<compilation>
 <compilers>Yuri P. Yampol'skii</compilers>
 <dataset>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>2.93e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>2.93</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>8.01e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>8.01</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>2.60e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>2.60</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.10e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.10</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>-1</exponent>
    <number>7.25e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>7.25</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.92e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.92</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.90e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.90</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.38e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.38</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>2.31e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.31</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.75e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.75</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.34e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.34</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>5.63e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>5.63</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.36e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.36</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.94e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.94</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>4</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>2.96e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.96</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.02e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.02</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.26e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.26</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>5</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>4.58e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.58</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>8.8e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>8.8</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.12e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.12</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>6</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>3.92e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.92</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.39e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.39</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.59e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.59</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>7</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>3.63e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.63</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>8.1e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>8.1</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.78e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.78</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>8</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>5.03e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>5.03</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.39e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.39</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.80e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.80</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>9</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>4.26e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.26</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.22e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.22</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.59e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.59</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>10</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>4.76e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.76</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>9.7e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>9.7</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.48e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.48</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>11</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>4.43e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.43</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>7.4e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>7.4</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.71e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.71</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>12</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Dual mode sorption parameters for carbon dioxide in polysulfone at different temperatures and its mixtures with plasticizers at 308 K</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The apparatus and procedure for measuring sorption isotherms were described in [1].</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Koros, W. J.; Paul, D. R.; Rocha, A. A.; J. Polym. Sci., Polym. Phys. Ed., 1976, 14, 687.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/pol.1976.180140410</url>
 </reference>
 <sources>
  <citation>Maeda, Y.; Paul, D. R.; J. Polym. Sci. B: Polym. Phys. 25, 957 (1987).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/polb.1987.090250501</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>124-38-9</casrn>
  <constituent>1</constituent>
  <formula>CO2</formula>
  <inchi>InChI=1S/CO2/c2-1-3</inchi>
  <inchikey>CURLTUGMZLYLDI-UHFFFAOYSA-N</inchikey>
  <molweight>44.0095</molweight>
  <name>Carbon dioxide</name>
  <sample>PSF: Union Carbide Corp., $T{\rm{g}}$ = 459 K.</sample>
 </substances>
 <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>
 </substances>
 <substances>
  <casrn>80-07-9</casrn>
  <constituent>3</constituent>
  <formula>C12H8C12O2S</formula>
  <inchi>InChI=1S/C12H8Cl2O2S/c13-9-1-5-11(6-2-9)17(15,16)12-7-3-10(14)4-8-12/h1-8H</inchi>
  <inchikey>GPAPPPVRLPGFEQ-UHFFFAOYSA-N</inchikey>
  <molweight>287.162</molweight>
  <name>4,4'-Dichlorodiphenyl sulfone</name>
 </substances>
 <substances>
  <casrn>135-88-6</casrn>
  <constituent>3</constituent>
  <formula>C16H13N</formula>
  <inchi>InChI=1S/C16H13N/c1-2-8-15(9-3-1)17-16-11-10-13-6-4-5-7-14(13)12-16/h1-12,17H</inchi>
  <inchikey>KEQFTVQCIQJIQW-UHFFFAOYSA-N</inchikey>
  <molweight>219.281</molweight>
  <name>N-phenyl-2-naphthylamine</name>
 </substances>
 <substances>
  <casrn>78-32-0</casrn>
  <constituent>3</constituent>
  <formula>C19H21O4P</formula>
  <inchi>InChI=1S/C21H21O4P/c1-16-4-10-19(11-5-16)23-26(22,24-20-12-6-17(2)7-13-20)25-21-14-8-18(3)9-15-21/h4-15H,1-3H3</inchi>
  <inchikey>BOSMZFBHAYFUBJ-UHFFFAOYSA-N</inchikey>
  <molweight>368.363</molweight>
  <name>Tricresyl phosphate</name>
 </substances>
 <system>Carbon dioxide with Polysulfone (PSF) and DDS, PNA, TCP </system>
 <title>Solubility data from IUPAC SDS Volume 70 (page 1376) - Carbon dioxide with Polysulfone (PSF) and DDS, PNA, TCP </title>
</compilation>