Separation of butanol from ABE mixtures by sweep gas pervaporation using a supported gelled ionic liquid membrane: Analysis of transport phenomena and selectivity


Plaza A., Merlet G., Hasanoglu A. M., Isaacs M., Sanchez J., Romero J.

JOURNAL OF MEMBRANE SCIENCE, cilt.444, ss.201-212, 2013 (SCI-Expanded) identifier identifier

  • Yayın Türü: Makale / Tam Makale
  • Cilt numarası: 444
  • Basım Tarihi: 2013
  • Doi Numarası: 10.1016/j.memsci.2013.04.034
  • Dergi Adı: JOURNAL OF MEMBRANE SCIENCE
  • Derginin Tarandığı İndeksler: Science Citation Index Expanded (SCI-EXPANDED), Scopus
  • Sayfa Sayıları: ss.201-212
  • Anahtar Kelimeler: Pervaporation, Butanol, Supported liquid membranes, Gelled ionic liquid, Mass transfer, DILUTE AQUEOUS-SOLUTIONS, ETHANOL ABE, MASS-TRANSFER, TRANSESTERIFICATION REACTION, IMMOBILIZED CELLS, N-BUTANOL, EXTRACTION, ACETONE, FERMENTATION, RECOVERY
  • Yıldız Teknik Üniversitesi Adresli: Evet

Özet

The separation of acetone butanol ethanol mixtures (ABE) from aqueous solutions, which are produced in ABE fermentation processes, is carried out by sweep gas pervaporation using gelled supported ionic liquid membranes and by membrane evaporation. The membranes were synthesized by the gelation of an ionic liquid ([bmim][PF6]) into the porosity of polytetrafluoroethylene (PTFE) hollow fibers. The performance of the membranes used in sweep gas pervaporation is compared with the membrane evaporation process using the same hollow fiber support without IL in order to verify the selectivity contributed by the gelled ionic liquid gap formed in the membrane pores. Improved butanol/ethanol selectivity was verified for gelled IL membranes in pervaporation experiments compared to the evaporation process. A resistance-in-series model was developed to simulate the pervaporation process. The model predictions were in good agreement with the experimental results. IL membranes are found to have potential for separation of butanol from the ABE mixtures by pervaporation. (C) 2013 Elsevier B.V. All rights reserved.