1990
DOI: 10.1016/0896-8446(90)90018-h
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Measurement of static dielectric constants of supercritical fluid solvents and cosolvents: Carbon dioxide and argon, carbon dioxide, and methanol at 323 K and pressures to 25 MPa

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Cited by 28 publications
(10 citation statements)
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“…Chafer et al (2007) report the increase of the solubility of gallic acid in scCO 2 when the pressure increases. The solubility of different types of compounds increases with pressure since the density of the supercritical fluid increases (Drake and Smith, 1990). Moreover, the natural presence of ethanol in red wine could improve the extractability of phenolic compounds in this case.…”
Section: Extraction Performancementioning
confidence: 99%
“…Chafer et al (2007) report the increase of the solubility of gallic acid in scCO 2 when the pressure increases. The solubility of different types of compounds increases with pressure since the density of the supercritical fluid increases (Drake and Smith, 1990). Moreover, the natural presence of ethanol in red wine could improve the extractability of phenolic compounds in this case.…”
Section: Extraction Performancementioning
confidence: 99%
“…4 Deul and Franck investigated the water-benzene system at both high temperatures and high pressures. 5 Drake and Smith investigated the dielectric behavior of the CO2-argon system and the CO2-methanol system at low methanol mole fractions. Dombro et al 6 reported on the dielectric behavior of mixtures of carbon dioxide and methanol in the liquid and mixture-critical regions at 90 to 115°C and pressures to 240 bar.…”
Section: Introductionmentioning
confidence: 99%
“…The dielectric permittivity of supercritical fluids is small and diminishes with increasing temperatures, but at a given temperature increases with the pressure, i.e., the density. Near the critical point the static permittivity ε 0 = 8.6 for water [1], 4.8 for methanol [6], and 1.3 for carbon dioxide [7]. The cohesive energy densities and their square roots, i.e., the total (Hildebrand) solubility parameters, as well as the partial (Hansen) solubility parameters of the supercritical fluids are shown in Table 2 as near the reduced temperature T r = T/T c = 1.1 and pressure P r = P/P c = 1.1 as data are available.…”
Section: Introductionmentioning
confidence: 99%