[1]
Kamel, K., Paolo, A., Ireneo, K., Abdallah, D., Solubility of diamines in supercritical carbon dioxide experimental determination and correlation, J. Supercrit. Fluids, 41, 10-19 (2007).
Google Scholar
[2]
J.H. Hsu, C.S. Tan, Separation of ethanol from aqueous solution by a method incorporating supercritical CO2 with reverse osmosis, J. of Membrane Science, 81, 273-285. (1993).
DOI: 10.1016/0376-7388(93)85179-z
Google Scholar
[3]
Zhang, J.C., WU, X.Y., CAO, W.L., Study on critical properties for CO2+cosolvent binary system and ternary system, Chin. J. Chem. Eng., 10 (2), 223-227 (2002).
Google Scholar
[4]
Ghaziaskar H.S., Daneshfar A., Rezayat M., The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide, Fluid Phase Equilibria, 238, 106-111 (2005).
DOI: 10.1016/j.fluid.2005.09.023
Google Scholar
[5]
Elizalde-Solis O., Galicia-Luna L.A., Sandler S.I., Vapor–liquid equilibria and critical points of the CO2 + 1-hexanol and CO2 + 1-heptanol systems, Fluid Phase Equilibria, 210, 215-227 (2003).
DOI: 10.1016/s0378-3812(03)00170-5
Google Scholar
[6]
Lee H.S., Lee H., High-pressure phase equilibria for the carbon dioxide–2-pentanol and carbon dioxide–water–2-pentanol systems, Fluid Phase Equilibria , 150-151, 695-701 (1998).
DOI: 10.1016/s0378-3812(98)00349-5
Google Scholar
[7]
Silva M.V., Barbosa D., High pressure vapor–liquid equilibrium data for the systems carbon dioxide/2-methyl-1-propanol and carbon dioxide/3-methyl-1-butanol at 288. 2, 303. 2 and 313. 2 K, Fluid Phase Equilibria 198, 229-237 (2002).
DOI: 10.1016/s0378-3812(01)00766-x
Google Scholar
[8]
Silva-Oliver G., Galicia-Luna L.A., Sandler S.I., Vapor–liquid equilibria and critical points for the carbon dioxide +1-pentanol and carbon dioxide +2-pentanol systems at temperatures from 332 to 432 K, Fluid Phase Equilibria, 200, 161-172 (2002).
DOI: 10.1016/s0378-3812(02)00024-9
Google Scholar
[9]
Zuniga-Moreno A., Galicia-Luna L.A., Sandler S.I., Compressed liquid densities and excess molar volumes for (CO2 + 1-pentanol) binary system at temperatures from 313 to 363 K and pressures up to 25 MPa, J. Chem. Thermodynamics , 40, 180-192 (2008).
DOI: 10.1016/j.jct.2007.07.005
Google Scholar
[10]
Lopez J.A., Trejos V.M., Cardona C.A., Parameters estimation and VLE calculation in asymmetric binary mixtures containing carbon dioxide + n-alkanols, Fluid Phase Equilibria 275, 1-7. (2009).
DOI: 10.1016/j.fluid.2008.09.013
Google Scholar
[11]
Cortesi A., Kikic I., Determination of partial molar volumes at infinite dilution of alcohols and terpenes in supercritical carbon dioxide, J. of Supercritical Fluid, 9, 141-145 (1996).
DOI: 10.1016/s0896-8446(96)90024-8
Google Scholar
[12]
Tatsuru, S., Naoki, T., Kunio, N., Solubilities of ethanol, 1-prjopanol, 2-propanol and 1-butanol in supercritical carbon dioxide at 313 K and 333 K, Fluid Phase Equilibrium, 67, 213-226 (1991).
DOI: 10.1016/0378-3812(91)90057-e
Google Scholar
[13]
Feng L.C., Cheng K.W., Tang M., Chen Y.P., Vapor–liquid equilibria of carbon dioxide with ethyl benzoate, diethyl succinate and isoamyl acetate binary mixtures at elevated pressures, J. of Supercritical Fluid , 21, 111-121 (2001).
DOI: 10.1016/s0896-8446(01)00091-2
Google Scholar
[14]
Yousef A.M., Elkanzi E.M., Singh H., "Prediction of supercritical CO2 solubility using the Krichevsky–Ilinskaya equation with as an adjustable parameter, J. of Supercritical Fluid, 20, 105-112 (2001).
DOI: 10.1016/s0896-8446(01)00054-7
Google Scholar
[15]
A. Cortesi, I. Kikic, J. of Supercritical Fluid 9(1996) 141-145.
Google Scholar
[16]
[S.O. Guadalupe, Galicia-Luna L.A., Vapor–liquid equilibria near critical point and critical points for the CO2+1-butanol and CO2+2-butanol systems at temperatures from 324 to 432 K, Fluid Phase Equilibria, 182, 145-156 (2001).
DOI: 10.1016/s0378-3812(01)00388-0
Google Scholar
[17]
Chen H.I., Chen P.H., Chang H.Y., High-Pressure Vapor−Liquid Equilibria for CO2 + 2-Butanol, CO2 + Isobutanol, and CO2 + tert-Butanol Systems, J. Chem. Eng. Data, 48, 1407-1412. (2003).
DOI: 10.1021/je020214r
Google Scholar
[18]
Peng D.Y., Robinson D.B., A new Two-Constant Equation of State , Ind. Eng. Chem. Fundam, 1559-64 (1976).
Google Scholar
[19]
Soave G., Equilibrium constants from a modified Redlich-Kwong equation of state, Chem. Eng. Sci. 27, 1197-1205 (1972).
DOI: 10.1016/0009-2509(72)80096-4
Google Scholar
[20]
Krichevsky I.R., Kasarnovsky J.S., Thermodynamical Calculations of Solubilities of Nitrogen and Hydrogen in Water at High Pressures, J. Am. Chem. Soc, 57, 2168–2171 (1935).
DOI: 10.1021/ja01314a036
Google Scholar
[21]
G.Q. Liu, L.X. Ma, J. Liu, Chemical Property Data Handbook. Chemical Industry Press, Peking, (2002) 60.
Google Scholar
[22]
John, M.P., Rüdiger, N.L., Edmundo, G.A., High pressure vapor-liquid equilibrium calculation, Molecular Thermodynamics of Fluid-Phase Equilibria, Chemical Industry Press, Beijing, 435-441(2006). (in Chinese).
Google Scholar