<compilation>
 <compilers>Valerii P. Sazonov</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.000e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>5.000</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>7.89e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>7.89</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.52e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>1.52</significand>
    <unit>1</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>7.02e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>7.02</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>2.13e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>2.13</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.000e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>5.000</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>5.29e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.29</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.86e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>3.86</significand>
    <unit>1</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.15e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.15</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.77e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>4.77</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.000e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>5.000</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>2.80e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.80</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>6.09e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>6.09</significand>
    <unit>1</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.98e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.98</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>6.76e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>6.76</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.000e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>5.000</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>7.0e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>7.0</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>2.0e-02</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</significand>
    <unit>1</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>4.5e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>2</sigfigs>
    <significand>4.5</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-2</exponent>
    <number>2.0e-02</number>
    <property>Mass fraction (2)</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.000e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>5.000</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>5.6e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>5.6</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>5.1e-02</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>2</sigfigs>
    <significand>5.1</significand>
    <unit>1</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>3.6e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>2</sigfigs>
    <significand>3.6</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-2</exponent>
    <number>5.1e-02</number>
    <property>Mass fraction (2)</property>
    <sigfigs>2</sigfigs>
    <significand>5.1</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.000e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>5.000</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>2</exponent>
    <number>3.2315e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2315</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>3.7e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>3.7</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>8.9e-02</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>2</sigfigs>
    <significand>8.9</significand>
    <unit>1</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>2.3e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>2</sigfigs>
    <significand>2.3</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-2</exponent>
    <number>8.9e-02</number>
    <property>Mass fraction (2)</property>
    <sigfigs>2</sigfigs>
    <significand>8.9</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
  <title>Compositions of the equilibrium of two liquid phases in the ternary system</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The analytical method was used. The equilibrium cell consisted of a vertical glass cylinder with a volume of about 80 mL. A magnetic stir bar was used for mixing the sample, and the cell was thermostated. The two partially miscible components were charged to the equilibrium cell in approximately equal volumes, and the mixture was stirred for a minimum of 15 min. Next, the third component, which distributes itself between the two phases, was added to the equilibrium cell, stirred, and allowed to equilibrate before sampling. Samples of each phase were taken and analyzed by gas chromatography.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Lafyatis, D. S.; Scott, L. S.; Trampe, D. M.; Eckert, C. A.; Ind. Eng. Chem. Res. 28, 585-90 (1989).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/ie00089a014</url>
 </sources>
 <substances>
  <casrn>75-52-5</casrn>
  <constituent>1</constituent>
  <formula>CH3NO2 </formula>
  <inchi>InChI=1S/CH3NO2/c1-2(3)4/h1H3</inchi>
  <inchikey>LYGJENNIWJXYER-UHFFFAOYSA-N</inchikey>
  <molweight>61.04</molweight>
  <name>Nitromethane</name>
  <sample>Source not specified; purity greater than 99.9 mole%; not purified.</sample>
 </substances>
 <substances>
  <casrn>98-01-1</casrn>
  <constituent>2</constituent>
  <formula>C5H4O2</formula>
  <inchi>InChI=1S/C5H4O2/c6-4-5-2-1-3-7-5/h1-4H</inchi>
  <inchikey>HYBBIBNJHNGZAN-UHFFFAOYSA-N</inchikey>
  <molweight>96.0841</molweight>
  <name>2-Furancarboxaldehyde</name>
  <sample>Source not specified, purity greater than 99.9 mole%; not purified.</sample>
 </substances>
 <substances>
  <casrn>108-87-2</casrn>
  <constituent>3</constituent>
  <formula>C7H14</formula>
  <inchi>InChI=1S/C7H14/c1-7-5-3-2-4-6-7/h7H,2-6H2,1H3</inchi>
  <inchikey>UAEPNZWRGJTJPN-UHFFFAOYSA-N</inchikey>
  <molweight>98.1861</molweight>
  <name>Methylcyclohexane</name>
  <sample>Source not specified, purity greater than 99.9 mole%; not purified.</sample>
 </substances>
 <system>Nitromethane with 2-Furancarboxoaldehyde and Methylcyclohexane</system>
 <title>Solubility data from IUPAC SDS Volume 72 (page ?) - Nitromethane with 2-Furancarboxoaldehyde and Methylcyclohexane</title>
</compilation>