<compilation>
 <compilers>Walter Hayduk</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.7335e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.7335</significand>
    <unit>K</unit>
   </conditions>
   <conditions>
    <exponent>-1</exponent>
    <number>2e-01</number>
    <property>Ambient temperature</property>
    <sigfigs>1</sigfigs>
    <significand>2</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.43e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.43</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.013e+02</number>
    <property>Pressure (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.013</significand>
    <unit>kPa</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>7e+01</number>
    <property>Henrys Constant</property>
    <sigfigs>1</sigfigs>
    <significand>7</significand>
    <unit>atm&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9815</significand>
    <unit>K</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.08e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.08</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.013e+02</number>
    <property>Pressure (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.013</significand>
    <unit>kPa</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>9.3e+01</number>
    <property>Henrys Constant</property>
    <sigfigs>2</sigfigs>
    <significand>9.3</significand>
    <unit>atm&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2315</significand>
    <unit>K</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>5.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>5.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>8.5e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>8.5</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.013e+02</number>
    <property>Pressure (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.013</significand>
    <unit>kPa</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.17e+02</number>
    <property>Henrys Constant</property>
    <sigfigs>3</sigfigs>
    <significand>1.17</significand>
    <unit>atm&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.4815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.4815</significand>
    <unit>K</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>7.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>7.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>7.2e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>7.2</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.013e+02</number>
    <property>Pressure (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.013</significand>
    <unit>kPa</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.39e+02</number>
    <property>Henrys Constant</property>
    <sigfigs>3</sigfigs>
    <significand>1.39</significand>
    <unit>atm&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.7315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.7315</significand>
    <unit>K</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>1.00e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>6.1e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>6.1</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.013e+02</number>
    <property>Pressure (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.013</significand>
    <unit>kPa</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.64e+02</number>
    <property>Henrys Constant</property>
    <sigfigs>3</sigfigs>
    <significand>1.64</significand>
    <unit>atm&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The apparatus and procedure are described in Ref. 1. The equilibration device is a capillary tube 1 mm in diameter containing an internal mixer which is moved up and down by means of an external, motor driven magnet. The capillary tube is sealed in a vertical position and connected to a gas and liquid charging system, pressure gauges, as well as a volume regulator to maintain a constant pressure and to determine the volume of gas charged.&lt;p&gt;Graphs of liquid solution molar volumes are also given as a function of solution compositions, including those for critical values at high pressures.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Kritchevskii, I. R.; Efremova, G. D.; Zh. Fiz. Khim. 1956, 30, 1877.</citation>
  <pubtype>paper</pubtype>
 </reference>
 <sources>
  <citation>Efremova, G. D.; Kovpakova, P. F.; Zh. Fiz. Khim. 1958, 32, 1231-1240.</citation>
  <pubtype>paper</pubtype>
 </sources>
 <substances>
  <casrn>74-85-1</casrn>
  <constituent>1</constituent>
  <formula>C2H4</formula>
  <inchi>InChI=1S/C2H4/c1-2/h1-2H2</inchi>
  <inchikey>VGGSQFUCUMXWEO-UHFFFAOYSA-N</inchikey>
  <molweight>28.0532</molweight>
  <name>Ethylene</name>
  <sample>Ethene purity 97.5% by analysis.</sample>
 </substances>
 <substances>
  <casrn>3922-36-9</casrn>
  <constituent>2</constituent>
  <formula>C7H12Cl4</formula>
  <inchi>InChI=1S/C7H12Cl4/c8-6-4-2-1-3-5-7(9,10)11/h1-6H2</inchi>
  <inchikey>HIZWVJSDYNNBMS-UHFFFAOYSA-N</inchikey>
  <molweight>237.982</molweight>
  <name>1,1,1,7-Tetrachloroheptane</name>
  <sample>Tetrachloro-propane vacuum distilled. Actual purity not given. Density and refractive index at 20&amp;deg;C:&lt;br /&gt;&amp;rho; = 1.2509 g cm&lt;sup&gt;-3&lt;/sup&gt;, &lt;br /&gt;n&lt;sub&gt;D&lt;/sub&gt; = 1.4843</sample>
 </substances>
 <system>Ethene with Heptane, 1,1,1,7-Tetrachloro-</system>
 <title>Solubility data from IUPAC SDS Volume 57 (page ?) - Ethene with Heptane, 1,1,1,7-Tetrachloro-</title>
</compilation>