Alexandre K. Bokarev 2 3.03e+02 Ambient temperature 3 3.03 $\pu{K}$ -1 1.319e-01 Henry's Law Solubility Coefficient 4 1.319 $\pu{cm3(g) cm-3(s) atm-1}$ -1 4.79e-01 Langmuir sorption capacity parameter 3 4.79 $\pu{cm3/cm3}$ -1 2.914e-01 Affinity Coefficient 4 2.914 $\pu{atm-1}$ 1 2 3.13e+02 Ambient temperature 3 3.13 $\pu{K}$ -1 1.012e-01 Henry's Law Solubility Coefficient 4 1.012 $\pu{cm3(g) cm-3(s) atm-1}$ -1 2.95e-01 Langmuir sorption capacity parameter 3 2.95 $\pu{cm3/cm3}$ -1 2.601e-01 Affinity Coefficient 4 2.601 $\pu{atm-1}$ 2 2 3.23e+02 Ambient temperature 3 3.23 $\pu{K}$ -2 7.69e-02 Henry's Law Solubility Coefficient 3 7.69 $\pu{cm3(g) cm-3(s) atm-1}$ -1 2.17e-01 Langmuir sorption capacity parameter 3 2.17 $\pu{cm3/cm3}$ -1 2.347e-01 Affinity Coefficient 4 2.347 $\pu{atm-1}$ 3 2 3.33e+02 Ambient temperature 3 3.33 $\pu{K}$ -2 6.13e-02 Henry's Law Solubility Coefficient 3 6.13 $\pu{cm3(g) cm-3(s) atm-1}$ -2 9.6e-02 Langmuir sorption capacity parameter 2 9.6 $\pu{cm3/cm3}$ -1 3.280e-01 Affinity Coefficient 4 3.280 $\pu{atm-1}$ 4 2 3.43e+02 Ambient temperature 3 3.43 $\pu{K}$ -2 4.93e-02 Henry's Law Solubility Coefficient 3 4.93 $\pu{cm3(g) cm-3(s) atm-1}$ -2 8.9e-02 Langmuir sorption capacity parameter 2 8.9 $\pu{cm3/cm3}$ -1 3.267e-01 Affinity Coefficient 4 3.267 $\pu{atm-1}$ 5 1 0 -7.13e+00 Enthalpy change 3 -7.13 $\pu{kcal/mol}$ 1 2 0 4.40e+00 Pressure (1) 3 4.40 $\pu{kPa}$ -1 6.0e-01 Sorption 2 6.0 $\pu{V_{1}/V_{2}}$ 1 0 5.77e+00 Pressure (1) 3 5.77 $\pu{kPa}$ -1 8.1e-01 Sorption 2 8.1 $\pu{V_{1}/V_{2}}$ 2 0 7.10e+00 Pressure (1) 3 7.10 $\pu{kPa}$ -1 9.9e-01 Sorption 2 9.9 $\pu{V_{1}/V_{2}}$ 3 0 9.80e+00 Pressure (1) 3 9.80 $\pu{kPa}$ 0 1.31e+00 Sorption 3 1.31 $\pu{V_{1}/V_{2}}$ 4 1 1.251e+01 Pressure (1) 4 1.251 $\pu{kPa}$ 0 1.61e+00 Sorption 3 1.61 $\pu{V_{1}/V_{2}}$ 5 1 1.517e+01 Pressure (1) 4 1.517 $\pu{kPa}$ 0 1.92e+00 Sorption 3 1.92 $\pu{V_{1}/V_{2}}$ 6 1 1.783e+01 Pressure (1) 4 1.783 $\pu{kPa}$ 0 2.17e+00 Sorption 3 2.17 $\pu{V_{1}/V_{2}}$ 7 1 2.194e+01 Pressure (1) 4 2.194 $\pu{kPa}$ 0 2.56e+00 Sorption 3 2.56 $\pu{V_{1}/V_{2}}$ 8 1 2.594e+01 Pressure (1) 4 2.594 $\pu{kPa}$ 0 2.92e+00 Sorption 3 2.92 $\pu{V_{1}/V_{2}}$ 9 3 0 4.37e+00 Pressure (1) 3 4.37 $\pu{kPa}$ -1 4.4e-01 Sorption 2 4.4 $\pu{V_{1}/V_{2}}$ 1 0 5.62e+00 Pressure (1) 3 5.62 $\pu{kPa}$ -1 5.7e-01 Sorption 2 5.7 $\pu{V_{1}/V_{2}}$ 2 0 7.07e+00 Pressure (1) 3 7.07 $\pu{kPa}$ -1 7.2e-01 Sorption 2 7.2 $\pu{V_{1}/V_{2}}$ 3 0 9.81e+00 Pressure (1) 3 9.81 $\pu{kPa}$ -1 9.2e-01 Sorption 2 9.2 $\pu{V_{1}/V_{2}}$ 4 1 1.243e+01 Pressure (1) 4 1.243 $\pu{kPa}$ 0 1.20e+00 Sorption 3 1.20 $\pu{V_{1}/V_{2}}$ 5 1 1.514e+01 Pressure (1) 4 1.514 $\pu{kPa}$ 0 1.39e+00 Sorption 3 1.39 $\pu{V_{1}/V_{2}}$ 6 1 1.780e+01 Pressure (1) 4 1.780 $\pu{kPa}$ 0 1.60e+00 Sorption 3 1.60 $\pu{V_{1}/V_{2}}$ 7 1 2.184e+01 Pressure (1) 4 2.184 $\pu{kPa}$ 0 