<compilation>
 <compilers>Yuri P. Yampol'skii</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.08e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.08</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.50e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.50</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>6.72e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>6.72</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>3.17e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.17</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.08e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.08</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-2</exponent>
    <number>7.53e-02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>7.53</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>9.98e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>9.98</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>1.56e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.56</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.08e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.08</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>6.64e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.64</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.790e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>4</sigfigs>
    <significand>1.790</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.260e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.260</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.08e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.08</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>1.61e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.61</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>9.86e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>9.86</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>6.98e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.98</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Dual mode sorption parameters for various gases in "as-received" polysulfone films at 308 K</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Sorption apparatus and procedure are described in [1].</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Koros, W. J.; Chan, A. H.; Paul, D. R.; J. Membr. Sci. 2, 165 (1977).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1016/s0376-7388(00)83242-1</url>
 </reference>
 <sources>
  <citation>Erb, A. J.; Paul, D. R.; J. Membr. Sci. 8, 11 (1981).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1016/s0376-7388(00)82135-3</url>
 </sources>
 <sources>
  <citation>Chiou, J. S.; Maeda, Y.; Paul, D. R.; J. Appl. Polym. Sci. 33, 1823 (1987).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/app.1987.070330533</url>
 </sources>
 <substances>
  <casrn>25135-51-7</casrn>
  <constituent>2</constituent>
  <formula>(C27H26O6S)n</formula>
  <inchi>InChI=1S/C15H16O2.C12H10O4S/c1-15(2,11-3-7-13(16)8-4-11)12-5-9-14(17)10-6-12;13-9-1-5-11(6-2-9)17(15,16)12-7-3-10(14)4-8-12/h3-10,16-17H,1-2H3;1-8,13-14H</inchi>
  <inchikey>ZUZZUJNBGCVPLQ-UHFFFAOYSA-N</inchikey>
  <molweight>478.6</molweight>
  <name>Polysulfone (PSF)</name>
  <sample>Commercial PSF: Union Carbide Corp., studied in the form of melt extruded film; $T_{\rm{g}}$ = 455 K (DSC).</sample>
 </substances>
 <substances>
  <constituent>1</constituent>
  <formula>$\ce{Ar}$, $\ce{N2}$, $\ce{CO2}$ and $\ce{CH4}$</formula>
  <molweight>0.0</molweight>
  <name>Various gases (x4)</name>
 </substances>
 <system>Various gases (x4) and Polysulfone (PSF)</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Various gases (x4) and Polysulfone (PSF)</title>
</compilation>