaz. Intez. Kozl. (Hungary) 1977, 18, 57-66.

Conditions:

Room Temp: 293.15 - 333.15 $\pu{K}$
Pressure: 101.325 $\pu{kPa}$

Compiler:

W. Hayduk

Methodology:

The gas solubility was determined using gas chromatography and employing helium as a carrier gas.
Based on the retention times and column characteristics, the Bunsen coefficient was calculated.

Sample Information:
  1. Sources and purities of gas and solvent not specified.
Measurement Errors:

Ambient temperature: δT/K = ±0.1
Mass concentration (m/v) (1): δp1/kPa = 2.0
δKB = ±6-8% (authors)

System Components:
  1. Ethene, $\ce{ C2H4 }$; [74-85-1] NIST WebBook
  2. 2,6,10,15,19,23-Hexamethyltetracosane, $\ce{ C30H64 }$; [111-01-3] NIST WebBook
Experimental Data

Also available in the paper were ethene Bunsen coefficients in four transformer oils, the properties of which were not specified.

$T$ ($\pu{K}$) $T$ (°C) $x_{1}$ $L$ α ($\pu{cm3(g) cm-3(l) atm-1}$)
293.1520 0.037321.7821.661
313.1540 0.028921.4321.251
323.1550 0.025721.3021.091
333.1560 0.023021.1820.9701

(1) The solubility results were in the form of two equations, the first describing the temperature effect at 101.3 kPa pressure and the second the effect of pressure, to 405.2 kPa, at 313.15 K:
log KB = 568.0378 ( T/K)-1 - 1.1785     correlation coeff. = 0.9985
KB = 0.0101 p/atm + 1.2241               correlation coeff. = 0.3171 (low)

(2) The Ostwald coefficient and mole fraction solubility at 101.3 kPa were calculated by the compiler. The solvent densities were extrapolated.

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