<compilation>
 <compilers>Robert W. Cargill</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.8815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.8815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>1.5e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>1.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>8.19e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>8.19</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.075e+00</number>
    <property>Ostwald coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.075</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.237e+02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.237</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>7.07e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>7.07</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.43e-01</number>
    <property>Ostwald coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>9.43</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.433e+02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.433</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></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>-4</exponent>
    <number>6.12e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>6.12</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>8.29e-01</number>
    <property>Ostwald coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>8.29</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.655e+02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.655</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <conditions>
    <exponent>1</exponent>
    <number>3.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-4</exponent>
    <number>5.37e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.37</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>7.38e-01</number>
    <property>Ostwald coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>7.38</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>1.888e+02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>1.888</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></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>-4</exponent>
    <number>4.79e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.79</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>6.68e-01</number>
    <property>Ostwald coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.68</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>2.117e+02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.117</significand>
    <unit>$\pu{MPa}$</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Known volumes of gas and solvent were introduced into 250 mL flask, then initial and final pressures were measured by a transducer connected to a digital multimeter. The flask was submerged in a thermostatic bath. Full details given in [1].</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Postigo, M. A.; Pedrosa, G. C.; Katz, M.; Anal. Asoc. Quim. Argentina 1978, 66, 25.</citation>
  <pubtype>paper</pubtype>
 </reference>
 <sources>
  <citation>Postigo, M. A.; Katz, M.; J. Solution Chem. 1987, 16, 1015-24.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1007/bf00652585</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: no information</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>Water: degassed by boiling; composition checked by refractive index measurement at 298 K.</sample>
 </substances>
 <system>Carbon dioxide with Water</system>
 <title>Solubility data from IUPAC SDS Volume 62 (page ?) - Carbon dioxide with Water</title>
</compilation>