<compilation>
 <compilers>Ari L. Horvath</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>1.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>1.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>0</exponent>
    <number>1.30e+00</number>
    <property>Mass density</property>
    <sigfigs>3</sigfigs>
    <significand>1.30</significand>
    <unit>g/L</unit>
   </conditions>
   <data></data>
   <pntnum>1</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.300e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.300</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>1.758e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.758</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>3.55e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.55</significand>
    <unit>m&lt;sup&gt;3&lt;/sup&gt; atm mol&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>2.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>0</exponent>
    <number>1.29e+00</number>
    <property>Mass density</property>
    <sigfigs>3</sigfigs>
    <significand>1.29</significand>
    <unit>g/L</unit>
   </conditions>
   <data></data>
   <pntnum>2</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.290e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.290</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>1.744e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.744</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>5.59e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>5.59</significand>
    <unit>m&lt;sup&gt;3&lt;/sup&gt; atm mol&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>3.0e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>2</sigfigs>
    <significand>3.0</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <conditions>
    <exponent>0</exponent>
    <number>1.27e+00</number>
    <property>Mass density</property>
    <sigfigs>3</sigfigs>
    <significand>1.27</significand>
    <unit>g/L</unit>
   </conditions>
   <data></data>
   <pntnum>3</pntnum>
   <supplemental>
    <exponent>-1</exponent>
    <number>1.270e-01</number>
    <property>Percent mass fraction (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.270</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-4</exponent>
    <number>1.717e-04</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>4</sigfigs>
    <significand>1.717</significand>
    <unit>1</unit>
   </supplemental>
   <supplemental>
    <exponent>-1</exponent>
    <number>8.55e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>8.55</significand>
    <unit>m&lt;sup&gt;3&lt;/sup&gt; atm mol&lt;sup&gt;-1&lt;/sup&gt;</unit>
   </supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The multiple equilibrium technique with direct aqueous injection into a gas chromatograph was used to determine the dimensionless Henry's law constant. A known volume of liquid and gas was introduced into a syringe and allowed to equilibrate. The ratio of gas to liquid volume was maintained constant. While vapor samples were injected directly into a gas chromatograph, the liquid samples were preconcentrated by liquid-liquid extraction before analysis. The experimentswere carried out in duplicates.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Munz, C. D.; Ph.D. Dissertation, Stanford University, Stanford, CA 1985, 306 pp.</citation>
  <pubtype>thesis</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 and deionized.</sample>
 </substances>
 <substances>
  <casrn>71-55-6</casrn>
  <constituent>1</constituent>
  <formula>C2H3Cl3</formula>
  <inchi>InChI=1S/C2H3Cl3/c1-2(3,4)5/h1H3</inchi>
  <inchikey>UOCLXMDMGBRAIB-UHFFFAOYSA-N</inchikey>
  <molweight>133.404</molweight>
  <name>1,1,1-Trichloroethane</name>
  <sample>Matheson Coleman &amp; Bell, OH, greater than 99.5% purity.</sample>
 </substances>
 <system>1,1,1-Trichloroethane with Water</system>
 <title>Solubility data from IUPAC SDS Volume 67 (page 533) - 1,1,1-Trichloroethane with Water</title>
</compilation>