1970
DOI: 10.1021/i260034a017
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Thermodynamics of Solid Solubility in Cryogenic Solvents

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Cited by 53 publications
(29 citation statements)
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“…The assumed temperature is T = 90 K. The notation x.y(−n) = x.y × 10 −n has been used. One can notice that ideal solubility of CO 2 is comparable to the values reported by Preston and Prausnitz (1970) and Preston et al (1971) for somewhat higher temperatures around 130-140 K. We stress that an identical value of the enrichment ∆ is the consequence of a saturation of solutes that occurs at the very end of the evaporation. Of course, a solvent of a different composition (e.g., a methane rich one) leads strictly to the same result because here we are making the calculations by adopting the ideal solution hypothesis.…”
Section: Evaporites Upper Layer Composition Calculationsupporting
confidence: 74%
“…The assumed temperature is T = 90 K. The notation x.y(−n) = x.y × 10 −n has been used. One can notice that ideal solubility of CO 2 is comparable to the values reported by Preston and Prausnitz (1970) and Preston et al (1971) for somewhat higher temperatures around 130-140 K. We stress that an identical value of the enrichment ∆ is the consequence of a saturation of solutes that occurs at the very end of the evaporation. Of course, a solvent of a different composition (e.g., a methane rich one) leads strictly to the same result because here we are making the calculations by adopting the ideal solution hypothesis.…”
Section: Evaporites Upper Layer Composition Calculationsupporting
confidence: 74%
“…(1) Tan et al (2013); (2) this work, by fitting data from Gabis (1991) provided by Glein & Shock (2013); (3) this work, by fitting data from Neumann & Mann (1969); (4) Gross & Sadowski (2001); (5) this work, by fitting Cheung & Zander (1968) and previously used by Preston & Prausnitz (1970); (6) this work, by fitting data from Diez-y- Riega et al (2014);(X) set to zero, as dissolution data were not found in the literature. (Etters & Kuchta, 1989;Simon, 1980) C 6 H 6 7.384 9.416 6.757 90 (Craven et al, 1993)…”
Section: Namementioning
confidence: 99%
“…We consider the case of the Ideal Solutions Theory (IST), for which X i,sat is calculated by assuming Γ i = 1 (all the molecules share the same affinity with each other), and the case of the Regular Solutions Theory (RST) of Preston and Prausnitz (1970) for which Γ i = 1 (molecules have preferential affinity with one or the other). The latter approach has already been used in several publications dealing with the lakes and seas composition (Raulin, 1987;Dubouloz et al, 1989;Cordier et al, 2009Cordier et al, , 2013b.…”
Section: B2 Solubility Of Titan's Solidsmentioning
confidence: 99%
“…Preston and Prausnitz (1970) and Szczepaniec-Cieciak et al (1978)), φ 1 is the volume fraction of the liquid, computed as follows:…”
Section: B2 Solubility Of Titan's Solidsmentioning
confidence: 99%