<compilation>
 <compilers>Valerii P. Sazonov</compilers>
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    <number>3.69e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.69</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>5.570e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>4</sigfigs>
    <significand>5.570</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.500e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.500</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <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>8.10e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>8.10</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.642e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>4.642</significand>
    <unit>1</unit>
   </data>
   <pntnum>15</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>3.80e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.80</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.859e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>4</sigfigs>
    <significand>4.859</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.500e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.500</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <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>8.45e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>8.45</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.533e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>3.533</significand>
    <unit>1</unit>
   </data>
   <pntnum>16</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>3.97e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.97</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>3.706e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>4</sigfigs>
    <significand>3.706</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.500e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.500</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <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>8.97e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>8.97</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.859e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>1.859</significand>
    <unit>1</unit>
   </data>
   <pntnum>17</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>4.23e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.23</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.956e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>4</sigfigs>
    <significand>1.956</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.500e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>4</sigfigs>
    <significand>2.500</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <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>8.87e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>8.87</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>8.85e-02</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.85</significand>
    <unit>1</unit>
   </data>
   <pntnum>18</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>4.18e-02</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.18</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-2</exponent>
    <number>9.31e-02</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.31</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
  <title>Compositions of liquid phases at equilibrium for the ternary system</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The analytical method was used. Liquid-liquid equilibrium was determined as described in Antosik [1]. The equilibrium cell of about 50 mL capacity, equipped with a magnetic stirrer, was sealed in a water jacket, and circulating water from a thermostat ensured temperature constancy. The three-component mixture was stirred in the equilibrium cell for about 30 min, then the mixture was left for about 1 h for complete phase separation, and samples of about 0.2 mL of each of the two phases were withdrawn from the equilibrium cell through a silicone-rubber septum using a syringe for gas chromatography analyses.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Antosik, M.; J. Chem. Thermodyn. 22, 85 (1990).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1016/0021-9614(90)90034-n</url>
 </reference>
 <sources>
  <citation>Antosik, M.; Stryjek, R.; Fluid Phase Equilib. 71, 321-331 (1992).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1016/0378-3812(92)80007-v</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 99.8 mass% by GLC; 0.025 mass% water by the Karl Fischer method.</sample>
 </substances>
 <substances>
  <casrn>7785-70-8</casrn>
  <constituent>2</constituent>
  <formula>C10H16</formula>
  <inchi>InChI=1S/C10H16/c1-7-4-5-8-6-9(7)10(8,2)3/h4,8-9H,5-6H2,1-3H3/t8-,9-/m1/s1</inchi>
  <inchikey>GRWFGVWFFZKLTI-RKDXNWHRSA-N</inchikey>
  <molweight>136.234</molweight>
  <name>(1R,5R)-2,6,6-Trimethylbicyclo[3.1.1]hept-2-ene</name>
  <sample>Isolated from turpentine and purified by fractional distillation at sub-ambient pressure; purity above 99.9 mass% by GLC.</sample>
 </substances>
 <substances>
  <casrn>13466-78-9</casrn>
  <constituent>3</constituent>
  <formula>C10H16</formula>
  <inchi>InChI=1S/C10H16/c1-7-4-5-8-9(6-7)10(8,2)3/h4,8-9H,5-6H2,1-3H3</inchi>
  <inchikey>BQOFWKZOCNGFEC-UHFFFAOYSA-N</inchikey>
  <molweight>136.234</molweight>
  <name>3,7,7-Trimethylbicyclo[4.1.0]hept-3-ene</name>
  <sample>Isolated from turpentine and purified by fractional distillation at sub-ambient pressure; purity above 99.9 mass% by GLC.</sample>
 </substances>
 <system>Nitromethane with 2,6,6-Trimethylbicyclo[3.1.1]hept-2-ene and 3,7,7-Trimethylbicyclo[4.1.0] hept-3-ene</system>
 <title>Solubility data from IUPAC SDS Volume 72 (page ?) - Nitromethane with 2,6,6-Trimethylbicyclo[3.1.1]hept-2-ene and 3,7,7-Trimethylbicyclo[4.1.0] hept-3-ene</title>
</compilation>