<compilation>
 <compilers>Colin L. Young</compilers>
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   <data>
    <exponent>-3</exponent>
    <number>1.2e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>1.2</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>4.71e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>4.71</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>4.22e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>4.22</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>4.06e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.06</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>14</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.30e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.30</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.57e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.57</significand>
    <unit>&amp;deg;C</unit>
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   <data>
    <exponent>-3</exponent>
    <number>1.2e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>1.2</significand>
    <unit>1</unit>
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   <data>
    <exponent>1</exponent>
    <number>4.85e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>4.85</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>4.36e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>4.36</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.98e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.98</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>15</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.64e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.64</significand>
    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>2.91e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.91</significand>
    <unit>&amp;deg;C</unit>
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   <data>
    <exponent>-3</exponent>
    <number>1.5e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>1.5</significand>
    <unit>1</unit>
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   <data>
    <exponent>1</exponent>
    <number>7.85e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>7.85</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>1</exponent>
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    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>7.37</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>3</exponent>
    <number>3.15e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.15</significand>
    <unit>$\pu{atm}$</unit>
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   <pntnum>16</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.71e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.71</significand>
    <unit>$\pu{K}$</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>&amp;deg;C</unit>
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   <data>
    <exponent>-3</exponent>
    <number>1.6e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>1.6</significand>
    <unit>1</unit>
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   <data>
    <exponent>1</exponent>
    <number>8.59e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>8.59</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>1</exponent>
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    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.15</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>3</exponent>
    <number>2.69e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.69</significand>
    <unit>$\pu{atm}$</unit>
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   <pntnum>17</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.78e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.78</significand>
    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>3.05e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.05</significand>
    <unit>&amp;deg;C</unit>
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   <data>
    <exponent>-3</exponent>
    <number>1.7e-03</number>
    <property>Mole fraction - Liquid (1)</property>
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    <significand>1.7</significand>
    <unit>1</unit>
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   <data>
    <exponent>1</exponent>
    <number>9.45e+01</number>
    <property>Ambient pressure</property>
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    <significand>9.45</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>1</exponent>
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    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.99</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>3</exponent>
    <number>2.78e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.78</significand>
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   <pntnum>18</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.87e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.87</significand>
    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>3.14e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.14</significand>
    <unit>&amp;deg;C</unit>
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   <data>
    <exponent>-3</exponent>
    <number>1.9e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>1.9</significand>
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   <data>
    <exponent>2</exponent>
    <number>1.058e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>1.058</significand>
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   <data>
    <exponent>2</exponent>
    <number>1.019e+02</number>
    <property>Pressure (2)</property>
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    <significand>1.019</significand>
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   <data>
    <exponent>3</exponent>
    <number>2.03e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.03</significand>
    <unit>$\pu{atm}$</unit>
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   <pntnum>19</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.95e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.95</significand>
    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>3.22e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.22</significand>
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   <data>
    <exponent>-3</exponent>
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    <property>Mole fraction - Liquid (1)</property>
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    <significand>1.8</significand>
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   <data>
    <exponent>2</exponent>
    <number>1.171e+02</number>
    <property>Ambient pressure</property>
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    <significand>1.171</significand>
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   <data>
    <exponent>2</exponent>
    <number>1.131e+02</number>
    <property>Pressure (2)</property>
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    <significand>1.131</significand>
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   <data>
    <exponent>3</exponent>
    <number>2.25e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.25</significand>
    <unit>$\pu{atm}$</unit>
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   <pntnum>20</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>6.16e+02</number>
    <property>Ambient temperature</property>
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    <significand>6.16</significand>
    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>3.43e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.43</significand>
    <unit>&amp;deg;C</unit>
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   <data>
    <exponent>-3</exponent>
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    <property>Mole fraction - Liquid (1)</property>
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    <significand>2.2</significand>
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   <data>
    <exponent>2</exponent>
    <number>1.523e+02</number>
    <property>Ambient pressure</property>
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    <significand>1.523</significand>
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   <data>
    <exponent>2</exponent>
    <number>1.481e+02</number>
    <property>Pressure (2)</property>
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    <significand>1.481</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>3</exponent>
    <number>1.87e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.87</significand>
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   <pntnum>21</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
    <number>6.21e+02</number>
    <property>Ambient temperature</property>
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    <significand>6.21</significand>
    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>3.48e+02</number>
    <property>Ambient temperature</property>
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    <significand>3.48</significand>
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   <data>
    <exponent>-3</exponent>
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    <property>Mole fraction - Liquid (1)</property>
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    <significand>2.3</significand>
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   <data>
    <exponent>2</exponent>
    <number>1.619e+02</number>
    <property>Ambient pressure</property>
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    <significand>1.619</significand>
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   <data>
    <exponent>2</exponent>
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    <property>Pressure (2)</property>
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    <significand>1.576</significand>
    <unit>$\pu{atm}$</unit>
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   <data>
    <exponent>3</exponent>
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    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.86</significand>
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 </dataset>
 <dataset>
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    <exponent>2</exponent>
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    <significand>4.36</significand>
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   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
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    <significand>1.63</significand>
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   <data>
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    <property>Mole fraction - Liquid (1)</property>
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    <exponent>0</exponent>
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    <property>Ambient pressure</property>
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   <data>
    <exponent>0</exponent>
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   <data>
    <exponent>3</exponent>
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    <property>Henry's Law Solubility Coefficient</property>
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    <significand>4.73</significand>
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   <pntnum>23</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
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    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>1.79e+02</number>
    <property>Ambient temperature</property>
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    <significand>1.79</significand>
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   <data>
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    <property>Mole fraction - Liquid (1)</property>
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    <significand>3.6</significand>
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   <data>
    <exponent>1</exponent>
