“…The Cambridge [16] 263 to 373 0.8 to 12 Vapour-liquid compositions Sih et al [17] 298 to 313 0.1 to 7 Viscosity of gas-expanded methanol Schwinghammer et al [20] 303 0.8 to 5.5 Vapour-liquid compositions Xie et al [23] 313 1 to 8 Solubility Xia et al [24] 313 to 395 Up to 9.7 Solubility and molality Bezanehtak et al [28] 278 to 308 1.5 to 7.4 Vapour-liquid compositions and saturated liquid density Gao et al [29] 323 to 473 6 to 16.2 Vapour-liquid compositions Smith et al [30] 313 to 323 10 to 20 ensity of gas-Dexpanded methanol Joung et al [34] 313 to 343 0.6 to 12 Vapour-liquid compositions Yeo et al [36] 298 to 430 Up to 17.5 Dew, bubble and critical points Elbaccouch et al [38] 313 1 to 7.5 Vapour-liquid compositions Chang et al [41] 291 to 313 Up to 8 Vapour-liquid compositions and saturated phase densities Reighard et al [44] 298 to 373 1.5 to 15 Vapour-liquid compositions Schlichting et al [48] 283 to 242 Up to 3.5 Vapour phase solubility Yoon et al [49] 313 0.7 to 8 Vapour-liquid compositions Ethanol (C 2 H 5 OH) Sima et al [6] 333 to 373 1.1 to 14.1 Solubility and critical data Mehl et al [7] 298 to 323 3 to 9 Solubility (bubble point) Tochigi et al [8] 313 0.5 to 4.0 Vapour-liquid compositions Seifried and Temelli [9] 313 to 343 0.1 to 11.2 Density of gas-expanded ethanol Kato et al [10] 313 1 to 10 Solubility and saturated liquid density Sih et al [11] 298 to 313 0.1 to 7.7 Viscosity of gas-expanded ethanol Chiu et al [12] 291 to 313 2.4 to 7.8 Vapour-liquid boundaries Knez et al [13] 313 to 353 1 to 14 Vapour-liquid compositions Secuianu et al [14] 293 to 353 Up to 11.1 Vapour-liquid compositions Dalmolin et al [18] 288 to 323 Up to 0.6 Solubility Wu et al [19] 333 to 572 6.7 to 14.8 Phase boundaries Kodama and Kato [21] 291 2 to 5.4 Vapour-liquid compositions and saturated phase densities Stievano and Elvassore [22] 291 to 323 3.3 to 8.1 Solubility and saturated liquid density Tsivintzelis et al [25] 313 to 328 0.6 to 9.4 Vapour-liquid c...…”
Section: Apparatus and Proceduresmentioning
confidence: 99%
“…It is due to higher dissolution of carbon dioxide in alcohol at lower temperatures. Sih et al [11,17] have also measured the gas expanded liquid viscosity for (carbon dioxide + methanol) and (carbon dioxide + ethanol) systems at 303.15 K using a customised falling-weight viscometer; these data were also presented in this figure. As on can see, the measured viscosity data are consistent with Sih et al [11,17] measurements.…”
Section: Solubility and Saturated Phase Propertiesmentioning
“…The Cambridge [16] 263 to 373 0.8 to 12 Vapour-liquid compositions Sih et al [17] 298 to 313 0.1 to 7 Viscosity of gas-expanded methanol Schwinghammer et al [20] 303 0.8 to 5.5 Vapour-liquid compositions Xie et al [23] 313 1 to 8 Solubility Xia et al [24] 313 to 395 Up to 9.7 Solubility and molality Bezanehtak et al [28] 278 to 308 1.5 to 7.4 Vapour-liquid compositions and saturated liquid density Gao et al [29] 323 to 473 6 to 16.2 Vapour-liquid compositions Smith et al [30] 313 to 323 10 to 20 ensity of gas-Dexpanded methanol Joung et al [34] 313 to 343 0.6 to 12 Vapour-liquid compositions Yeo et al [36] 298 to 430 Up to 17.5 Dew, bubble and critical points Elbaccouch et al [38] 313 1 to 7.5 Vapour-liquid compositions Chang et al [41] 291 to 313 Up to 8 Vapour-liquid compositions and saturated phase densities Reighard et al [44] 298 to 373 1.5 to 15 Vapour-liquid compositions Schlichting et al [48] 283 to 242 Up to 3.5 Vapour phase solubility Yoon et al [49] 313 0.7 to 8 Vapour-liquid compositions Ethanol (C 2 H 5 OH) Sima et al [6] 333 to 373 1.1 to 14.1 Solubility and critical data Mehl et al [7] 298 to 323 3 to 9 Solubility (bubble point) Tochigi et al [8] 313 0.5 to 4.0 Vapour-liquid compositions Seifried and Temelli [9] 313 to 343 0.1 to 11.2 Density of gas-expanded ethanol Kato et al [10] 313 1 to 10 Solubility and saturated liquid density Sih et al [11] 298 to 313 0.1 to 7.7 Viscosity of gas-expanded ethanol Chiu et al [12] 291 to 313 2.4 to 7.8 Vapour-liquid boundaries Knez et al [13] 313 to 353 1 to 14 Vapour-liquid compositions Secuianu et al [14] 293 to 353 Up to 11.1 Vapour-liquid compositions Dalmolin et al [18] 288 to 323 Up to 0.6 Solubility Wu et al [19] 333 to 572 6.7 to 14.8 Phase boundaries Kodama and Kato [21] 291 2 to 5.4 Vapour-liquid compositions and saturated phase densities Stievano and Elvassore [22] 291 to 323 3.3 to 8.1 Solubility and saturated liquid density Tsivintzelis et al [25] 313 to 328 0.6 to 9.4 Vapour-liquid c...…”
Section: Apparatus and Proceduresmentioning
confidence: 99%
“…It is due to higher dissolution of carbon dioxide in alcohol at lower temperatures. Sih et al [11,17] have also measured the gas expanded liquid viscosity for (carbon dioxide + methanol) and (carbon dioxide + ethanol) systems at 303.15 K using a customised falling-weight viscometer; these data were also presented in this figure. As on can see, the measured viscosity data are consistent with Sih et al [11,17] measurements.…”
Section: Solubility and Saturated Phase Propertiesmentioning
“…Then, viscosity was predicted for different CO 2 and MeOH mixtures using a correlation of second order between viscosity and MeOH content, on the basis of experimentally determined data published by Sih et al [32]:…”
Section: Column Performance With State-of-the-art Sfc Instrumentationmentioning
“…P was corrected for the native system pressure drop determined without a column in place. Estimation of supercritical CO 2 viscosity was made on the correlations proposed by Ouyang [43] and applied to different CO 2 /methanol mixtures using a second order correlation between viscosity and MeOH concentration, based on previously published experimentally-determined data [44]. By combining these two correlations, the viscosity of mixtures of supercritical CO 2 and MeOH for a given pressure and temperature can easily be predicted.…”
Section: Evaluation Of Column Performancementioning
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