Issue
Korean Journal of Chemical Engineering,
Vol.21, No.3, 693-698, 2004
Pervaporation of Esters with Hydrophobic Membrane
Surface-modified alumina membrane (Al2O3) was used for ester flavor recovery by pervaporation. This study focused on the permeation characteristics of ester compounds (ethyl acetate, EA; ethyl propionate, EP; ethyl butyrate, EB) through tube-type hydrophobic membrane. Experiments were performed to evaluate the effects of the feed concentration (0.15-0.60 wt%) and temperature (30-50 ℃) on separation of EA, EP, and EB from aqueous solutions. It was found that the permeation flux increased with increasing feed ester concentration and operating temperature. The fluxes of EA, EP, and EB at 0.60 wt% feed concentration and 40 ℃ were 254, 343, and 377 g/m2 hr, which was much higher than those of polymer membranes. It was reported that the permeate flux of EA with PDMS was 1.1-58 g/m2Þhr at feed concentration of 90-4,800 ppm and 45 ℃. The separation factors for the 0.15-0.60 wt% feed solution of EA, EP, and EB at 40 ℃ were in the range of 66.9-78.9, 106.5-97.3, and 120.5-122.8, respectively. Due to the high separation factor, phase separation occurred in permeate stream because the ester concentration in permeate was much above the saturation limit.
[References]
  1. Baker RW, Wijmans JG, Athayde AL, Daniels R, Ly JH, Le M, J. Membr. Sci., 137(1-2), 159, 1997
  2. Baudot A, Marin M, Trans. IChemE, 75, 117, 1997
  3. Baudot A, Marin M, Ind. Eng. Chem. Res., 38(11), 4458, 1999
  4. Baudot A, Souchon I, Marin M, J. Membr. Sci., 158(1-2), 167, 1999
  5. Beaumelle D, Marin M, Chem. Eng. Process., 33(6), 449, 1994
  6. Charalambous G, Inglett GE, "Flavor of Foods and Beverages, Chemistry and Technology," New York, 1978
  7. Choi SG, Cho MS, Kim JH, Kim SJ, Han NW, HWAHAK KONGHAK, 37(2), 243, 1999
  8. Djebbar MK, Nguyen QT, Clement R, Germain Y, J. Membr. Sci., 146(1), 125, 1998
  9. Feng XS, Huang RY, J. Membr. Sci., 118(1), 127, 1996
  10. Song KM, Hong YK, Yu J, Hong WH, Korean J. Chem. Eng., 19(2), 290, 2002
  11. Heath HB, Pharm B, "Flavor Technology," AVI, London, 1978
  12. Ho CT, Tan CT, Tong CH, "Flavor Technology, Physical Chemistry, Modification, and Process," American Chemical Society, 1995
  13. Howell JA, Sanchez V, Field RW, "Membrane in Bioprocessing Theory and Application," Chapman & Hall, 1993
  14. Joao I, Crespo G, Boddeker KW, "Pervaporation, Removal of Organics from Water and Organic/Organic Separations, Membrane Processes in Separation and Purification," Netherlands, 1993
  15. Won JM, Bae SY, Ha BH, Kim HT, Dumazawa H, Korean J. Chem. Eng., 13(3), 324, 1996
  16. Mulder M, "Basic Principles of Membrane Technology," Kluwer, 2nd Ed., Netherlands, 1991
  17. Olsson J, Tragardh G, J. Membr. Sci., 187(1-2), 23, 2001
  18. Rajagopalan N, Cheryan M, J. Membr. Sci., 104(3), 243, 1995
  19. Ren JZ, Jiang CZ, J. Membr. Sci., 140(2), 221, 1998
  20. Sampranpiboon P, Jiraratananon R, Uttapap D, Feng X, Huang RYM, J. Membr. Sci., 173(1), 53, 2000
  21. Yeom CK, Dickson JM, Brook MA, Korean J. Chem. Eng., 13(5), 482, 1996