<compilation>
 <compilers>Rosa Crovetto</compilers>
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   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.256e-01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>4.256</significand>
    <unit>1</unit>
   </data>
   <pntnum>14</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.144e+00</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.144</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.2745e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2745</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>5.43e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.43</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>3.273e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>3.273</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.00e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.046e-01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>4.046</significand>
    <unit>1</unit>
   </data>
   <pntnum>15</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.166e+00</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.166</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.3625e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.3625</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>6.31e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>6.31</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>2.824e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.824</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.00e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.491e-01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.491</significand>
    <unit>1</unit>
   </data>
   <pntnum>16</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.243e+00</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.243</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.4135e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.4135</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>6.82e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>6.82</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>2.648e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.648</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.00e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.273e-01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.273</significand>
    <unit>1</unit>
   </data>
   <pntnum>17</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.302e+00</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.302</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.4555e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.4555</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>7.24e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>7.24</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>2.483e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.483</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.00e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.069e-01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.069</significand>
    <unit>1</unit>
   </data>
   <pntnum>18</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.259e+00</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.259</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.4785e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.4785</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>7.47e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>7.47</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>2.432e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.432</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.00e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.006e-01</number>
    <property>Solubility coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.006</significand>
    <unit>1</unit>
   </data>
   <pntnum>19</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.394e+00</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>1.394</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>An improved apparatus for solvent pretreatment was used [1]. The gas content in the solution was analyzed with a gas burette. The solvent was equilibrated by flowing a liquid film through the gas. No supersaturation was observed.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Morrison, T. J.; Billett, F., J. Chem. Soc. 1948, 2033-8.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1039/jr9480002033</url>
 </reference>
 <sources>
  <citation>Morrison, T. J.; Billett, F.; J. Chem. Soc. 1952, 3819-3822.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1039/jr9520003819</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>Prepare from marble.&lt;br/&gt;The system was sealed to prevent contamination with air.</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>Pure. Degassed.</sample>
 </substances>
 <system>Carbon dioxide with Water</system>
 <title>Solubility data from IUPAC SDS Volume 62 (page ?) - Carbon dioxide with Water</title>
</compilation>