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Publication List Dias, A. M. A.; Bonifácio, R. P.; Marrucho, I. M.; Pádua, A. A H.; Gomes, M. F. C. Solubility of Oxygen in n-hexane and in n-perfluorohexane. Experimental determination and prediction by molecular simulation, Phys. Chem. Chem. Phys. (2003) 5: 543 Dias, A. M. A; Freire, M. G.; Coutinho, J. A. P.; Marrucho, I. M. Solubility of Oxygen in Liquid Perfluorocarbons, Fluid Phase Equilibria (2004) 222-223: 325 Dias, A. M. A; Pàmies, J. C.; Coutinho, J. A. P.; Marrucho, I. M.; Vega, L. F. SAFT Modeling of the Solubility of Gases in Perfluoroalkanes, J. of Phys. Chem. B (2004) 108: 1450 Dias, A. M. A; Coutinho, J. A. P.; Piñeiro M.; Gomes, M. F. C.; Marrucho, I. M. Thermodynamic Properties of Perfluoro-n-octane, Fluid Phase Equilibria (2004) 225: 39 Freire, M. G.; Dias, A. M. A.; Coelho, M. A. Z.; Coutinho, J. A. P.; Marrucho, I. M. Ageing Mechanisms of Perfluorocarbon Emulsions using Image Analysis, J. of Colloid and Interface Science (2004) 286: 224 Freire, M. G.; Dias, A. M. A.; Coelho, M. A. Z; Coutinho, J. A. P.; Marrucho, I. M. Enzymatic Method for Determining Oxygen Solubility in Perfluorocarbon Emulsions, Fluid Phase Equilibria (2004) 231: 109 Dias, A. M. A.; Gonçalves, C. M.; Caço, A. I.; Santos, L. M. N. B. F.; Piñeiro, M. M.; Vega, L. F.; Coutinho, J. A. P.; Marrucho, I. M. Densities and Vapor Pressures of Highly Fluorinated Compounds, J. of Chem. Eng. Data (2005) 50: 1328 Dias, A. M. A.; Gonçalves, C. M. B.; Legido, JJJ. L.; Coutinho, J. A. P.; Marrucho, I. M. Solubility of Oxygen in Substituted Perfluorocarbon, Aceite em Fluid Phase Equilibria (2005) Dias, A. M. A; Pàmies, J. C.; Vega, L. F.; Coutinho, J. A. P.; Marrucho, I. M. Modelling the Solubility of Gases in Saturated and Substituted Perfluoroalkanes Aceite em Polish Journal of Chemistry (2005) Dias, A. M. A.; Pamies, J.; Carrier, H.; Daridon, JL; Vega, L. F.; Coutinho, J. A. P.; Marrucho, I. M. Vapor – Liquid Equilibrium of Carbon Dioxide – Perfluoroalkane Mixtures: experimental data and SAFT modeling, Submetido a IECR (2005) Melo, M. J. P.; Dias, A. M. A.; Blesic, M.; Rebelo, L. P. N.; Vega, L. F.; Coutinho, J. A. P.; Marrucho, I. M., Liquid-Liquid Equilibrium of (Perfluoroalkane + Alkane) Binary Mixtures, Submetido a IECR (2005)
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Ana Maria Antunes Dias Universidade
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o júri presidente Prof. Dr. Joaqui
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palavras-chave resumo perfluoroalca
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Contents Notation List of Tables Li
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Notation Abbreviations AAD EoS LCST
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List of Tables Table I.1 Average Bo
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Table III.6 Adjusted Binary Paramet
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Figure II.9 Comparison between corr
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Figure III.8 Temperature-density di
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Figure III.25 Vapor-phase mole frac
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I.1. Fluorine Properties General In
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Table I.2. Physicochemical Properti
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General Introduction order to compa
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General Introduction the numerous a
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General Introduction carbon dioxide
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General Introduction animals. That
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General Introduction Table I.3. Lit
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References General Introduction Ban
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General Introduction Hildebrand, J.
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General Introduction Rowinsky EK. N
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II. Part EXPERIMENTAL METHODS, RESU
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Experimental Methods, Results and D
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Table II.3. (continued) T K ρexp g
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ρ / g.cm-3 1.750 1.730 1.710 1.690
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I. 3. Vapour pressure I.3.1. Biblio
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I.3.2. Apparatus and Procedure Expe
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I.3.3. Experimental Results and Dis
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Table II.8. (continued) T K Pexp kP
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ΔH vap = TΔS vap 2⎛ d ln P ⎞
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I.4. Solubility at atmospheric pres
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x2 (T,P2) 7.0E-03 6.0E-03 5.0E-03 4
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L 2,1 0.70 0.60 0.50 0.40 0.30 285
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P / MPa 6 5 4 3 2 1 0 P / MPa 14 12
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II.6. Liquid - Liquid Equilibrium I
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0 τ β Δ1 2Δ1 [ 1+ B τ + B τ +
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References Experimental Methods, Re
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III.1. Introduction Modeling Most c
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Modeling The pioneering work of Wer
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III.2. Soft-SAFT Model Modeling A S
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Modeling The equation of state is w
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Chain Term Modeling Originally Wert
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Modeling The model is easily extend
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( ) ( ) ∑∑∑ 3 2 2 2 2 qq 32π
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Modeling HRT is a promising theory,
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( ρ) ρ , 0 ≤ ρ ( ρ) 2 Modelin
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III.3. Application to Pure Compound
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Modeling From the optimised paramet
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T / K 400 350 300 250 200 150 100 5
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ln Pvap 1.0E+01 1.0E+00 1.0E-01 1.0
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Modeling Table III.2. Absolute Aver
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Modeling The correlation coefficien
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Pvap (MPa) 4.00 3.50 3.00 2.50 2.00
Page 143 and 144: Modeling The mixture parameters a a
Page 145 and 146: Modeling the assumptions made by th
Page 147 and 148: Modeling between oxygen and perfluo
Page 149 and 150: xSolute 5.5E-03 5.0E-03 4.5E-03 4.0
Page 151 and 152: Modeling previous work, dealing wit
Page 153 and 154: Modeling These results confirm that
Page 155 and 156: Modeling CO2 binary mixtures using
Page 157 and 158: Modeling average deviation (AAD) be
Page 159 and 160: P / MPa 14 12 10 8 6 4 2 0 0 0.2 0.
Page 161 and 162: Modeling Figures III.16, III.17 and
Page 163 and 164: Modeling calculations from the orig
Page 165 and 166: Table III.9. References for VLE exp
Page 167 and 168: P / MPa 20 18 16 14 12 10 8 6 4 2 0
Page 169 and 170: Modeling Finally, Figure III.24 pre
Page 171 and 172: III.4.4. VLE and LLE of Alkane and
Page 173 and 174: Modeling number of perfluro-n-alkan
Page 175 and 176: y C6F14 1.0 0.8 0.6 0.4 0.2 0.0 0.0
Page 177 and 178: P / MPa 0.08 0.07 0.06 0.05 0.04 0.
Page 179 and 180: P / MPa 0.12 0.10 0.08 0.06 0.04 0.
Page 181 and 182: Modeling approach based on the meth
Page 183 and 184: Modeling Blas, F. J.; Vega, L. F.,
Page 185 and 186: DIPPR, Thermophysical Properties Da
Page 187 and 188: Modeling Hildebrand, J. H.; Fisher,
Page 189 and 190: Modeling McCabe, C.; Jackson, SAFT-
Page 191 and 192: Modeling Poling, B.; Prauznitz, J.;
Page 193: Modeling Wertheim, M. S., Fluids wi
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