<compilation>
 <compilers>Ari L. Horvath</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.51e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.51</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-2</exponent>
    <number>6.93e-02</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>3</sigfigs>
    <significand>6.93</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>1.471e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.471</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>3</exponent>
    <number>3.920e+03</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>3.920</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>5.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>5.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>2.696e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>2.696</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>5.731e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>5.731</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>3</exponent>
    <number>2.480e+03</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>2.480</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>7.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>7.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>7.419e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>7.419</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>1.583e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.583</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>3</exponent>
    <number>1.650e+03</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.650</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>9.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>9.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>4</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>1.6652e+00</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>5</sigfigs>
    <significand>1.6652</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>3.579e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>3.579</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>3</exponent>
    <number>1.240e+03</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.240</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>9.60e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>9.60</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>5</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>2.1071e+00</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>5</sigfigs>
    <significand>2.1071</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>4.545e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>4.545</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>3</exponent>
    <number>1.130e+03</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.130</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>1.00e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>1.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data></data>
   <pntnum>6</pntnum>
   <supplemental>
    <exponent>0</exponent>
    <number>2.4173e+00</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>5</sigfigs>
    <significand>2.4173</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-3</exponent>
    <number>5.227e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>5.227</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>3</exponent>
    <number>1.080e+03</number>
    <property>Distribution Coefficient (gas/liquid)</property>
    <sigfigs>4</sigfigs>
    <significand>1.080</significand>
    <unit>1</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The distribution coefficient was determined by distillation. An inert gas was used to take samples from the vapor phase at equilibrium. The concentration of dichloromethane in both liquid and vapor phases was determined by using $\ce{^{36}Cl}$ labeled compound.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Prosyanov, N. N.; Shalygin, V. A.; Zel'venskii, Ya. D.; Tr. Mosk. Khim. Tekhnol. Inst. 1973, 100.</citation>
  <pubtype>paper</pubtype>
 </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 (compiler).</sample>
 </substances>
 <substances>
  <casrn>75-09-2</casrn>
  <constituent>1</constituent>
  <formula>CH2Cl2</formula>
  <inchi>InChI=1S/CH2Cl2/c2-1-3/h1H2</inchi>
  <inchikey>YMWUJEATGCHHMB-UHFFFAOYSA-N</inchikey>
  <molweight>84.9326</molweight>
  <name>Dichloromethane</name>
  <sample>Source and purity not given.</sample>
 </substances>
 <system>Dichloromethane with Water</system>
 <title>Solubility data from IUPAC SDS Volume 60 (page ?) - Dichloromethane with Water</title>
</compilation>