1.92e+00 Sorption 3 1.92 $\pu{V_{1}/V_{2}}$ 8 1 2.598e+01 Pressure (1) 4 2.598 $\pu{kPa}$ 0 2.22e+00 Sorption 3 2.22 $\pu{V_{1}/V_{2}}$ 9 4 0 5.74e+00 Pressure (1) 3 5.74 $\pu{kPa}$ -1 4.2e-01 Sorption 2 4.2 $\pu{V_{1}/V_{2}}$ 1 0 8.37e+00 Pressure (1) 3 8.37 $\pu{kPa}$ -1 6.0e-01 Sorption 2 6.0 $\pu{V_{1}/V_{2}}$ 2 1 1.107e+01 Pressure (1) 4 1.107 $\pu{kPa}$ -1 7.8e-01 Sorption 2 7.8 $\pu{V_{1}/V_{2}}$ 3 1 1.381e+01 Pressure (1) 4 1.381 $\pu{kPa}$ -1 9.7e-01 Sorption 2 9.7 $\pu{V_{1}/V_{2}}$ 4 1 1.780e+01 Pressure (1) 4 1.780 $\pu{kPa}$ 0 1.20e+00 Sorption 3 1.20 $\pu{V_{1}/V_{2}}$ 5 1 2.180e+01 Pressure (1) 4 2.180 $\pu{kPa}$ 0 1.44e+00 Sorption 3 1.44 $\pu{V_{1}/V_{2}}$ 6 1 2.599e+01 Pressure (1) 4 2.599 $\pu{kPa}$ 0 1.68e+00 Sorption 3 1.68 $\pu{V_{1}/V_{2}}$ 7 5 0 5.70e+00 Pressure (1) 3 5.70 $\pu{kPa}$ -1 3.0e-01 Sorption 2 3.0 $\pu{V_{1}/V_{2}}$ 1 0 8.33e+00 Pressure (1) 3 8.33 $\pu{kPa}$ -1 4.5e-01 Sorption 2 4.5 $\pu{V_{1}/V_{2}}$ 2 1 1.103e+01 Pressure (1) 4 1.103 $\pu{kPa}$ -1 5.8e-01 Sorption 2 5.8 $\pu{V_{1}/V_{2}}$ 3 1 1.373e+01 Pressure (1) 4 1.373 $\pu{kPa}$ -1 7.1e-01 Sorption 2 7.1 $\pu{V_{1}/V_{2}}$ 4 1 1.773e+01 Pressure (1) 4 1.773 $\pu{kPa}$ -1 9.1e-01 Sorption 2 9.1 $\pu{V_{1}/V_{2}}$ 5 1 2.188e+01 Pressure (1) 4 2.188 $\pu{kPa}$ 0 1.09e+00 Sorption 3 1.09 $\pu{V_{1}/V_{2}}$ 6 1 2.595e+01 Pressure (1) 4 2.595 $\pu{kPa}$ 0 1.28e+00 Sorption 3 1.28 $\pu{V_{1}/V_{2}}$ 7 6 0 5.66e+00 Pressure (1) 3 5.66 $\pu{kPa}$ -1 2.5e-01 Sorption 2 2.5 $\pu{V_{1}/V_{2}}$ 1 0 8.33e+00 Pressure (1) 3 8.33 $\pu{kPa}$ -1 3.4e-01 Sorption 2 3.4 $\pu{V_{1}/V_{2}}$ 2 1 1.092e+01 Pressure (1) 4 1.092 $\pu{kPa}$ -1 4.6e-01 Sorption 2 4.6 $\pu{V_{1}/V_{2}}$ 3 1 1.370e+01 Pressure (1) 4 1.370 $\pu{kPa}$ -1 5.7e-01 Sorption 2 5.7 $\pu{V_{1}/V_{2}}$ 4 1 1.766e+01 Pressure (1) 4 1.766 $\pu{kPa}$ -1 7.3e-01 Sorption 2 7.3 $\pu{V_{1}/V_{2}}$ 5 1 2.184e+01 Pressure (1) 4 2.184 $\pu{kPa}$ -1 8.8e-01 Sorption 2 8.8 $\pu{V_{1}/V_{2}}$ 6 1 2.595e+01 Pressure (1) 4 2.595 $\pu{kPa}$ 0 1.05e+00 Sorption 3 1.05 $\pu{V_{1}/V_{2}}$ 7 7 Solubility, Solubility data series Sorption was determined by a gravimetric method using a Calm microbalance (Model KG). Corrections were made for buoyancy effects. The International Union of Pure and Applied Chemistry Casur, E.; Smith, T. G.; J. Appl. Polym. Sci. 31, 1425 (1986). paper https://doi.org/10.1002/app.1986.070310526 9004-57-3 2 C23H24N6O4 InChI=1S/C23H24N6O4/c1-4-5-8-28(9-10-33-17(3)30)20-6-7-22(16(2)11-20)26-27-23-18(14-24)12-21(29(31)32)13-19(23)15-25/h6-7,11-13H,4-5,8-10H2,1-3H3 ARSKJXYLLONUAJ-UHFFFAOYSA-N 440.5 Ethyl Cellulose 74-98-6 1 C3H8 InChI=1S/C3H8/c1-3-2/h3H2,1-2H3 ATUOYWHBWRKTHZ-UHFFFAOYSA-N 44.0956 Propane Gases: purity 99.99%. EC (Ethocel 10 cp): Dow Chemical Co., contained 48%-49.5% ethoxy groups, $\rho = \pu{1.13 g mL-1}$, $T_{\rm{g}}$ = 396 K. Propane with Ethyl Cellulose (EC)