<compilation>
 <compilers>William E. Acree, Jr.</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>2.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>2.77e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>2.77</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.97e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.97</significand>
    <unit>1</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>4.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>4.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>5.23e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>5.23</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.95e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.95</significand>
    <unit>1</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>1</exponent>
    <number>6.00e+01</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>6.00</significand>
    <unit>&amp;deg;C</unit>
   </conditions>
   <data>
    <exponent>-3</exponent>
    <number>9.12e-03</number>
    <property>Mole fraction - Liquid (1)</property>
    <sigfigs>3</sigfigs>
    <significand>9.12</significand>
    <unit>1</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>9.91e-01</number>
    <property>Mole fraction - Liquid (2)</property>
    <sigfigs>3</sigfigs>
    <significand>9.91</significand>
    <unit>1</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Constant temperature bath, thermometer, and a precision balance. Excess solute and solvent placed in closed glass container and allowed to equilibrate for several hours at constnat temperature. Aliquots of saturated solutions were transferred into tared containers and weighed. Solubilities calculated from weight of solid residue that remained after solvent had evaporated.</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <sources>
  <citation>Smutek, M.; Friš, M.; Fohl, J.; Collect. Czech. Chem. Commun. 1967, 32, 931-943.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1135/cccc19670931</url>
 </sources>
 <substances>
  <casrn>86-74-8</casrn>
  <constituent>1</constituent>
  <formula>C12H9N</formula>
  <inchi>InChI=1S/C12H9N/c1-3-7-11-9(5-1)10-6-2-4-8-12(10)13-11/h1-8,13H</inchi>
  <inchikey>UJOBWOGCFQCDNV-UHFFFAOYSA-N</inchikey>
  <molweight>167.207</molweight>
  <name>Carbazole</name>
  <sample>Coal tar extract, was recrystallized several times from toluene and pyridine, and then sublimed to give a final purity of 98.3%.</sample>
 </substances>
 <substances>
  <casrn>67-63-0</casrn>
  <constituent>2</constituent>
  <formula>C3H8O</formula>
  <inchi>InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3</inchi>
  <inchikey>KFZMGEQAYNKOFK-UHFFFAOYSA-N</inchikey>
  <molweight>60.095</molweight>
  <name>2-Propanol</name>
  <sample>99%, Commercial sample, source and purification method was not specified.</sample>
 </substances>
 <system>Carbazole with 2-Propanol</system>
 <title>Solubility data from IUPAC SDS Volume 58 (page 272) - Carbazole with 2-Propanol</title>
</compilation>