<compilation>
 <compilers>Yuri P. Yampol'skii</compilers>
 <dataset>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>1.353e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>1.353</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.1e-01</number>
    <property>Pressure</property>
    <sigfigs>2</sigfigs>
    <significand>2.1</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>2.609e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>2.609</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>6.0e-01</number>
    <property>Pressure</property>
    <sigfigs>2</sigfigs>
    <significand>6.0</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>3.548e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>3.548</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.8e-01</number>
    <property>Pressure</property>
    <sigfigs>2</sigfigs>
    <significand>9.8</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>4.217e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>4.217</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.33e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.33</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>4.841e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>4.841</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.65e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.65</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>5.261e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>5.261</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.95e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.95</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>5.750e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>5.750</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.26e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.26</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>7</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>6.195e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>6.195</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.51e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.51</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>8</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>6.481e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>6.481</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.77e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.77</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>9</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>6.880e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>6.880</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.03e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.03</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>10</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>7.190e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>7.190</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.27e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.27</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>11</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>7.591e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>7.591</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.47e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.47</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>12</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>8.036e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>8.036</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.72e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.72</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>13</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>8.460e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>8.460</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.91e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.91</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>14</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>8.839e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>8.839</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.13e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>4.13</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>15</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>9.286e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>9.286</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.30e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>4.30</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>16</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>1</exponent>
    <number>9.349e+01</number>
    <property>Sorption</property>
    <sigfigs>4</sigfigs>
    <significand>9.349</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.47e+00</number>
    <property>Pressure</property>
    <sigfigs>3</sigfigs>
    <significand>4.47</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>17</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Sorption isotherms of carbon dioxide in TMPC on a fugacity basis at 308 K (The original data were represented graphically)</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Pressure decay sorption cell and procedure used are described in [1].</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Fleming, G. K.; Koros, W. J.; Macromolecules 19, 2285 (1986).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/ma00162a030</url>
 </reference>
 <sources>
  <citation>Fleming, G. K.; Koros, W. J.; J. Polym. Sci. B: Polym. Phys. 28, 1137 (1990).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/polb.1990.090280711</url>
 </sources>
 <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>$\ce{CO2}$: Linde Inc., purity 99.99%. TMPC: Bayer AG, $\rho = \pu{1.083 g mL-1}$, $T_{\rm{g}}$ = 475 K, $d$ spacing 6.0 Å (WAXD).</sample>
 </substances>
 <substances>
  <casrn>38797-88-5</casrn>
  <constituent>2</constituent>
  <formula>None</formula>
  <molweight>0.0</molweight>
  <name>Tetramethylpolycarbonate (TMPC)</name>
 </substances>
 <system>Carbon dioxide with Tetramethylpolycarbonate (TMPC)</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Carbon dioxide with Tetramethylpolycarbonate (TMPC)</title>
</compilation>