SDS Volume (1218)

Volume 57. Ethene, p None

Original Measurements

Shim, J.; Kohn, J. P.; J. Chem. Eng. Data 1964, 9, 1-2.

Variables:

Room Temp: 273 - 373 $\pu{K}$
Pressure: 1.0 - 10.2 $\pu{MPa}$

Prepared by:

W. Hayduk

Method/Apparatus/Procedure:

Calibrated borosilicate glass cells were used in two sizes: 12-mL for pressures to 70 atm and 5-mL for pressures from 70-100 atm. The cell was initially almost filled with solvent then evacuated to the solvent vapor pressure. The initial solvent volume was obtained. Gas was volumetrically charged from a high pressure reservoir by displacement with mercury. Gas absorption was facilitated using a magnetically actuated stainless steel ball. At the highest pressure the cell was essentially completely filled with solution. The change in solution volume was noted with each increment of gas. The corresponding gas phase compositions were obtained using separate experiments and measuring the small volume of solvent necessary to saturate the gas. Details in [1].

Source and Purity of Materials:
  1. Ethene was from Matheson; purity 99.5%. Gas dried at 50 atm pressure using silica gel.
  2. Chloroform was the spectro grade from Matheson Coleman Bell; no purity given.
Estimated Errors:

Ambient temperature: δT/K = ±0.07
Mass concentration (m/v) (1): δx1/x1 = ±0.01
Pressure: δP/P = ±0.01

References

1 Shim, J.; Kohn, J. P., J. Chem. Eng. Data 1962, 7, 3.

Components:
  1. Ethene, $\ce{ C2H4 }$; [74-85-1] NIST WebBook
  2. Trichloromethane, $\ce{ CHCl3 }$; [67-66-3] NIST WebBook
Experimental Data

Liquid phase and gas phase molar volumes also given in this paper

$T$ ($\pu{K}$) $T$ (°C) $y_{1}$ $x_{1}$ $P_{\rm{tot}}$ ($\pu{atm}$) $P_{\rm{tot}}$ ($\pu{MPa}$)
273.150 10.2361E+11.013
273.150 10.4752E+12.027
273.150 10.7083E+13.040
273.150 10.9644E+14.053
298.1525 0.9730.1481E+10.9859
298.1525 0.9870.2972E+12.000
298.1525 0.9930.4483E+13.018
298.1525 0.9990.6064E+14.050
298.1525 0.9990.7715E+15.061
298.1525 0.9780.9686E+15.946
298.1525 0.9690.96960.25.911
323.1550 0.9030.1141E+10.9150
323.1550 0.9520.2202E+11.929
323.1550 0.9660.3243E+12.936
323.1550 0.9700.4314E+13.931
323.1550 0.9720.5395E+14.924
323.1550 0.9720.6546E+15.909
323.1550 0.9590.7777E+16.802
323.1550 0.8940.89476.86.957
348.1575 0.8280.0781E+10.8390
348.1575 0.9050.1642E+11.834
348.1575 0.9360.2473E+12.845
348.1575 0.9470.3284E+13.838
348.1575 0.9500.4125E+14.813
348.1575 0.9500.5006E+15.776
348.1575 0.9430.5947E+16.688
348.1575 0.9260.6948E+17.506
348.1575 0.8740.8169E+17.97
348.1575 0.8300.83090.97.645
373.15100 0.6580.0571E+10.6667
373.15100 0.8330.1242E+11.688
373.15100 0.8700.1923E+12.645
373.15100 0.8860.2604E+13.591
373.15100 0.8960.3275E+14.539
373.15100 0.9020.3986E+15.484
373.15100 0.9040.4797E+16.412
373.15100 0.9020.5638E+17.312
373.15100 0.8880.6549E+18.098
373.15100 0.8370.7731E+28.481
373.15100 0.7970.797100.98.148

(2) Interpolated by authors.

(3) Critical conditions as indicated by authors.

(1) Calculated by the compiler.

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