RT Journal Article T1 Studies on pervaporation separation of acetone, acetonitrile and ethanol from aqueous solutions A1 Khayet Souhaimi, Mohamed A1 Cojocaru, C. A1 Zakrzewska-Tunadel, G. AB Pervaporation is applied for acetone, acetonitrile and ethanol removal from water solutions. The separation of binary acetone-water, acetonitrile-water and ethanol-water mixtures was initially carried out. The effects of feed concentration and feed temperature on the pervaporation performance, total and partial permeate fluxes as well as organic selectivity, have been investigated. The overall mass transfer coefficients have been determined and discussed for each organic-water mixture at different conditions of feed temperature and initial organic feed concentrations. The overall and individual activation energies of water and each organic compound associated to the permeation process have been calculated. Finally, pervaporation was applied to wastewater solutions containing acetone, acetonitrile and ethanol at a temperature of 40 degrees C. The organic selectivity was found to be in the order of acetone > acetonitrile > ethanol. PB Elsevier Science BV SN 1383-5866 YR 2008 FD 2008-10-22 LK https://hdl.handle.net/20.500.14352/51165 UL https://hdl.handle.net/20.500.14352/51165 LA eng NO [1] P.A. Kober, Pervaporation, perstillation and percrystallization, J. Am. Chem. Soc. 39 (1917) 944–948.[2] R.C. Binning, R.J. Lee, Separation of azeotropic mixtures, U.S. Patent 2,953,502 (September 20, 1960).[3] R.Y.M. Huang, Pervaporation Membrane Separation Processes, Membrane Science and Technology Series 1, Elsevier, New York, 1991.[4] T. Matsuura, Synthetic Membranes and Membrane Separation Processes, CRC Press, Boca Raton, FL, 1993.[5] M. Khayet, J.P.G. Villaluenga, M.P. Godino, J.I. Mengual, B. Seoane, K.C. Khulbe, T. Matsuura, Preparation and application of dense poly(phenylene oxide) membranes in pervaporation, J. Colloid Interface Sci. 278 (2004) 410–422.[6] S.K. Ray, S.B. Sawant, J.B. Joshi, V.G. Pangarkar, Development of new synthetic membranes for separation of benzene–cyclohexane mixtures by pervaporation: a solubility parameter approach, Ind. Eng. Chem. Res. 36 (12) (1997) 5265–5276.[7] F. Liu, L. Liu, X. Feng, Separation of acetone–butanol–ethanol (ABE) from dilute aqueous solutions by pervaporation, Sep. Purif. Technol. 42 (2005) 273–282.[8] M. Khayet, T. Matsuura, Surface modification of membranes for the separation of volatile organic compounds from water by pervaporation, Desalination 148 (2002) 31–37.[9] M. Khayet, G. Chowdhury, T. Matsuura, Surface modification of polyvinylidene fluoride pervaporation membranes, AIChE J. 48 (2002) 2833–2843.[10] T. Masuda, M. Takatsuka, B. Tang, T. Higashimura, Pervaporation of organic–liquid–water mixtures through substituted polyacetylene membranes, J. Membr. Sci. 49 (1990) 69–83.[11] M. Zhou, M. Persin, J. Sarrazin, Methanol removal from organic mixtures by pervaporation using polypyrrole membranes, J. Membr. Sci. 117 (1996) 303–309.[12] M. Khayet, T. Matsuura, Pervaporation and vacuum membrane distillation processes: modeling and experiments, AIChE J. 50 (2004) 1697–1712.[13] M. Khayet, M.M. Nasef, J.I. Mengual, Radiation grafted poly(ethylene terephthalate)-graft-polystyrene pervaporation membranes for organic/organic separation, J. Membr. Sci. 263 (2005) 77–95.[14] S. Ray, S.K. Ray, Effect of copolymer type and composition on separation characteristics of pervaporation membranes—a case study with separation of acetone–water mixtures, J. Membr. Sci. 270 (2006) 73–87.[15] Q. Liu, R.D. Noble, J.L. Falconer, H.H. Funke, Organics/water separation by pervaporation with a zeolite membrane, J. Membr. Sci. 117 (1996) 163–174.[16] A.M. Urtiaga, E.D. Gorri, J.K. Beasley, I. Ortiz, Mass transfer analysis of the pervaporative separation of chloroform from aqueous solutions in hollow fibers devices, J. Membr. Sci. 156 (1999) 275.[17] A.M. Gronda, S. Buechel, E.L. Cussler, Mass transfer in corrugated membranes, J. Membr. Sci. 165 (2000) 177. NO © 2008 Elsevier B.V. This work was financially supported by FP6 European Funds under Marie Curie project: AMERAC no. MTKD-CT-2004-509226. The authors gratefully acknowledge this financial support. NO Unión Europea. FP6 DS Docta Complutense RD 28 abr 2024