<compilation>
 <compilers>William E. Acree, Jr.</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.8405e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.8405</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>3.8e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>3.8</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.62e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.62</significand>
    <unit>1</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.8905e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.8905</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>4.5e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>4.5</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.55e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.55</significand>
    <unit>1</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9195e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9195</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>5.0e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>5.0</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.50e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.50</significand>
    <unit>1</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9535e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9535</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>5.8e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>5.8</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.42e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.42</significand>
    <unit>1</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.9825e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>2.9825</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>6.6e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>6.6</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.34e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.34</significand>
    <unit>1</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0325e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0325</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>7.7e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>7.7</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.23e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.23</significand>
    <unit>1</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.0795e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.0795</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>9.1e-02</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>2</sigfigs>
    <significand>9.1</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.09e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.09</significand>
    <unit>1</unit>
   </data>
   <pntnum>7</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1345e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1345</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.13e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.13</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>8.87e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.87</significand>
    <unit>1</unit>
   </data>
   <pntnum>8</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1735e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1735</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.40e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.40</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>8.60e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.60</significand>
    <unit>1</unit>
   </data>
   <pntnum>9</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.1975e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.1975</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.56e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.56</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>8.44e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.44</significand>
    <unit>1</unit>
   </data>
   <pntnum>10</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.2355e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.2355</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.76e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>1.76</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>8.24e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>8.24</significand>
    <unit>1</unit>
   </data>
   <pntnum>11</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.3045e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>5</sigfigs>
    <significand>3.3045</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>2.28e-01</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.28</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>7.72e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>7.72</significand>
    <unit>1</unit>
   </data>
   <pntnum>12</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Constant temperature bath and a precision thermometer.&lt;br&gt;Solubilities were measured using a dynamic method. Mixtures of known concentrations were sealed in thick-walled glass ampoules and placed in a constant temperature to equilibrate. Bath temperature was slowly increased by 2 K per hour. Solubility determined by visually noting the temperature at which the last trace of solid solute disappeared.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Domanska, U.; Pol. J. Chem. 1981, 55, 1715-1720.</citation>
  <pubtype>paper</pubtype>
 </sources>
 <substances>
  <casrn>91-20-3</casrn>
  <constituent>1</constituent>
  <formula>C10H8</formula>
  <inchi>InChI=1S/C10H8/c1-2-6-10-8-4-3-7-9(10)5-1/h1-8H</inchi>
  <inchikey>UFWIBTONFRDIAS-UHFFFAOYSA-N</inchikey>
  <molweight>128.171</molweight>
  <name>Naphthalene</name>
  <sample>Purity not specified, P.O.Ch., Gliwice, Poland, was vacuum sublimed to a melting temperature of 80.25&amp;deg;C.</sample>
 </substances>
 <substances>
  <casrn>71-36-3</casrn>
  <constituent>2</constituent>
  <formula>C4H10O</formula>
  <inchi>InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3</inchi>
  <inchikey>LRHPLDYGYMQRHN-UHFFFAOYSA-N</inchikey>
  <molweight>74.1216</molweight>
  <name>1-Butanol</name>
  <sample>Initial purity not specified, P.O.Ch., was dried over sodium carbonate and fractionally distilled to a final purity of 99.9+%.</sample>
 </substances>
 <system>Naphthalene with 1-Butanol</system>
 <title>Solubility data from IUPAC SDS Volume 59 (page ?) - Naphthalene with 1-Butanol</title>
</compilation>