<compilation>
 <compilers>Colin L. Young</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.082e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.082</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>4.25e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.25</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>2.35e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.35</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.232e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.232</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>5.06e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>5.06</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>1.98e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.98</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.432e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.432</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>6.18e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.18</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>1.62e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.62</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.632e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.632</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>7.44e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>7.44</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>1.34e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.34</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.732e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.732</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>8.18e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>8.18</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>1.22e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.22</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>4.232e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>4.232</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>2</exponent>
    <number>1.14e+02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.14</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>-3</exponent>
    <number>8.77e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>8.77</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
  <title>Solubility of Ethene (1) + Octadecane (2)</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Gas chromatographic method. Solvent supported on Chromosorb P in 6m column. Gas injected as sample, helium used as carrier gas. Henry's law constant calculated from knowledge of retention time and flow rate.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Ng, S.; Harris, H. G.; Prausnitz, J. M.; J. Chem. Eng. Data 1969, 14, 482-3.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/je60043a014</url>
 </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>Ethene</name>
  <sample>Matheson sample, purity greater than 99 mole%.</sample>
 </substances>
 <substances>
  <casrn>593-45-3</casrn>
  <constituent>2</constituent>
  <formula>C18H38</formula>
  <inchi>InChI=1S/C18H38/c1-3-5-7-9-11-13-15-17-18-16-14-12-10-8-6-4-2/h3-18H2,1-2H3</inchi>
  <inchikey>RZJRJXONCZWCBN-UHFFFAOYSA-N</inchikey>
  <molweight>254.494</molweight>
  <name>Octadecane</name>
  <sample>Matheson, Coleman and Bell sample, MP: Octadecane = 27-28.5&amp;deg;C, Eicosane = 35-36.5&amp;deg;C, Docosane = 43-45&amp;deg;C</sample>
 </substances>
 <system>Ethene with Octadecane</system>
 <title>Solubility data from IUPAC SDS Volume 57 (page 95) - Ethene with Octadecane</title>
</compilation>