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    <property>Ambient pressure</property>
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   <data>
    <exponent>0</exponent>
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    <exponent>3</exponent>
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    <property>Henry's Law Solubility Coefficient</property>
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    <significand>4.53</significand>
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   <pntnum>24</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
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    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
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   <data>
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    <property>Mole fraction - Liquid (1)</property>
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    <exponent>1</exponent>
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    <significand>1.47</significand>
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    <exponent>1</exponent>
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    <property>Pressure (2)</property>
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    <significand>1.315</significand>
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   <data>
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    <property>Henry's Law Solubility Coefficient</property>
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    <significand>4.22</significand>
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   <pntnum>25</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
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    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
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    <property>Ambient temperature</property>
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    <significand>1.99</significand>
    <unit>&amp;deg;C</unit>
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   <data>
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    <property>Mole fraction - Liquid (1)</property>
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    <property>Ambient pressure</property>
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    <significand>1.63</significand>
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   <data>
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   <data>
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    <property>Henry's Law Solubility Coefficient</property>
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    <significand>3.76</significand>
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   <pntnum>26</pntnum>
   <supplemental></supplemental>
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  <points>
   <conditions>
    <exponent>2</exponent>
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    <unit>$\pu{K}$</unit>
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   <conditions>
    <exponent>2</exponent>
    <number>2.22e+02</number>
    <property>Ambient temperature</property>
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    <significand>2.22</significand>
    <unit>&amp;deg;C</unit>
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   <data>
    <exponent>1</exponent>
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    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.52</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.362e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>4</sigfigs>
    <significand>2.362</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.64e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.64</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>27</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>4.97e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>4.97</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.24e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.24</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>3.8e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>3.8</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.60e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.60</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.453e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>4</sigfigs>
    <significand>2.453</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.89e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.89</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>28</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.00e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.00</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.27e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.27</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>4.0e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.75e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>2.75</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.594e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>4</sigfigs>
    <significand>2.594</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.9e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>2</sigfigs>
    <significand>3.9</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>29</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.06e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.06</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.33e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.33</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>4.1e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>4.1</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.04e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.04</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.896e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>4</sigfigs>
    <significand>2.896</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.55e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.55</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>30</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.157e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>5.157</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.425e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.425</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>4.6e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>4.6</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.60e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.60</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.43e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>3.43</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.73e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.73</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>31</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.17e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.17</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.44e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.44</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>4.5e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>4.5</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.68e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>3.68</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.52e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>3.52</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.53e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.53</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>32</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.60e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.60</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.87e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.87</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>5.4e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>5.4</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>7.16e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>7.16</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>6.98e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>6.98</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.31e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.31</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>33</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.61e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.61</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.88e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.88</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>5.2e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>5.2</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>7.25e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>7.25</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>7.08e+01</number>
    <property>Pressure (2)</property>
    <sigfigs>3</sigfigs>
    <significand>7.08</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>3.25e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.25</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>34</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.90e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.90</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.17e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.17</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>6.5e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>6.5</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.067e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>1.067</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.050e+02</number>
    <property>Pressure (2)</property>
    <sigfigs>4</sigfigs>
    <significand>1.050</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>2.6e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>2</sigfigs>
    <significand>2.6</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>35</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.92e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.92</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.19e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.19</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>6.7e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>6.7</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.111e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>1.111</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.093e+02</number>
    <property>Pressure (2)</property>
    <sigfigs>4</sigfigs>
    <significand>1.093</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>3</exponent>
    <number>2.68e+03</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.68</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>36</pntnum>
   <supplemental></supplemental>
  </points>
  <series>2</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Static bomb of approximately 100 mL capacity. Heated in electric tube furnace. Liquid volume of approximately half to two thirds bomb volume. Samples of mixture analyzed by absorbing water in Anhydrone and carbon dioxide in carbsorb. Details in source.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Ellis, A. J.; Am. J. Sci. 1959, 257, 217-34.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.2475/ajs.257.3.217</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>Carbon dioxide generated in apparatus by reaction of sodium bicarbonate and hydrochloric acid.&lt;br/&gt;Two series studied:&lt;br/&gt;Series A: 0.02 moles $\ce{NaHCO3}$; 0.00797 moles $\ce{HCl}$; 42 or 52 mL of water.&lt;br/&gt;Series B: 0.007 moles $\ce{NaHCO3}$; 0.00302 moles $\ce{HCl}$; 55 mL of water.</sample>
 </substances>
 <substances>
  <casrn>7732-18-5</casrn>
  <constituent>2</constituent>
  <formula>H2O</formula>
  <inchi>InChI=1S/H2O/h1H2</inchi>
  <inchikey>XLYOFNOQVPJJNP-UHFFFAOYSA-N</inchikey>
  <molweight>18.0153</molweight>
  <name>Water</name>
 </substances>
 <system>Carbon dioxide with Water</system>
 <title>Solubility data from IUPAC SDS Volume 62 (page ?) - Carbon dioxide with Water</title>
</compilation>