<compilation>
 <compilers>Walter Hayduk</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.21e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.21</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>4.52e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.52</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.93e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.93</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.41e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.41</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.7315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.7315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>0</exponent>
    <number>0e+00</number>
    <property>Ambient temperature</property>
    <sigfigs>0</sigfigs>
    <significand>0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>4.01e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.01</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.49e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.49</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.5315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.5315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>-2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>-2.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>5.93e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.93</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.69e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.69</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.3315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.3315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>-4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>-4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>9.21e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>9.21</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.09e+01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.09</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.2315</significand>
    <unit>$\pu{K}$</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>-1</exponent>
    <number>1.20e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.20</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>8.33e+00</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>8.33</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>A static method was used. Details are given in [1].</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Braude, G. E.; Shakhova, C. F.; Khim. Prom. 1961, 3, 177.</citation>
  <pubtype>paper</pubtype>
 </reference>
 <sources>
  <citation>Kosyakov, N. E.; Yushko, V. L.; Sergienko, I. D.; Khokhlov, C. F.; Taraba, P. F.; Khim. Prom. 1972, 48, 432-433.</citation>
  <pubtype>paper</pubtype>
 </sources>
 <substances>
  <casrn>126-73-8</casrn>
  <constituent>2</constituent>
  <formula>C12H27O4P</formula>
  <inchi>InChI=1S/C12H27O4P/c1-4-7-10-14-17(13,15-11-8-5-2)16-12-9-6-3/h4-12H2,1-3H3</inchi>
  <inchikey>STCOOQWBFONSKY-UHFFFAOYSA-N</inchikey>
  <molweight>266.314</molweight>
  <name>Tributylphosphate</name>
  <sample>Purity and source unspecified.</sample>
 </substances>
 <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>Ethene minimum purity 99.0 mole%.</sample>
 </substances>
 <system>Ethene and Tributyl phosphate</system>
 <title>Solubility data from IUPAC SDS Volume 57 (page ?) - Ethene and Tributyl phosphate</title>
</compilation>