<compilation>
 <compilers>Rosa Crovetto</compilers>
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    <property>Pressure (Compiler)</property>
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    <property>Ambient temperature</property>
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    <property>Pressure (Compiler)</property>
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    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <exponent>2</exponent>
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    <property>Pressure (Compiler)</property>
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    <significand>1.520</significand>
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    <number>3.4815e+02</number>
    <property>Ambient temperature</property>
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    <significand>3.4815</significand>
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    <property>Ambient temperature</property>
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   <data>
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   <data>
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    <exponent>2</exponent>
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    <property>Pressure (Compiler)</property>
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    <significand>2.026</significand>
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    <number>3.4815e+02</number>
    <property>Ambient temperature</property>
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    <significand>3.4815</significand>
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    <number>7.5e+01</number>
    <property>Ambient temperature</property>
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    <significand>7.5</significand>
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    <property>Pressure (Compiler)</property>
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    <number>3.4815e+02</number>
    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <unit>atm</unit>
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   <data>
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    <property>Pressure (Compiler)</property>
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    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <property>Pressure (Compiler)</property>
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    <property>Pressure (Compiler)</property>
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    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <property>Ambient temperature</property>
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    <property>Pressure (Compiler)</property>
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    <property>Ambient temperature</property>
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  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.7315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.7315</significand>
    <unit>K</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>1.00e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.554e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.554</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>4e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>4</significand>
    <unit>atm</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.239e+01</number>
    <property>Solubility coefficient </property>
    <sigfigs>4</sigfigs>
    <significand>3.239</significand>
    <unit>cm&lt;sup&gt;3&lt;/sup&gt; (1)/g (2)</unit>
   </data>
   <pntnum>28</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>4.053e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>4.053</significand>
    <unit>bar</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.7315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.7315</significand>
    <unit>K</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>1.00e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>3.022e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>3.022</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>2</exponent>
    <number>7e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>7</significand>
    <unit>atm</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>3.850e+01</number>
    <property>Solubility coefficient </property>
    <sigfigs>4</sigfigs>
    <significand>3.850</significand>
    <unit>cm&lt;sup&gt;3&lt;/sup&gt; (1)/g (2)</unit>
   </data>
   <pntnum>29</pntnum>
   <supplemental>
    <exponent>2</exponent>
    <number>7.093e+02</number>
    <property>Pressure (Compiler)</property>
    <sigfigs>4</sigfigs>
    <significand>7.093</significand>
    <unit>bar</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>A high-pressure autoclave was used. Two flasks helped to maintain pressure constant during sampling. Pressure was read on a dead weight gauge. The liquid sample was analyzed for its CO&lt;sub&gt;2&lt;/sub&gt; content by expansion into a thermostatted gas buret.&lt;br/&gt;It was not stated if stirring was used.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <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>
 </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>Purity 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>