<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>4.64e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>4.64</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.536e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.536</significand>
    <unit>1</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>4.90e+02</number>
    <property>Ambient pressure</property>
    <sigfigs>3</sigfigs>
    <significand>4.90</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>3.81e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>3.81</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.619e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.619</significand>
    <unit>1</unit>
   </data>
   <pntnum>2</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>2.84e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.84</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.716e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.716</significand>
    <unit>1</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>1.960e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>1.960</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.97e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.97</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.803e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.803</significand>
    <unit>1</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>3.850e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>3.850</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>1.20e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.20</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.880e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.880</significand>
    <unit>1</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>3</exponent>
    <number>5.200e+03</number>
    <property>Ambient pressure</property>
    <sigfigs>4</sigfigs>
    <significand>5.200</significand>
    <unit>$\pu{atm}$</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>8.8e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>8.8</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.912e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>4</sigfigs>
    <significand>9.912</significand>
    <unit>1</unit>
   </data>
   <pntnum>6</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>111-65-9</casrn>
  <constituent>2</constituent>
  <formula>C8H18</formula>
  <inchi>InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3</inchi>
  <inchikey>TVMXDCGIABBOFY-UHFFFAOYSA-N</inchikey>
  <molweight>114.229</molweight>
  <name>Octane</name>
  <sample>Pure grade, Phillips Petroleum, was dried over phosphorous pentoxide and distilled.</sample>
 </substances>
 <system>Phenanthrene with n-Octane</system>
 <title>Solubility data from IUPAC SDS Volume 59 (page ?) - Phenanthrene with n-Octane</title>
</compilation>