A new high-pressure vapour–liquid equilibrium apparatus

Experimental measurements and predictions of density, viscosity, and carbon dioxide solubility in methanol, ethanol, and 1-propanol

“…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...…”

Density and Phase Behavior of the CO2 + Methylbenzene System in Wide Ranges of Temperatures and Pressures

“…The phase equilibria for the (CO2 + methylbenzene) system have been reported by several authors at temperatures from (283 to 572) K and pressures from (10 to 70) MPa. [29][30][31][32][33][34][35][36][37][38][39][40][41] However, density data for this binary system are lacking in the literature. To our knowledge, there are only two sets of compressed fluid density data available: the study of Pohler and Kiran, for mixtures containing (75 to 95) mol % CO2 at temperatures from (323 to 423) K and pressures from (10 to 70) MPa; 42 44 Therefore, the present work significantly extends the experimental range of density data for the (CO2 + methylbenzene) system to include high-temperature and high-pressure states relevant to CO2-EOR.…”

Phase equilibria of (Methylbenzene + Carbon dioxide + Methane) at elevated pressure: Experiment and modelling

“…To our knowledge, there are no phase equilibria data reported in the literature for the ternary mixture (C7H8 + CO2 + CH4) which is studied in this work. However, the constitute binaries systems (C7H8 + CO2) [8][9][10][11][12][13][14][15][16][17][18][19], (C7H8 + CH4) [20][21][22][23][24][25][26][27] and (CO2 + CH4) [28][29][30][31][32][33][34][35] have been reasonably well studied in the literature.…”