Korean Journal of Chemical Engineering, Vol.30, No.6, 1289-1294, 2013
Phase equilibrium data for aqueous solutions of formic acid with 2-ethyl-1-hexanol at T=(298.2, 308.2, 318.2, and 328.2) K
Liquid-liquid equilibrium (LLE) data for the system of (water+formic acid+2-ethyl-1-hexanol) were experimentally determined at T=(298.2, 308.2, 318.2, and 328.2) K and atmospheric pressure. A type-2 LLE was obtained for this ternary system. The influence of temperature on the equilibrium characteristics was found to be smallat the temperatures studied. Distribution coefficients and separation factors were calculated over the immiscibility regions. The experimental tie-line data were correlated using the UNIQUAC model. The values of the interaction parameters between each pair of the components were obtained for this thermodynamic model. The root mean square deviation (RMSD) between the observed and calculated mass fractions was 0.61%.
[References]
Dramur U, Tatli B, J. Chem. Eng. Data. , 38 , 23, 1993
Briones JA, Mullins JC, Thies MC, Ind. Eng. Chem. Res. , 33 (1), 151, 1994
Zigova J, Sturdik E, J. Ind. Microbiol. Biotechnol. , 24 , 153, 2000
Hong YK, Hong WH, Han DH, Biotechnol. Bioprocess Eng. , 6 , 386, 2001
Arce A, Blanco A, Souza P, Vidal I, J. Chem. Eng. Data. , 38 , 201, 1993
Almuhtaseb SA, Fahim MA, Fluid Phase Equilib. , 123 (1-2), 189, 1996
Radwan GM, Almuhtaseb SA, Sep. Sci. Technol. , 32 (8), 1463, 1997
Ozmen D, J. Chem. Thermodyn. , 39 (1), 123, 2007
Senol A, Fluid Phase Equilib. , 243 (1-2), 51, 2006
Uslu H, Kirbaslar SI, Fluid Phase Equilib. , 287 (2), 134, 2010
Sahin S, Kirbaslar SI, Bilgin M, J. Chem. Thermodyn. , 41 (1), 97, 2009
Bilgin M, Arisoy C, Fluid Phase Equilib. , 250 (1-2), 59, 2006
Bartholome E, Biekert E, Hellmann H, Ley H, Ullmanns Encyklopadie der Technischen Chemie, 4. Auflage, Band 7, Verlag Chemie, Weinheim, 362, 1974
Kertes AS, King CJ, Biotechnol. Bioeng. , 28 , 269, 1986
Cai W, Zhu S, Piao X, J. Chem. Eng. Data. , 46 , 1472, 2001
Yang ST, White SA, Hsu ST, Ind. Eng. Chem. Res. , 30 , 1335, 1991
Senol A, J. Chem. Eng. Jpn. , 32 (6), 717, 1999
Senol A, Sep. Purif. Technol. , 21 (1-2), 165, 2000
Uslu H, Bayat C, Goekmen S, Yorulmaz Y, J. Chem. Eng. Data , 54 (1), 48, 2009
Leung RWK, Badakhshan A, Ind. Eng. Chem. Res. , 26 , 1593, 1987
BaslIoglu B, Cehreli, Fluid Phase Equilib. , 312 , 85, 2011
Senol A, Fluid Phase Equilib. , 227 (1), 87, 2005
Bilgin M, Birman I, Fluid Phase Equilib. , 302 (1-2), 249, 2011
Ince E, Kirbaslar SI, Sahin S, J. Chem. Eng. Data , 52 (5), 1889, 2007
Ozmen D, Fluid Phase Equilib. , 269 (1-2), 12, 2008
Abrams DS, Prausnitz JM, AIChE J. , 21 , 116, 1975
Treybal RE, Liquid extraction, McGraw-Hill: New York, 1963
Othmer DF, Tobias PE, Ind. Eng. Chem. , 34 , 690, 1942
Bachman I, Ind. Eng. Chem. Anal. Ed. , 12 , 38, 1940
Sorensen JM, Ph.D. Thesis, Technical University of Denmark, Lyngby, Denmark, 1980
Arce A, Blanco A, Martinezageitos J, Vidal I, Fluid Phase Equilib. , 93 , 285, 1994
Gilani HG, Golpour M, Ashraf SS, Fluid Phase Equilib. , 310 (1-2), 192, 2011
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