<compilation>
 <compilers>Ari L. Horvath</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>2.5e+00</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.5</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>3.705e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>3.705</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>5.0191e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>5.0191</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>1.667e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.667</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>7.0e+00</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>7.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>3.891e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>3.891</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>5.2719e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>5.2719</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>2.096e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>2.096</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.29e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.29</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.323e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>4.323</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>5.8595e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>5.8595</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>2.691e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>2.691</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.80e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.80</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.523e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>4.523</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>6.1327e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>6.1327</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>3.414e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>3.414</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.95e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.95</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.985e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>4.985</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>6.7619e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>6.7619</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>3.364e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>3.364</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.43e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.43</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.922e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>4.922</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>6.6761e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>6.6761</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>4.461e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>4.461</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.61e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.61</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>7</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>4.902e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>4.902</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>6.6486e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>6.6486</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>4.847e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>4.847</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>A 5 μL 1,1,2-trichloroethane 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 1,1,2-trichloroethane 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>79-00-5</casrn>
  <constituent>1</constituent>
  <formula>C2H3Cl3</formula>
  <inchi>InChI=1S/C2H3Cl3/c3-1-2(4)5/h2H,1H2</inchi>
  <inchikey>UBOXGVDOUJQMTN-UHFFFAOYSA-N</inchikey>
  <molweight>133.404</molweight>
  <name>1,1,2-Trichloroethane</name>
  <sample>Source and purity not given.</sample>
 </substances>
 <system>1,1,2-Trichloroethane with Water</system>
 <title>Solubility data from IUPAC SDS Volume 67 (page 546) - 1,1,2-Trichloroethane with Water</title>
</compilation>