<compilation>
 <compilers>Nikolai I. Lisov, Valerii P. Sazonov</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>0e+00</number>
    <property>Ambient temperature</property>
    <sigfigs>0</sigfigs>
    <significand>0.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.732e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.732</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>1.4e+00</number>
    <property>Relative mass - solution (2)</property>
    <sigfigs>2</sigfigs>
    <significand>1.4</significand>
    <unit>g&lt;sub&gt;2&lt;/sub&gt;/100 g&lt;sub&gt;1&lt;/sub&gt;</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.4e+00</number>
    <property>Percent mass fraction (2)</property>
    <sigfigs>2</sigfigs>
    <significand>1.4</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>5e-03</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>1</sigfigs>
    <significand>5</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.832e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.832</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>2.1e+00</number>
    <property>Relative mass - solution (2)</property>
    <sigfigs>2</sigfigs>
    <significand>2.1</significand>
    <unit>g&lt;sub&gt;2&lt;/sub&gt;/100 g&lt;sub&gt;1&lt;/sub&gt;</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>2.1e+00</number>
    <property>Percent mass fraction (2)</property>
    <sigfigs>2</sigfigs>
    <significand>2.1</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>7e-03</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>1</sigfigs>
    <significand>7</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>2.932e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.932</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>0</exponent>
    <number>4.5e+00</number>
    <property>Relative mass - solution (2)</property>
    <sigfigs>2</sigfigs>
    <significand>4.5</significand>
    <unit>g&lt;sub&gt;2&lt;/sub&gt;/100 g&lt;sub&gt;1&lt;/sub&gt;</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>4.3e+00</number>
    <property>Percent mass fraction (2)</property>
    <sigfigs>2</sigfigs>
    <significand>4.3</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-2</exponent>
    <number>1.6e-02</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>2</sigfigs>
    <significand>1.6</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>3.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.032e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.032</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>1</exponent>
    <number>1.73e+01</number>
    <property>Relative mass - solution (2)</property>
    <sigfigs>3</sigfigs>
    <significand>1.73</significand>
    <unit>g&lt;sub&gt;2&lt;/sub&gt;/100 g&lt;sub&gt;1&lt;/sub&gt;</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>1.48e+01</number>
    <property>Percent mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>1.48</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-2</exponent>
    <number>5.7e-02</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>2</sigfigs>
    <significand>5.7</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>4.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>4.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.132e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>3.132</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>3</exponent>
    <number>9e+03</number>
    <property>Relative mass - solution (2)</property>
    <sigfigs>1</sigfigs>
    <significand>9</significand>
    <unit>g&lt;sub&gt;2&lt;/sub&gt;/100 g&lt;sub&gt;1&lt;/sub&gt;</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>9.89e+01</number>
    <property>Percent mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.89</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>9.69e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.69</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
  <title>Solubility of tridecanoic acid (2) in nitroethane (1)</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The synthetic method, as described in Hoerr, et al. [1], was used. No details were reported.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Pool, W. O.; Ralston, A. W.; Ind. Eng. Chem. 34, 1104 (1942).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/ie50393a019</url>
 </reference>
 <sources>
  <citation>Hoerr, C. W.; Ralston, A. W.; J. Org. Chem. 9, 329-37 (1944).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/jo01186a005</url>
 </sources>
 <substances>
  <casrn>79-24-3</casrn>
  <constituent>1</constituent>
  <formula>C2H5NO2</formula>
  <inchi>InChI=1S/C2H5NO2/c1-2-3(4)5/h2H2,1H3</inchi>
  <inchikey>MCSAJNNLRCFZED-UHFFFAOYSA-N</inchikey>
  <molweight>75.0666</molweight>
  <name>Nitroethane</name>
  <sample>Source not specified; purity not specified; dried and twice distilled.</sample>
 </substances>
 <substances>
  <casrn>638-53-9</casrn>
  <constituent>2</constituent>
  <formula>C13H26O2</formula>
  <inchi>InChI=1S/C13H26O2/c1-2-3-4-5-6-7-8-9-10-11-12-13(14)15/h2-12H2,1H3,(H,14,15)</inchi>
  <inchikey>SZHOJFHSIKHZHA-UHFFFAOYSA-N</inchikey>
  <molweight>214.344</molweight>
  <name>Tridecanoic acid</name>
  <sample>Source not specified; purified according to Pool and Ralston [2], FP = 41.76&amp;deg;C.</sample>
 </substances>
 <system>Nitroethane with Tridecanoic acid</system>
 <title>Solubility data from IUPAC SDS Volume 77 (page ?) - Nitroethane with Tridecanoic acid</title>
</compilation>