Submitted:
17 September 2024
Posted:
17 September 2024
You are already at the latest version
Abstract

Keywords:
1. Introduction
2. Materials and Methods
2.1. Solvents and Materials
2.2. Inverse Gas Chromatography
2.3. Thermodynamic Methods
2.3.1. Fundamental Equation of IGC
2.3.2. London Dispersive Surface Energy of Solid Surfaces
2.3.3. London Dispersive and Polar Free Energies of Adsorption
- It was proved that these various methods cannot be considered as accurate quantitative methods that allow an accurate separation between the dispersive and polar free energies of adsorption and the only method theoretically well-founded was that based on the deformation polarizability. However, this method was not well-applied, because the authors did some approximations that led to wrong values of the polar contribution of the free energy of interaction between the solvents and the solid materials.
2.3.4. Lewis’s Acid-Base Parameters of PS-b-P4VP Diblock Copolymer
2.3.4. Lewis’s Acid-Base Surface Energies of PS-b-P4VP Copolymer
3. Experimental Results
3.1. Variations of of Solvents Adsorbed on PS-b-P4VP Diblock Copolymer
3.2. London Dispersive Surface Energy of PS-b-P4VP Diblock Copolymer
- -
- relative to PS glass transition
- -
- relative to P4VP glass transition
- -
- the surface entropy: ,
- -
- the London dispersive energy at 0K: ,
- -
- the intrinsic temperature .
3.3. Polar Free Surface Energy of PS-b-P4VP Diblock Copolymer

3.4. Polar Enthalpy and Entropy of Adsorption
3.5. Temperature Effect on the Lewis’s Acid-Base Parameters of the Copolymer

3.6. Separation Distance, Lewis Acid-Base Surface Energies of PS-b-P4VP Copolymer, and and Polar Surface Energy of Solvents
3.7. Work of Adhesion of Solvents on the PS-b-P4VP Copolymer against the Temperature

4. Conclusions
Supplementary Materials
Funding
Data Availability Statement
Conflicts of Interest
References
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| Equation of | R2 | Temperature interval |
| = 7.10-4T2 - 0.324T + 66.3 | 0.9983 | 313.15K - 378.15K |
| = 1.7.10-2T2 - 13.733T + 2806 | 0.9910 | 378.15K - 421.15K |
| = 9.1.10-3T2 - 8.465T + 1979 | 0.9914 | 421.15K - 473.15K |
| Solvent | Equation of (kJ/mol)) | (J/k.mol) | (kJ/mol)) | R2 |
| CHCl3 | = -0.0086T + 8.083 | 8.6 | 8.083 | 0.7739 |
| CH2Cl2 | = -0.0079T + 14.074 | 7.9 | 14.074 | 0.7529 |
| THF | = -0.0186T + 1.733 | 18.6 | 1.733 | 0.8626 |
| MeCN | = -0.018T + 24.538 | 18.0 | 24.538 | 0.9422 |
| CCl4 | = -0.0195T + 13.095 | 19.5 | 13.095 | 0.8499 |
| Ethyl acetate | = -0.0071T + 8.773 | 7.1 | 8.773 | 0.423 |
| Ethanol | = -0.020T + 18.952 | 20.0 | 18.952 | 0.8176 |
| Acetone | = 0.0084T + 13.14 | 8.4 | 13.140 | 0.3215 |
| Lewis’s acid-base parameter | Average values | R2 |
| 0.092 | 0.8556 | |
| 0.693 | 0.8556 | |
| / | 7.533 | 0.8556 |
| 0.785 | 0.8556 | |
| 0.06 | 0.6732 | |
| 1.0 | 0.6732 | |
| 18.18 | 0.6732 | |
| 1.06 | 0.6732 |
| T(K) | |||||
|---|---|---|---|---|---|
| 313.15 | 43.33 | 15.82 | 52.36 | 28.24 | 80.61 |
| 323.15 | 51.05 | 14.93 | 55.21 | 29.63 | 84.85 |
| 333.15 | 59.29 | 14.07 | 57.77 | 31.00 | 88.77 |
| 343.15 | 68.08 | 13.25 | 60.07 | 32.33 | 92.40 |
| 353.15 | 76.49 | 12.40 | 61.59 | 33.29 | 94.88 |
| 363.15 | 82.96 | 12.28 | 63.84 | 34.79 | 98.63 |
| 368.15 | 81.51 | 11.81 | 62.05 | 30.08 | 92.13 |
| 373.15 | 79.96 | 11.59 | 60.87 | 27.26 | 88.13 |
| 378.15 | 82.02 | 12.02 | 62.79 | 32.75 | 95.54 |
| 383.15 | 73.70 | 11.33 | 57.81 | 29.72 | 87.52 |
| 393.15 | 58.03 | 11.62 | 51.94 | 25.17 | 77.11 |
| 403.15 | 65.57 | 11.81 | 55.66 | 25.31 | 80.97 |
| 413.15 | 77.12 | 12.34 | 61.69 | 27.09 | 88.78 |
| 421.15 | 79.58 | 11.54 | 60.60 | 29.45 | 90.05 |
| 423.15 | 78.67 | 11.55 | 60.30 | 26.54 | 86.84 |
| 433.15 | 51.16 | 8.51 | 41.73 | 19.85 | 61.58 |
| 438.15 | 51.42 | 8.06 | 40.72 | 16.93 | 57.65 |
| 443.15 | 50.79 | 7.66 | 39.45 | 15.46 | 54.92 |
| 453.15 | 52.39 | 7.57 | 39.82 | 13.05 | 52.87 |
| 463.15 | 54.15 | 7.25 | 39.63 | 11.72 | 51.35 |
| 473.15 | 53.70 | 6.89 | 38.48 | 10.68 | 49.16 |
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