<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>-2</exponent>
    <number>3.77e-02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>3.77</significand>
    <unit>$\pu{cm3(STP) cm-3 cmHg-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>1.1320e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>5</sigfigs>
    <significand>1.1320</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>4.10e-02</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>-2</exponent>
    <number>1.69e-02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>1.69</significand>
    <unit>$\pu{cm3(STP) cm-3 cmHg-1}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>4.505e-01</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>4</sigfigs>
    <significand>4.505</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>4.48e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>4.48</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>5.870e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>5.870</significand>
    <unit>$\pu{cm3(STP) cm-3 cmHg-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>8.9390e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>5</sigfigs>
    <significand>8.9390</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.094e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.094</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>6.340e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>6.340</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>4.8500e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>5</sigfigs>
    <significand>4.8500</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>3.610e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>3.610</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>5.800e-01</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>5.800</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>5.1600e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>5</sigfigs>
    <significand>5.1600</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-1</exponent>
    <number>2.430e-01</number>
    <property>Affinity Coefficient</property>
    <sigfigs>4</sigfigs>
    <significand>2.430</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>-2</exponent>
    <number>5.13e-02</number>
    <property>Henry's Law Solubility Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>5.13</significand>
    <unit>$\pu{cm3(g) cm-3(s) atm-1}$</unit>
   </data>
   <data>
    <exponent>0</exponent>
    <number>2.3050e+00</number>
    <property>Langmuir sorption capacity parameter</property>
    <sigfigs>5</sigfigs>
    <significand>2.3050</significand>
    <unit>$\pu{cm3/cm3}$</unit>
   </data>
   <data>
    <exponent>-2</exponent>
    <number>6.22e-02</number>
    <property>Affinity Coefficient</property>
    <sigfigs>3</sigfigs>
    <significand>6.22</significand>
    <unit>$\pu{atm-1}$</unit>
   </data>
   <pntnum>6</pntnum>
   <supplemental></supplemental>
  </points>
  <series>1</series>
  <title>Dual mode sorption parameters for various gases in PVC at 308 K</title>
 </dataset>
 <keywords>Solubility, Solubility data series</keywords>
 <method>The sorption measurement was carried out using the pressure decay method, [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>El-Hibri, M. J.; Paul, D. R.; J. Appl. Polym. Sci. 31, 2533 (1986).</citation>
  <pubtype>paper</pubtype>
  <url>https://doi.org/10.1002/app.1986.070310814</url>
 </sources>
 <substances>
  <casrn>9002-86-2</casrn>
  <constituent>2</constituent>
  <formula>(C2H3Cl)n</formula>
  <inchi>InChI=1S/C2H3Cl/c1-2-3/h2H,1H2</inchi>
  <inchikey>BZHJMEDXRYGGRV-UHFFFAOYSA-N</inchikey>
  <molweight>62.5</molweight>
  <name>Poly(vinyl chloride) (PVC)</name>
  <sample>PVC: B.F. Goodrich Co. (CS 5760); $\rho = \pu{1.389 g mL-1}$, $T_{\rm{g}}$ = 344 K. It contained 2% of tin stabilizer.</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>
  <sample>$\ce{CH4}$: purity 99%.; Other gases: purity 99.7%.</sample>
 </substances>
 <system>Various gases (x4) and Poly(vinyl chloride) (PVC)</system>
 <title>Solubility data from IUPAC SDS Volume 70 (page ?) - Various gases (x4) and Poly(vinyl chloride) (PVC)</title>
</compilation>