<compilation>
 <compilers>William E. Acree, Jr.</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>1e+00</number>
    <property>Ambient pressure</property>
    <sigfigs>1</sigfigs>
    <significand>1</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>4.01e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.01</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.599e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.599</significand>
    <unit>1</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>5.00e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>5.00</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>3.21e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.21</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.679e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.679</significand>
    <unit>1</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>9.00e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>9.00</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.92e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.92</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.708e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.708</significand>
    <unit>1</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>1.000e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>1.000</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>2.72e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.72</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.728e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.728</significand>
    <unit>1</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>2.000e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>2.000</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.84e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.84</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.816e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.816</significand>
    <unit>1</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>3.430e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>3.430</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.11e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.11</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.889e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.889</significand>
    <unit>1</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>5.000e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>5.000</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>8.4e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>8.4</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.916e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.916</significand>
    <unit>1</unit>
   </data>
   <pntnum>7</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>7.000e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>7.000</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>5.2e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>5.2</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.948e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.948</significand>
    <unit>1</unit>
   </data>
   <pntnum>8</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Constant temperature bath, analytical balance and high pressure equipment.&lt;br&gt;Excess solute and solvent allowed to equilibrate in a specially designed high pressure cell at constant temperature for 20-24 hours. Known amount of saturated solution removed, solvent evaporated to dryness, and concentration determined from weight of solid residue.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Doane, E. P.; Drickamer, H. G.; J. Phys. Chem. 1955, 59, 454-457.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/j150527a018</url>
 </sources>
 <substances>
  <casrn>85-01-8</casrn>
  <constituent>1</constituent>
  <formula>C14H10</formula>
  <inchi>InChI=1S/C14H10/c1-3-7-13-11(5-1)9-10-12-6-2-4-8-14(12)13/h1-10H</inchi>
  <inchikey>YNPNZTXNASCQKK-UHFFFAOYSA-N</inchikey>
  <molweight>178.229</molweight>
  <name>Phenanthrene</name>
  <sample>Purest grade, Eastman Kodak Chemical Company, Rochester, New York, USA, was used as received.</sample>
 </substances>
 <substances>
  <casrn>142-82-5</casrn>
  <constituent>2</constituent>
  <formula>C7H16</formula>
  <inchi>InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3</inchi>
  <inchikey>IMNFDUFMRHMDMM-UHFFFAOYSA-N</inchikey>
  <molweight>100.202</molweight>
  <name>Heptane</name>
  <sample>Pure grade, Phillips Petroleum, was dried over phosphorous pentoxide and distilled.</sample>
 </substances>
 <system>Phenanthrene with n-Heptane</system>
 <title>Solubility data from IUPAC SDS Volume 59 (page ?) - Phenanthrene with n-Heptane</title>
</compilation>