<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>5.96e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>5.96</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.20e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.20</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.78e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.78</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>1</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.23e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.23</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>4.56e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.56</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.03e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.03</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.48e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.48</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>2</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.53e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.53</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>3.35e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.35</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>5.9e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>5.9</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.52e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.52</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>3</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.83e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.83</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>2.54e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.54</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>3.4e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>3.4</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.62e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.62</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>4</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.23e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.23</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>6.09e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.09</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.79e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.79</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.92e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.92</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>5</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.53e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.53</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>4.49e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.49</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.06e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.06</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.36e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.36</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.53e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.53</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>3.16e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.16</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>1</exponent>
    <number>1.10e+01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>3</sigfigs>
    <significand>1.10</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.67e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.67</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>7</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.83e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.83</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>3.27e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.27</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>7.0e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>7.0</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>1.40e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.40</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>8</pntnum>
   <supplemental></supplemental>
  </points>
  <points>
   <conditions>
    <exponent>2</exponent>
    <number>3.53e+02</number>
    <property>Ambient temperature</property>
    <sigfigs>3</sigfigs>
    <significand>3.53</significand>
    <unit>$\pu{K}$</unit>
   </conditions>
   <data>
    <exponent>-1</exponent>
    <number>2.67e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.67</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.7e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>2</sigfigs>
    <significand>4.7</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.16e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>2.16</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>9</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Dual mode sorption parameters for CO2 in commercial and laboratory samples of BPDA-ODA polyimides</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>Apparatus and procedure of sorption measurement was similar to one described in [1].</method>
 <publisher>The International Union of Pure and Applied Chemistry</publisher>
 <reference>
  <citation>Koros, W. J.; Paul, D. R.; J. Polym. Sci., Polym. Phys. Ed., 1976, 14, 1903.</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/pol.1976.180141014</url>
 </reference>
 <sources>
  <citation>Okamoto, K. I.; Tanaka, K.; Kita, H.; Nakamura, A.; Kusuki, Y.; J. Poly. Sci.; Part B: Polym. Phys. 27, 1221-1233 (1989).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/polb.1989.090270604</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>Films of the polymer prepared from BPDA and ODA in $p$-chlorphenol were cast from the same solvent, dried (373 K, three hours), immersed in ethanol, dried once more at 443 K for 20 hrs (Sample (1)). Sample (2) was prepared by annealing it at 543 K, three hours. Commercial Upilex-R (Ube Industries) had $T_{\rm{g}}$ = 558 K, $\rho = \pu{1.402 g mL-1}$. Sample (1) had the same $T_{\rm{g}}$.</sample>
 </substances>
 <substances>
  <casrn>26615-45-2</casrn>
  <constituent>2</constituent>
  <formula>None</formula>
  <molweight>0.0</molweight>
  <name>Polyimide of BPDA and ODA</name>
 </substances>
 <system>Carbon dioxide with Polyimide of BPDA and ODA (Upilex-R)</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Carbon dioxide with Polyimide of BPDA and ODA (Upilex-R)</title>
</compilation>