Rigorous modelling and optimization of hybrid separation processes based on pervaporation

Katalin Koczka, Peter Mizsey, Zsolt Fonyo

Research output: Contribution to journalArticle

23 Citations (Scopus)

Abstract

Hybrid separation processes are becoming more and more important in the practice if membrane technologies are also involved. In this work, a systematic investigation is completed for three sequence alternatives of distillation and pervaporation. These are the following: pervaporation followed with distillation (PV+D), distillation followed with pervaporation (D+PV), two distillation columns and a pervaporation unit between them (D+PV+D). The hybrid separation process alternatives are evaluated with rigorous modelling tools, but first, a rigorous simulation algorithm is determined for the pervaporation. The three hybrid separation processes are rigorously modelled with CHEMCAD, and optimized with the dynamic programming optimization method for the case of the separation of ethanol-water mixture. The objective function is the total annual cost (TAC). The energy consumption is also investigated. The selection of the ethanol-water mixture has two motivations: (i) it is quite often studied and well known, and (ii) to make biofuel (ethanol) production more economical, membrane technologies might also be applied. The results are compared with each other and with the classical separation completed with heteroazeotropic distillation. The optimized TAC shows that the distillation column followed with pervaporation is the most economical hybrid separation process alternative. Its TAC is about 66% of that of the classical separation.

Original languageEnglish
Pages (from-to)1124-1147
Number of pages24
JournalCentral European Journal of Chemistry
Volume5
Issue number4
DOIs
Publication statusPublished - Dec 1 2007

Keywords

  • CHEMCAD
  • Hybrid separation processes

ASJC Scopus subject areas

  • Chemistry(all)
  • Materials Chemistry

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