Modelling of Hybrid Method for VOC Removal from Process Wastewater: Distillation and Hydrophilic Pervaporation

被引:7
作者
Szilagyi, Botond [1 ]
Do Thi Huyen Trang [1 ]
Fozer, Daniel [1 ]
Selim, Asmaa [1 ,2 ]
Haaz, Eniko [1 ]
Toth, Andras Jozsef [1 ,3 ]
机构
[1] Budapest Univ Technol & Econ, Environm & Proc Engn Res Grp, Dept Chem & Environm Proc Engn, Fac Chem Technol & Biotechnol, POB 91, H-1521 Budapest, Hungary
[2] Natl Res Ctr, Dept Chem Engn & Pilot Plant, 33 El Buhouth St, Cairo 12622, Egypt
[3] Univ Miskolc, Inst Chem, POB 21, H-3513 Miskolc, Egyetemvaros, Hungary
关键词
ethanol and methanol removal; process wastewater; hydrophilic pervaporation; mathematical modelling; computer simulation; HIGHLY NONIDEAL MIXTURES; ORGANOPHILIC PERVAPORATION; ORGANIC MIXTURES; SEPARATION; MEMBRANES; ETHANOL; WASTEWATERS; PERMEATION; SIMULATION;
D O I
10.3311/PPch.15190
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The study is motivated by the industrial problem from pharmaceutical industry, which is ethanol and methanol removal from process wastewater. To complete this goal hybrid method is investigated and optimized. Two distillation columns are sufficient for separation of alcohol-water mixture. Suitable water can be purified as bottom product of first column. Ethanol and methanol purification is achieved with combination of second distillation column and pervaporation. The target of this research is to rigorously model and optimize the separation of water-ethanol-methanol ternary mixture in professional flowsheet simulator environment. The minimal sufficient membrane transfers area and number of minimal theoretical stages of the columns are determined. Cost estimation is also investigated according to Douglas methodology. Considering the simulation and economic results it can be determined that, the hybrid configuration is suitable for separation of ternary mixture in 99.5 weight percent purity.
引用
收藏
页码:364 / 370
页数:7
相关论文
共 49 条
  • [1] Distillation contra pervaporation: Comprehensive investigation of isobutanol-water separation
    Andre, Anita
    Nagy, Tibor
    Toth, Andras Jozsef
    Haaz, Eniko
    Fozer, Daniel
    Tarjani, Janka Ariella
    Mizsey, Peter
    [J]. JOURNAL OF CLEANER PRODUCTION, 2018, 187 : 804 - 818
  • [2] [Anonymous], 1990, MEMBR SCI TECHNOL SE
  • [3] [Anonymous], PERVAPORATION
  • [4] [Anonymous], INVENTORY INDEX FACT
  • [5] [Anonymous], IND ECOL
  • [6] Effect of protein on flux and selectivity in pervaporation of ethanol from a dilute solution
    Aroujalian, A
    Belkacemi, K
    Davids, SJ
    Turcotte, G
    Pouliot, Y
    [J]. SEPARATION SCIENCE AND TECHNOLOGY, 2003, 38 (12-13) : 3239 - 3247
  • [7] Baker R.W., 2012, Membrane Technology and Applications, DOI [10.1002/0470020393, DOI 10.1002/0470020393]
  • [8] Pervaporation of organic/water mixtures through B-ZSM-5 zeolite membranes on monolith supports
    Bowen, TC
    Kalipcilar, H
    Falconer, JL
    Noble, RD
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2003, 215 (1-2) : 235 - 247
  • [9] Removal of aromatics from multicomponent organic mixtures by pervaporation using polyurethane membranes: experimental and modeling
    Cunha, VS
    Paredes, MLL
    Borges, CP
    Habert, AC
    Nobrega, R
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2002, 206 (1-2) : 277 - 290
  • [10] DEVINE KM, 1995, SEVENTH INTERNATIONAL CONFERENCE ON PERVAPORATION PROCESSES IN THE CHEMICAL INDUSTRY, PROCEEDINGS OF, P218