<compilation>
 <compilers>Yuri P. Yampol'skii</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.05e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.05</significand>
    <unit>$\pu{cm3(STP) cm-3 cmHg-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.17e+00</number>
    <property>Amount concentration (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.17</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>4.91e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.91</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.84e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.84</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>4.03e+01</number>
    <property>Amount concentration (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.03</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>4.96e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.96</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Table 1. Dual mode sorption parameters for methane and carbon dioxide in PVC at 298 K</title>
 </dataset>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.7e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>1.7</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.8e-01</number>
    <property>Sorption</property>
    <sigfigs>2</sigfigs>
    <significand>3.8</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
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    <unit>$\pu{K}$</unit>
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    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>3.4</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>5.3e-01</number>
    <property>Sorption</property>
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    <significand>5.3</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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    <unit>$\pu{K}$</unit>
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    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>8.5e-01</number>
    <property>Sorption</property>
    <sigfigs>2</sigfigs>
    <significand>8.5</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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    <property>Ambient temperature</property>
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    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.11e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.11</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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    <property>Ambient temperature</property>
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    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
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   <data>
    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.13e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.13</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>7.8</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.42e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.42</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <supplemental></supplemental>
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   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
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    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
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   <data>
    <exponent>-1</exponent>
    <number>8.8e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>8.8</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.61e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.61</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
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   <data>
    <exponent>-1</exponent>
    <number>9.8e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>9.8</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.67e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.67</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>1.06e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.06</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.83e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.83</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
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   <data>
    <exponent>0</exponent>
    <number>1.16e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.16</significand>
    <unit>$\pu{MPa}$</unit>
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   <data>
    <exponent>0</exponent>
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    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.95</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <conditions>
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    <property>Ambient temperature</property>
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    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.6e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>1.6</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.48e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>3.48</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
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    <unit>$\pu{K}$</unit>
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   <data>
    <exponent>-1</exponent>
    <number>2.7e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>2.7</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>5.28e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>5.28</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <conditions>
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    <unit>$\pu{K}$</unit>
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    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>4.1</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
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    <unit>$\pu{K}$</unit>
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   <data>
    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>5.4</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>9.71e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>9.71</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <supplemental></supplemental>
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  <points>
   <conditions>
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    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>6.4e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.098e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>1.098</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>15</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
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    <unit>$\pu{K}$</unit>
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   <data>
    <exponent>-1</exponent>
    <number>7.7e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.272e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>1.272</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>16</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>8.8</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.399e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>1.399</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
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    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.527e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>1.527</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>18</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>1.14e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.14</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.694e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>1.694</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>19</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.98e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.98</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>1.27e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.27</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.801e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>1.801</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>20</pntnum>
   <supplemental></supplemental>
  </points>
  <series>2</series>
  <title>Table 2. Sorption isotherms of methane and carbon dioxide in PVC at 298 K (The original data wre represented graphically)</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Sorption isotherms were obtained by the pressure decay method. [1]. Conditioning at 23 atm for 60 h and degassing preceded the measurements.</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>Field, J. R.; Parker, B. E; Ballard, R. L.; Japan-US Polymer Symposium, pp. 247-248 (1985).</citation>
  <pubtype>symposium</pubtype>
 </sources>
 <substances>
  <casrn>9002-86-2</casrn>
  <constituent>2</constituent>
  <formula>(C2H3Cl)n</formula>
  <inchi>InChI=1S/C2H3Cl/c1-2-3/h2H,1H2</inchi>
  <inchikey>BZHJMEDXRYGGRV-UHFFFAOYSA-N</inchikey>
  <molweight>62.5</molweight>
  <name>Poly(vinyl chloride) (PVC)</name>
  <sample>PVC: Samples were compression modeled at 450 K from a mixture of low molecular mass PVC resin and 3% of a stabilizer (Cincinnati Milacorn (TM-692)).</sample>
 </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>
 </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>
 </substances>
 <system>Carbon dioxide, Methane and Poly(vinyl chloride) (PVC)</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Carbon dioxide, Methane and Poly(vinyl chloride) (PVC)</title>
</compilation>