<compilation>
 <compilers>Oleg M. Ilinitch</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>3.3e+00</number>
    <property>Pressure (1)</property>
    <sigfigs>2</sigfigs>
    <significand>3.3</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>2.8e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>2.8</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>6.3e+00</number>
    <property>Pressure (1)</property>
    <sigfigs>2</sigfigs>
    <significand>6.3</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>3.6e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>3.6</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>9.6e+00</number>
    <property>Pressure (1)</property>
    <sigfigs>2</sigfigs>
    <significand>9.6</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>4.3e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>4.3</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.33e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.33</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>5.1e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>5.1</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.87e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.87</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>5.8e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>5.8</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.40e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.40</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>6.6e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>6.6</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.93e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.93</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>7.3e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>7.3</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>7</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.93e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.93</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>4.9e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>4.9</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>8</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>3.33e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.33</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>5.5e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>5.5</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>9</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>3.44e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.44</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>7.9e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>7.9</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>10</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>4.00e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.00</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>8.4e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>8.4</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>11</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>4.67e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.67</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>9.4e+00</number>
    <property>Solubility (v/v)</property>
    <sigfigs>2</sigfigs>
    <significand>9.4</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>12</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.33e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.33</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>1.02e+01</number>
    <property>Solubility (v/v)</property>
    <sigfigs>3</sigfigs>
    <significand>1.02</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>13</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>6.13e+01</number>
    <property>Pressure (1)</property>
    <sigfigs>3</sigfigs>
    <significand>6.13</significand>
    <unit>$\pu{kPa}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>1.12e+01</number>
    <property>Solubility (v/v)</property>
    <sigfigs>3</sigfigs>
    <significand>1.12</significand>
    <unit>$\pu{cm3(STP) cm-3(s)}$</unit>
   </data>
   <pntnum>14</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Solubility $C_{vv}$ of propane 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>74-98-6</casrn>
  <constituent>1</constituent>
  <formula>C3H8</formula>
  <inchi>InChI=1S/C3H8/c1-3-2/h3H2,1-2H3</inchi>
  <inchikey>ATUOYWHBWRKTHZ-UHFFFAOYSA-N</inchikey>
  <molweight>44.0956</molweight>
  <name>Propane</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>Propane 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 1416) - Propane with Statistical co-polymer of 2,6-dimethyl- and 2,6-diphenyl-1,4-phenylene oxide</title>
</compilation>