<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>0</exponent>
    <number>7.230e+00</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>7.230</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-5</exponent>
    <number>8.841e-05</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>8.841</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>1.166e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.166</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>1.651e+01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.651</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>2.021e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.021</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>1.146e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.146</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>1.596e+01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.596</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>1.953e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.953</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>1.355e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.355</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>1.683e+01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.683</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>2.060e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.060</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>1.418e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.418</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.2e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.2</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>1</exponent>
    <number>2.173e+01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.173</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>2.661e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.661</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>1.512e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.512</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>2.00e+01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.00</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>2.448e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.448</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>1.981e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.981</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>5 μL 1,2,3-trichloropropane 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 1,2,3-trichloropropane 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>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>
 <substances>
  <casrn>96-18-4</casrn>
  <constituent>1</constituent>
  <formula>C3H5Cl3</formula>
  <inchi>InChI=1S/C3H5Cl3/c4-1-3(6)2-5/h3H,1-2H2</inchi>
  <inchikey>CFXQEHVMCRXUSD-UHFFFAOYSA-N</inchikey>
  <molweight>147.431</molweight>
  <name>1,2,3-Trichloropropane</name>
  <sample>Source and purity not given.</sample>
 </substances>
 <system>1,2,3-Trichloropropane with Water</system>
 <title>Solubility data from IUPAC SDS Volume 68 (page ?) - 1,2,3-Trichloropropane with Water</title>
</compilation>