<compilation>
 <compilers>Pirketta Scharlin, Xiaohui Shen</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.7815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.7815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>6.11e-02</number>
    <property>Solubility coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.11</significand>
    <unit>mol/kg</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <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>
   <data>
    <exponent>-2</exponent>
    <number>4.29e-02</number>
    <property>Solubility coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.29</significand>
    <unit>mol/kg</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>
   <data>
    <exponent>-2</exponent>
    <number>3.13e-02</number>
    <property>Solubility coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.13</significand>
    <unit>mol/kg</unit>
   </data>
   <pntnum>3</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>
   <data>
    <exponent>-2</exponent>
    <number>2.56e-02</number>
    <property>Solubility coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.56</significand>
    <unit>mol/kg</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1815e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1815</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.10e-02</number>
    <property>Solubility coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.10</significand>
    <unit>mol/kg</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Table 1. Solubility of CO&lt;sub&gt;2&lt;/sub&gt; in water</title>
 </dataset>
 <dataset>
  <points>
   <conditions></conditions>
   <data>
    <exponent>3</exponent>
    <number>4.6088e+03</number>
    <property>Equation Coefficient (First)</property>
    <sigfigs>5</sigfigs>
    <significand>4.6088</significand>
    <unit>$\pu{K}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2e-01</number>
    <property>Error</property>
    <sigfigs>1</sigfigs>
    <significand>2</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>-2.8953e+01</number>
    <property>Equation Coefficient (Second)</property>
    <sigfigs>5</sigfigs>
    <significand>-2.8953</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>4.018e-02</number>
    <property>Equation Coefficient (Third)</property>
    <sigfigs>4</sigfigs>
    <significand>4.018</significand>
    <unit>$\pu{K-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <series>2</series>
  <title>Table 2. Coefficients of eq. (1) for smoothed results for solubility of CO&lt;sub&gt;2&lt;/sub&gt; in water</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Static-state method. The authors designed a solubility apparatus which is composed of three isothermal pre-saturators, saturator and sampler. A schematic diagram of the apparatus is in the original source. $\ce{CO2}$ was introduced (10 hours) through the pre-saturators and the saturator which contained about 120 g of solvent. The equilibrated sample (about 100 g) was transferred from the saturator into the weighed sampler which contained a weighed amount of standard $\ce{NaOH}$ solution. The sampler was weighed again and shaken to complete the reaction between $\ce{CO2}$ and $\ce{NaOH}$. The excess of $\ce{NaOH}$ and the $\ce{NaHCO3}$ was titrated potentiometrically with standard $\ce{HCl}$ solution. The mass of dissolved $\ce{CO2}$ was calculated from the equation: $$w = c_{\ce{HCl}}(V_{2} - V_{1})M$$ where $w$ = mass of dissolved $\ce{CO2}$, $c_{\ce{HCl}}$ = concentration of $\ce{HCl}$; $V_{1}$ and $V_{2}$ are volumes of the $\ce{HCl}$ solution to the first and second end point, respectively, and $M$ = molar mass of $\ce{CO2}$.&lt;br/&gt;(The authors also report solubilities of $\ce{CO2}$ in 15 mass % glucose/$\ce{H2O}$ and in $\ce{NaCl}$ + 15 mass % glucose/$\ce{H2O}$.)</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Yuan, C-B.; Yang, J-Z.; Gaodeng Xuexiao Huaxue Xuebao 1993, 14, 80-3.</citation>
  <pubtype>paper</pubtype>
  <url>http://www.cjcu.jlu.edu.cn/EN/Y1993/V14/I1/80</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 of $\ce{CO2}$ 99.95%.</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>Double deionized. Conductivity of $\ce{H2O}$ was $\pu{\lt 1.5E-4 S m-1}$.</sample>
 </substances>
 <system>Carbon dioxide with Water</system>
 <title>Solubility data from IUPAC SDS Volume 62 (page ?) - Carbon dioxide with Water</title>
</compilation>