<compilation>
 <compilers>Adam Skrzecz</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</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>-1</exponent>
    <number>2.29e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.29</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>7.62e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>7.62</significand>
    <unit>1</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.02e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.02</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>8.95e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.95</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</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>-1</exponent>
    <number>3.92e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.92</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>5.93e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>5.93</significand>
    <unit>1</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>2.00e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.00</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>7.95e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>7.95</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</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>-1</exponent>
    <number>5.13e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.13</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.65e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>4.65</significand>
    <unit>1</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>2.94e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.94</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>6.99e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>6.99</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</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>-1</exponent>
    <number>6.14e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>6.14</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.57e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>3.57</significand>
    <unit>1</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>3.92e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.92</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>5.98e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>5.98</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</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>-1</exponent>
    <number>6.90e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>6.90</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.75e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>2.75</significand>
    <unit>1</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.82e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.82</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>5.04e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>5.04</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</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>-1</exponent>
    <number>7.46e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>7.46</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.03e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>2.03</significand>
    <unit>1</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>5.70e-01</number>
    <property>Mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.70</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.08e-01</number>
    <property>Mass fraction (2)</property>
    <sigfigs>3</sigfigs>
    <significand>4.08</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
  <title>Compositions along the saturation curve</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The titration method was used to determine binodal curve. The synthetic method was used to determine phase equilibra. The mole fraction of hydrocarbon in the charge before separation was about 0.30. After separation phases were analyzed by GLC to determine methanol and hydrocarbon; concentration of water was determined by Karl Fischer method.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Budantseva, L. S.; Lesteva, T. M.; Nemstov, M. S.; Zh. Fiz. Khim. 1976, 50, 1344.</citation>
  <pubtype>paper</pubtype>
 </sources>
 <substances>
  <casrn>67-56-1</casrn>
  <constituent>1</constituent>
  <formula>CH4O</formula>
  <inchi>InChI=1S/CH4O/c1-2/h2H,1H3</inchi>
  <inchikey>OKKJLVBELUTLKV-UHFFFAOYSA-N</inchikey>
  <molweight>32.0419</molweight>
  <name>Methanol</name>
  <sample>Source not specified.</sample>
 </substances>
 <substances>
  <casrn>592-41-6</casrn>
  <constituent>2</constituent>
  <formula>C6H12</formula>
  <inchi>InChI=1S/C6H12/c1-3-5-6-4-2/h3H,1,4-6H2,2H3</inchi>
  <inchikey>LIKMAJRDDDTEIG-UHFFFAOYSA-N</inchikey>
  <molweight>84.1595</molweight>
  <name>1-Hexene</name>
  <sample>Source not specified; distilled; purity &gt;99.9%.</sample>
 </substances>
 <substances>
  <casrn>7732-18-5</casrn>
  <constituent>3</constituent>
  <formula>H2O</formula>
  <inchi>InChI=1S/H2O/h1H2</inchi>
  <inchikey>XLYOFNOQVPJJNP-UHFFFAOYSA-N</inchikey>
  <molweight>18.0153</molweight>
  <name>Water</name>
  <sample>Source not specified.</sample>
 </substances>
 <system>Methanol with 1-Hexene and Water</system>
 <title>Solubility data from IUPAC SDS Volume 69 (page ?) - Methanol with 1-Hexene and Water</title>
</compilation>