<compilation>
 <compilers>Rosa Crovetto</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9485e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9485</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.17e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.17</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.461e-01</number>
    <property>Mole fraction - Vapor (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.461</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-4</exponent>
    <number>1.000e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.000</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.35e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.35</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.63e-01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>3</sigfigs>
    <significand>1.63</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9365e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9365</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.05e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.05</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.514e-01</number>
    <property>Mole fraction - Vapor (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.514</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-4</exponent>
    <number>1.261e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.261</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.51e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.51</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.77e-01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>3</sigfigs>
    <significand>1.77</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9145e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9145</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>1.83e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.83</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.230e-01</number>
    <property>Mole fraction - Vapor (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.230</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-5</exponent>
    <number>9.930e-05</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>9.930</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.23e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.23</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.45e-01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>3</sigfigs>
    <significand>1.45</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9485e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9485</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.17e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.17</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.569e-01</number>
    <property>Mole fraction - Vapor (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.569</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-4</exponent>
    <number>1.045e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.045</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.52e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.52</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.80e-01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>3</sigfigs>
    <significand>1.80</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9505e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9505</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.19e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.19</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.490e-01</number>
    <property>Mole fraction - Vapor (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.490</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-4</exponent>
    <number>1.172e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.172</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.48e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.48</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.76e-01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>3</sigfigs>
    <significand>1.76</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9425e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9425</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.11e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.11</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.781e-01</number>
    <property>Mole fraction - Vapor (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.781</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-4</exponent>
    <number>1.263e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.263</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.74e-01</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>1.74</significand>
    <unit>$\pu{atm}$</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>2.02e-01</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>3</sigfigs>
    <significand>2.02</significand>
    <unit>$\pu{bar}$</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Equilibration was obtained by flowing the gas through a column of water packed with Raschig rings.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Koch, H. A.; Stutzman, L. F.; Blum, H. A.; Hutchings, L. E.; Chem. Eng. Prog. 1949, 45(11), 677-82.</citation>
  <pubtype>paper</pubtype>
 </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>Not stated.</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>Distilled.</sample>
 </substances>
 <system>Carbon dioxide with Water</system>
 <title>Solubility data from IUPAC SDS Volume 62 (page ?) - Carbon dioxide with Water</title>
</compilation>