<compilation>
 <compilers>Ari L. Horvath</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>1.9e+00</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>1.9</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>8.251e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>8.251</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.254e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.254</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>6.89e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>3</sigfigs>
    <significand>6.89</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.35e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.35</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>7.846e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>7.846</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.192e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.192</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>2</exponent>
    <number>1.287e+02</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.287</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.57e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.57</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>7.565e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>7.565</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.149e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.149</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>2</exponent>
    <number>1.467e+02</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.467</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.71e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.71</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>7.676e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>7.676</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.166e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.166</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>2</exponent>
    <number>1.550e+02</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.550</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.20e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.20</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>7.669e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>7.669</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.165e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.165</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>2</exponent>
    <number>1.945e+02</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.945</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.49e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.49</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>8.297e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>8.297</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.261e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.261</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>2</exponent>
    <number>2.048e+02</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>2.048</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>A 5 µL trichloromethane sample was injected into a 2.3 L equilibration cell containing distilled water. After the cell was shaken vigorously for about 5 minutes, the homogeneity of the liquid sample was maintained with a magnetic stirrer. Compressed air was passed through the cell and the gas flow was measured with a soap film flowmeter. The trichloromethane content was extracted and analyzed using a dual flame ionization detector gas chromatograph.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Leighton, D. T.; Calo, J. M.; J. Chem. Eng. Data 1981, 26, 382-5.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1021/je00026a010</url>
 </sources>
 <substances>
  <casrn>67-66-3</casrn>
  <constituent>1</constituent>
  <formula>CHCl3</formula>
  <inchi>InChI=1S/CHCl3/c2-1(3)4/h1H</inchi>
  <inchikey>HEDRZPFGACZZDS-UHFFFAOYSA-N</inchikey>
  <molweight>119.378</molweight>
  <name>Trichloromethane</name>
  <sample>Source and purity not given.</sample>
 </substances>
 <substances>
  <casrn>7732-18-5</casrn>
  <constituent>2</constituent>
  <formula>H2O</formula>
  <inchi>InChI=1S/H2O/h1H2</inchi>
  <inchikey>XLYOFNOQVPJJNP-UHFFFAOYSA-N</inchikey>
  <molweight>18.0153</molweight>
  <name>Water</name>
  <sample>Distilled.</sample>
 </substances>
 <system>Trichloromethane with Water</system>
 <title>Solubility data from IUPAC SDS Volume 60 (page ?) - Trichloromethane with Water</title>
</compilation>