<compilation>
 <compilers>Oleg M. Ilinitch</compilers>
 <dataset>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>3.40e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.40</significand>
    <unit>$\pu{kPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4e-01</number>
    <property>Solubility</property>
    <sigfigs>1</sigfigs>
    <significand>4</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>5.33e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.33</significand>
    <unit>$\pu{kPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>8e-01</number>
    <property>Solubility</property>
    <sigfigs>1</sigfigs>
    <significand>8</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>6.67e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>6.67</significand>
    <unit>$\pu{kPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.2e+00</number>
    <property>Solubility</property>
    <sigfigs>2</sigfigs>
    <significand>1.2</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>8.26e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>8.26</significand>
    <unit>$\pu{kPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.5e+00</number>
    <property>Solubility</property>
    <sigfigs>2</sigfigs>
    <significand>1.5</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Solubility of methane in the copolymer</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The conventional McBain sorption spring balance was used.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Ilinitch, O. M.; Semin, G. L.; Chertova, M. V.; Zamaraev, K. I.; J. Membr. Sci. 66, 1-8 (1992).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1016/0376-7388(92)80085-x</url>
 </sources>
 <substances>
  <casrn>74-82-8</casrn>
  <constituent>1</constituent>
  <formula>CH4</formula>
  <inchi>InChI=1S/CH4/h1H4</inchi>
  <inchikey>VNWKTOKETHGBQD-UHFFFAOYSA-N</inchikey>
  <molweight>16.0425</molweight>
  <name>Methane</name>
  <sample>All the gases had a purity $\pu{\gt 99.9\%}$.</sample>
 </substances>
 <substances>
  <constituent>2</constituent>
  <formula>None</formula>
  <molweight>0.0</molweight>
  <name>Copoly(2,6-dimethyl-1,4-phenylene oxide-2,6-diphenyl-1,4-phenylene oxide)</name>
  <sample>The co-polymer was prepared via oxidative co-polycondensation of two monomers. The purity of product $\pu{99.9\%}$, it had $d = \pu{1.10 g mL-1}$ and $T_{\rm{g}} = \pu{754 K}$. </sample>
 </substances>
 <system>Methane with Statistical co-polymer of 2,6-dimethyl- and 2,6-diphenyl-1,4-phenylene oxide</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page 1417) - Methane with Statistical co-polymer of 2,6-dimethyl- and 2,6-diphenyl-1,4-phenylene oxide</title>
</compilation>