1 |
Weber, W. J. and Smith, E. H., "Removing Dissolved Organic Contaminants from Water," Environ. Sci. Tech., 20(10), 970-979 (1986).
DOI
ScienceOn
|
2 |
Arce, A., Blanco, A., Martinez-Ageitos, J. and Vidal, I., "LLE Data for The Systems Water+(methanol or ethanol)+n-amyl Acetate," Fluid Phase Equilib, 109(2), 291-297(1995).
DOI
ScienceOn
|
3 |
Fernandez-Torres, M. J., Gomis-Yagues, V., Ramos-Nofuentes, M. and Ruiz-Bevia, F., "The Influence of the Temperature on the Liquid- Liquid Equilibrium of the Ternary System 1-Pentanol-Ethanol-Water," Fluid Phase Equilib, 164(2), 267-273(1999).
DOI
ScienceOn
|
4 |
Al-Muhtaseb, S. A. and Fahim, M. A., "Phase Equilibria of the Ternary System Water/Acetic acid/2-Pentanol," Fluid Phase Equilib, 123(1-2), 189-203(1996).
DOI
|
5 |
Alkandary, J. A., Aljimaz, A. S., Fandary, M. S. and Fahim, M. A., "Liquid-Liquid Equilibria of Water+MTBE+Reformate," Fluid Phase Equilib., 187-188, 131-138(2001).
DOI
ScienceOn
|
6 |
Peschke, N. and Sandler, S. I., "Liquid-Liquid Equilibria of Fuel Oxygenate+Water+Hydrocarbon Mixtures. 1," J. Chem. Eng. Data, 40(1), 315-320(1995).
DOI
ScienceOn
|
7 |
Helinger and Sandler, S. I., "Liquid-Liquid Equilibria of Fuel Oxygenate+Water+Hydrocarbon Mixtures. 2," J. Chem. Eng. Data, 40(1), 321-325(1995).
DOI
ScienceOn
|
8 |
Wisniewska-Goclowska, B. and Malanowski, S. K., "A New Modification of the UNIQUAC Equation Including Temperature Dependent Parameters," Fluid Phase Equilib, 180(1-2), 103-113(2001).
DOI
ScienceOn
|
9 |
Ghannadzadeh, H., "Eleccion de Disolventes Selectivos Para La Extraccion en Fase Liquida de Alcoholes C4 (ABE) a Partir de. Biomasa," Ph.D. Thesis, Universitat Politecnica de Catalunya, Barcelona, Spain(1993).
|
10 |
Water and Waste Water Handbook Commete, "Water and Waste Water Handbook," Hanmi, Seoul(1992).
|
11 |
Marcilla, A., Olaya, M. M. and Ruiz, F., "Liquid-Liquid-Solid Equilibria of the Quaternary System Water-Ethanol-1-Butanol- Soldium Chloride at ," Fluid Phase Equilibria, 105(1), 71-91 (1995).
DOI
ScienceOn
|
12 |
Asensi, J. C., Gomis, V. and Ruiz, F., "Quaternary Liquid-Liquid Equilibrium: Water-Acetic Acid-2-Butanone-Cyclohexane at ," Fluid Phase Equilibria, 106(1-2), 203-211(1995).
DOI
ScienceOn
|
13 |
Hamad, E. Z. and Salem, A. B., "Liquid-Liquid Equilibrium of the Five Component System of n-Hexane-n-Heptane-Toluene-o- Xylene-Propylene Carbonate," Fluid Phase Equilibria, 108(1-2), 231-241(1995).
DOI
ScienceOn
|
14 |
Alnaafa, M. A., Bakr, A. and Salem, S. H., "Quaternary Liquid- Liquid Equilibrium of n-Heptane-Toluene-o-Xylene-Propylene Carbonate," Ind. Eng. Chem. Res., 33(3), 689-692(1994).
DOI
|
15 |
Nagata, I. and Tamura, K., "Quaternary LiquidLiquid Equilibria of Acetonitrile+2-Propanol+Cyclohexane+Heptane at 298.15 K," J. Chem. Eng. Data, 41(4), 873-875(1996).
DOI
ScienceOn
|
16 |
Garcia, A. N., Marcilla, A. and Olaya, M. M., "LiquidLiquidSolid Equilibria for the Quaternary System Water+Acetone+1-Butanol +Sodium Chloride at ," J. Chem. Eng. Data, 41(4), 910-917 (1996).
DOI
ScienceOn
|
17 |
Fredenslund, A., "Vapor-Liquid Equilibria using UNIFAC," Elsevier, Amsterdam(1977).
|
18 |
Gupte, P. A., "Prediction of Liquid-Liquid Equilibria with UNIFAC: a Critical Evaluation," Ind. Eng. Chem. Res., 26(10), 2036-2042(1987).
DOI
ScienceOn
|
19 |
Larsen, B. L., "A modified UNIFAC Group-Contribution Model for Prediction of Phase Equilibria and Heats of Mixing," Ind. Eng. Chem. Res., 26(10), 2274-2286(1987).
DOI
|
20 |
Haddad, P. O. and Edmister, W. C., "Phase Equilibriums in Acetic Acid-Diethylketone-Water System," J. Chem. Eng, Data, 17(3), 275-278(1972).
DOI
|
21 |
Lee, J. W. and Park, D. W., "A Study on the Recovery of Acetonitrile in the Preocess of Acrylonitrile," J. Korean Ind. & Eng. Chem., 5(6), 1016-1023(1994).
|
22 |
Treybal, R. E., "Liquid Extraction," McGRAW-HILL, New York (1963).
|
23 |
Othmer, D. F. and Tobias, P. E., "Tie Line Correlation," Ind. Eng. Chem., 34(6), 690-696(1942).
DOI
|
24 |
Hand, D. B., "Dineric Distribution," J. Phys. Chem., 34(9), 1961-2000(1930).
DOI
|
25 |
Magnussen, T., Rasmussen, P. and Fredenslund, A., "UNIFAC Parameter Table for Prediction of Liquid-Liquid Equilibriums," Ind. Eng. Process Des. Dev., 20(2), 331-339(1981).
DOI
|