<compilation>
 <compilers>Yuri P. Yampol'skii</compilers>
 <dataset>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>3.80e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.80</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.2280e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>5</sigfigs>
    <significand>1.2280</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.96e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.96</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>7.00e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>7.00</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.684e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>4</sigfigs>
    <significand>2.684</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.74e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.74</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>4.39e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.39</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.1817e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>5</sigfigs>
    <significand>1.1817</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.16e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.16</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-2</exponent>
    <number>7.3e-02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>2</sigfigs>
    <significand>7.3</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.653e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>4</sigfigs>
    <significand>2.653</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.75e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.75</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Dual mode sorption parameters for carbon dioxide and methane in Kapton H at 333 K</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>A pressure decay method of sorption measurement used was described in detail in [1]. Each isotherm included several consecutive series of runs with stepwise pressure increase. The virgin films were degassed at 333 K for 120 h before measurement.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Koros, W. J.; Paul, D. R.; J. Polym. Sci., Polym. Phys. Ed., 1976, 14, 1903.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/pol.1976.180141014</url>
 </reference>
 <sources>
  <citation>Chern, R. T.; Koros, W. J.; Yui, R.; Hopfenberg, H. B.; Stannett, V. T.; J. Polym. Sci., Polym. Phys. Ed. 1984, 22, 1061.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/pol.1984.180220610</url>
 </sources>
 <substances>
  <casrn>25036-53-7</casrn>
  <constituent>2</constituent>
  <formula>None</formula>
  <molweight>0.0</molweight>
  <name>Copoly(pyromellitic dianhydride-oxydianiline) (PMDA-ODA)</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>$\ce{CO2}$ Coleman-grade 99.999%. $\ce{CH4}$: instrument-grade 99.7%. Kapton H: H. I. DuPont Co.; no glass transition temperature revealed in DSC measurement up to 777 K.</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>$\ce{CO2}$ Coleman-grade 99.999%. $\ce{CH4}$: instrument-grade 99.7%. Kapton H: H. I. DuPont Co.; no glass transition temperature revealed in DSC measurement up to 777 K.</sample>
 </substances>
 <system>Carbon dioxide, Methane and Polyimide Kapton H</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Carbon dioxide, Methane and Polyimide Kapton H</title>
</compilation>