<compilation>
 <compilers>Rosa Crovetto</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9115e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9115</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>1.8e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>1.8</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.554e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.554</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>2.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.951e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.951</significand>
    <unit>1</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>2.533e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>2.533</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9115e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9115</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>1.8e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>1.8</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.527e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.527</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.203e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.203</significand>
    <unit>1</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>5.066e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>5.066</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.156e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.156</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.723e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.723</significand>
    <unit>1</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>5.066e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>5.066</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0419e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0419</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.104e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.104</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.134e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.134</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>2.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.418e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.418</significand>
    <unit>1</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>2.533e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>2.533</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0419e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0419</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.104e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.104</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.917e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.917</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.415e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.415</significand>
    <unit>1</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>5.066e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>5.066</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.037e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.037</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>2.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.295e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.295</significand>
    <unit>1</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>2.533e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>2.533</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.766e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.766</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.221e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.221</significand>
    <unit>1</unit>
   </data>
   <pntnum>7</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>5.066e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>5.066</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.203e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.203</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>7.5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>7.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.784e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.784</significand>
    <unit>1</unit>
   </data>
   <pntnum>8</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>7.599e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>7.599</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.303e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.303</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>1</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.913e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.913</significand>
    <unit>1</unit>
   </data>
   <pntnum>9</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>1.0133e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>5</sigfigs>
    <significand>1.0133</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.410e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.410</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.5e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>1.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.052e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.052</significand>
    <unit>1</unit>
   </data>
   <pntnum>10</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>1.520e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.520</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.511e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.511</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>2e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>2</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.183e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.183</significand>
    <unit>1</unit>
   </data>
   <pntnum>11</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>2.026e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>2.026</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.810e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.810</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>4e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>4</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.573e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.573</significand>
    <unit>1</unit>
   </data>
   <pntnum>12</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>4.053e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>4.053</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.983e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.983</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>5e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.799e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.799</significand>
    <unit>1</unit>
   </data>
   <pntnum>13</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>5.066e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>5.066</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>9.316e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>9.316</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>2.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.162e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.162</significand>
    <unit>1</unit>
   </data>
   <pntnum>14</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>2.533e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>2.533</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.620e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.620</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.035e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.035</significand>
    <unit>1</unit>
   </data>
   <pntnum>15</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>5.066e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>5.066</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.046e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.046</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>7.5e+01</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>7.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.581e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.581</significand>
    <unit>1</unit>
   </data>
   <pntnum>16</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>7.599e+01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>7.599</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.201e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.201</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>1</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.781e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.781</significand>
    <unit>1</unit>
   </data>
   <pntnum>17</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>1.0133e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>5</sigfigs>
    <significand>1.0133</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.271e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.271</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.25e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.25</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.871e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.871</significand>
    <unit>1</unit>
   </data>
   <pntnum>18</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>1.267e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.267</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.323e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.323</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.5e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>2</sigfigs>
    <significand>1.5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.939e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.939</significand>
    <unit>1</unit>
   </data>
   <pntnum>19</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>1.520e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.520</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.504e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.504</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>2e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>2</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.174e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.174</significand>
    <unit>1</unit>
   </data>
   <pntnum>20</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>2.026e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>2.026</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.744e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.744</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>4e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>4</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.487e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.487</significand>
    <unit>1</unit>
   </data>
   <pntnum>21</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>4.053e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>4.053</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>4.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>4.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.887e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.887</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>5e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.673e+01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.673</significand>
    <unit>1</unit>
   </data>
   <pntnum>22</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>5.066e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>5.066</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>&lt;p&gt;Apparatus and procedure are described in [1]. A high-pressure autoclave was used with stirring.&lt;/p&gt;&lt;p&gt;Note that some measurements were done at pressures higher than the corresponding vapor pressure of $\ce{CO2}$. In these conditions liquid-liquid equilibria will exist.&lt;/p&gt;&lt;p&gt;For reference, for $\ce{CO2}$ $T_{\rm{c}} = \pu{304.2 K}$ and $P_{\rm{c}} = \pu{72.8 atm}$.&lt;/p&gt;</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Wiebe, R.; Gaddy, V. L.; J. Am. Chem. Soc. 1939, 61, 315-8</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/ja01871a025</url>
 </reference>
 <sources>
  <citation>Wiebe, R.; Gaddy, V. L.; J. Am. Chem. Soc. 1940, 62, 815-7.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/ja01861a033</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>99.98%</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>
  <sample>Not stated.</sample>
 </substances>
 <system>Carbon dioxide with Water</system>
 <title>Solubility data from IUPAC SDS Volume 62 (page ?) - Carbon dioxide with Water</title>
</compilation>