<compilation>
 <compilers>Ari L. Horvath</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>1.0e+00</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>1.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>5.256e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>5.256</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>9.610e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>9.610</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>3.062e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>3.062</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>0</exponent>
    <number>1.3e+00</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>1.3</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>5.363e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>5.363</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>9.807e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>9.807</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>3.089e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>3.089</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.10e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.10</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>6.032e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>6.032</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.1035e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>1.1035</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>4.656e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>4.656</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.10e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.10</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>6.801e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>6.801</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.2451e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>1.2451</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>6.889e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>6.889</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>6.426e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>6.426</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.1761e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>1.1761</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>7.659e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>7.659</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.72e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.72</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>6.548e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>6.548</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.1985e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>5</sigfigs>
    <significand>1.1985</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>1</exponent>
    <number>9.546e+01</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>9.546</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>A 5 μL 1,2-dichloroethane 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-dichloroethane 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>107-06-2</casrn>
  <constituent>1</constituent>
  <formula>C2H4Cl2</formula>
  <inchi>InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2</inchi>
  <inchikey>WSLDOOZREJYCGB-UHFFFAOYSA-N</inchikey>
  <molweight>98.9592</molweight>
  <name>1,2-Dichloroethane</name>
  <sample>Source and purity not given.</sample>
 </substances>
 <system>1,2-Dichloroethane with Water</system>
 <title>Solubility data from IUPAC SDS Volume 67 (page 604) - 1,2-Dichloroethane with Water</title>
</compilation>