<compilation>
 <compilers>Alexandre K. Bokarev</compilers>
 <dataset>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>2.89e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.89</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.001e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>4</sigfigs>
    <significand>1.001</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.84e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.84</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-2</exponent>
    <number>5.1e-02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>2</sigfigs>
    <significand>5.1</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.70e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>2.70</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>6.7e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>2</sigfigs>
    <significand>6.7</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Dual mode sorption parameters for PHE at 308 K</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The sorption apparatus and procedures used in the present sorption experiments are the same as described earlier [1].</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Koros, W. J.; Paul, D. R.; Rocha, A. A.; J. Polym. Sci., Polym. Phys. Ed., 1976, 14, 687.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/pol.1976.180140410</url>
 </reference>
 <sources>
  <citation>Barbari, T. A.; Koros, W. J.; Paul, D. R.; J. Polym. Sci. B: Polym. Phys. 26, 729-744 (1988).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/polb.1988.090260402</url>
 </sources>
 <substances>
  <casrn>26402-79-9</casrn>
  <constituent>2</constituent>
  <formula>(C18H20O3)n</formula>
  <inchi>InChI=1S/C18H22O3/c1-13(2)17-5-3-4-6-18(17)14-7-9-16(10-8-14)21-12-15(20)11-19/h3-10,15,18-20H,11-12H2,1-2H3</inchi>
  <inchikey>LPXOYRYOYTYPRA-UHFFFAOYSA-N</inchikey>
  <molweight>284.35</molweight>
  <name>Polyhydroxyether (PHE)</name>
 </substances>
 <substances>
  <casrn>124-38-9</casrn>
  <constituent>1</constituent>
  <formula>CO2</formula>
  <inchi>InChI=1S/CO2/c2-1-3</inchi>
  <inchikey>CURLTUGMZLYLDI-UHFFFAOYSA-N</inchikey>
  <molweight>44.0095</molweight>
  <name>Carbon dioxide</name>
  <sample>PHE (Union Carbide) had a trade name Phenoxy PKHH.&lt;br/&gt;Density: 1.18 g mL-1; $T_{\rm{g}}$ = 376 K.&lt;br/&gt;Each gas was of chromatographic quality (purity &gt; 99.99%).</sample>
 </substances>
 <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>PHE (Union Carbide) had a trade name Phenoxy PKHH.&lt;br/&gt;Density: 1.18 g mL-1; $T_{\rm{g}}$ = 376 K.&lt;br/&gt;Each gas was of chromatographic quality (purity &gt; 99.99%).</sample>
 </substances>
 <system>Carbon dioxide, Methane and Polyhydroxyether (PHE)</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Carbon dioxide, Methane and Polyhydroxyether (PHE)</title>
</compilation>