<compilation>
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    <sigfigs>3</sigfigs>
    <significand>3.30</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>5.89e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>5.89</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>35</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>3.37e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.37</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>6.42e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>6.42</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>36</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>3.67e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.67</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>6.42e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>6.42</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>39</pntnum>
   <supplemental></supplemental>
  </points>
  <series>2</series>
  <title>Table 2. Sorption isotherms of methane in PEMA at 298 K (a) and 318 K (b) (The original data were represented graphically)</title>
 </dataset>
 <dataset>
  <points>
   <conditions></conditions>
   <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>-1</exponent>
    <number>3.3e-01</number>
    <property>Sorption</property>
    <sigfigs>2</sigfigs>
    <significand>3.3</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>3.9e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>3.9</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.8e-01</number>
    <property>Sorption</property>
    <sigfigs>2</sigfigs>
    <significand>4.8</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>5.0e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>5.0</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>6.1e-01</number>
    <property>Sorption</property>
    <sigfigs>2</sigfigs>
    <significand>6.1</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>7.7e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>7.7</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.4e-01</number>
    <property>Sorption</property>
    <sigfigs>2</sigfigs>
    <significand>9.4</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>8.5e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>8.5</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.07e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.07</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>1.04e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.04</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.22e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.22</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>1.26e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.26</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.51e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.51</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>7</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>1.40e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.40</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.68e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.68</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>8</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>1.61e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.61</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.94e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.94</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>9</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>1.75e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.75</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.05e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.05</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>10</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>1.98e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.98</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.25e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.25</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>11</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>2.04e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.04</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.42e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.42</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>12</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <number>2.27e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.27</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.66e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.66</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>13</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.45</significand>
    <unit>$\pu{MPa}$</unit>
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   <data>
    <exponent>0</exponent>
    <number>2.77e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.77</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>14</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.79</significand>
    <unit>$\pu{MPa}$</unit>
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   <data>
    <exponent>0</exponent>
    <number>3.21e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>3.21</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>15</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.85</significand>
    <unit>$\pu{MPa}$</unit>
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   <data>
    <exponent>0</exponent>
    <number>3.21e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>3.21</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>16</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>3.29e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.29</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.69e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>3.69</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>17</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{MPa}$</unit>
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   <data>
    <exponent>0</exponent>
    <number>3.82e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>3.82</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>18</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.68</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.08e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>4.08</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>19</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
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    <unit>$\pu{MPa}$</unit>
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   <data>
    <exponent>-1</exponent>
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    <property>Sorption</property>
    <sigfigs>2</sigfigs>
    <significand>7.0</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>20</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>-1</exponent>
    <number>5.1e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>5.1</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.29e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.29</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>21</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <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>
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    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.89</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>22</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <sigfigs>3</sigfigs>
    <significand>1.02</significand>
    <unit>$\pu{MPa}$</unit>
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   <data>
    <exponent>0</exponent>
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    <property>Sorption</property>
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    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>23</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
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    <property>Sorption</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>24</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.52</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.44e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>3.44</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>25</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.82</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.15e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>4.15</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>26</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.14</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.63e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>4.63</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>28</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>2.23e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.23</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>5.00e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>5.00</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>29</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.60</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
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    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>5.57</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>30</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
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    <property>Sorption</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>31</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions></conditions>
   <data>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
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    <property>Sorption</property>
    <sigfigs>3</sigfigs>
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    <unit>$\pu{V_{1}/V_{2}}$</unit>
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   <pntnum>32</pntnum>
   <supplemental></supplemental>
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  <points>
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   <data>
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   <data>
    <exponent>0</exponent>
    <number>2.03e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.03</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>67</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>3.53e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.53</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.99e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>1.99</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>68</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>3.67e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.67</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.21e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.21</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>69</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions></conditions>
   <data>
    <exponent>0</exponent>
    <number>3.78e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.78</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.21e+00</number>
    <property>Sorption</property>
    <sigfigs>3</sigfigs>
    <significand>2.21</significand>
    <unit>$\pu{V_{1}/V_{2}}$</unit>
   </data>
   <pntnum>70</pntnum>
   <supplemental></supplemental>
  </points>
  <series>3</series>
  <title>Table 3. Sorption isotherms of various gases in PEMA at 308 K (The original data were represented graphically)</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>1.83e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.83</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.87e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>2.87</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>6.77e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.77</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.08e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.08</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.65e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.65</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.24e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>2.24</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>5.36e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>5.36</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.13e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.13</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.44e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.44</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.87e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.87</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>4.22e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.22</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.08e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.08</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>9.02e-02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>9.02</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.20e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.20</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>4.05e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.05</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Table 1. Dual mode sorption parameters for methane and argon in PEMA</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Sorption isotherms were measured by the pressure decay method using a dual volume sorption cell.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Chiou, J. S.; Paul, D. R.; J. Membr. Sci. 45, 167 (1989).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1016/s0376-7388(00)80852-2</url>
 </sources>
 <substances>
  <casrn>97-63-2</casrn>
  <constituent>2</constituent>
  <formula>(C6H802)n</formula>
  <inchi>InChI=1S/C6H10O2/c1-4-8-6(7)5(2)3/h2,4H2,1,3H3</inchi>
  <inchikey>SUPCQIBBMFXVTL-UHFFFAOYSA-N</inchikey>
  <molweight>114.14</molweight>
  <name>Poly(ethyl methacrylate) (PEMA)</name>
  <sample>PEMA: DuPont Co. (Elvacite 2042). $M_{\rm{w}}$ = 438 000, $T_{\rm{g}}$ = 342 K (DSC method).</sample>
 </substances>
 <substances>
  <constituent>1</constituent>
  <formula>$\ce{Ar}$, $\ce{N2}$, $\ce{CO2}$ and $\ce{CH4}$</formula>
  <molweight>0.0</molweight>
  <name>Various gases (x4)</name>
 </substances>
 <system>Various gases (x4) and Poly(ethyl methacrylate) (PEMA)</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Various gases (x4) and Poly(ethyl methacrylate) (PEMA)</title>
</compilation>