Development of non-woven fabric-based ECTFE membranes for direct contact membrane distillation application

被引:19
作者
Ursino, C. [1 ]
Ounifi, I. [2 ]
Di Nicolo, E. [3 ]
Cheng, X. Q. [4 ]
Shao, L. [5 ]
Zhang, Y. [4 ]
Drioli, E. [1 ]
Criscuoli, A. [1 ]
Figoli, A. [1 ]
机构
[1] CNR, Inst Membrane Technol ITM, Via P Bucci 17c, I-87036 Arcavacata Di Rende, CS, Italy
[2] Technopk Borj Cedria, Ctr Res & Water Technol, Lab Water Membrane & Environm Biotechnol, Technopk Borj Cedria,BP 273, Soliman 8020, Tunisia
[3] Solvay Specialty Polymers, Viale Lombardia 20, I-20021 Bollate, MI, Italy
[4] Harbin Inst Technol, Sino Europe Membrane Technol Res Inst, Sch Marine Sci & Technol, Weihai, Peoples R China
[5] Harbin Inst Technol, Sch Chem & Chem Engn, Harbin, Peoples R China
关键词
Coating; ECTFE; Direct contact membrane distillation; Desalination; Non-woven fabric; Salt rejection; HYDROPHOBIC/HYDROPHILIC COMPOSITE MEMBRANES; HOLLOW-FIBER MEMBRANE; POLYETHERSULFONE MEMBRANES; PERFLUOROPOLYETHER PFPE; TIPS METHOD; DESALINATION; PVDF; WATER; FLUX; SOLVENT;
D O I
10.1016/j.desal.2020.114879
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, a lower melting point of HALAR (R) Ethylene-Chlorotrifluoroethylene (LMP ECTFE) was used to prepare non-woven fabric-based porous membranes, using a polyester non woven (NWPET) as support, via dipcoating. Di-ethyl Adipate (DEA) and di-ethylene Glycol (DEG) were selected as primary and secondary diluent, respectively. SEM analyses showed that in all cases the coating layer was homogeneous, covering all the NWPET support and leading to an interconnected sponge-like microstructure. Membrane characterization evidenced the effects of the DEG concentration, which plays the role of pore former. The effect of the immersion time was examined and studied, too. The produced membranes were fully characterized in terms of water contact angle, porosity and pore size. Direct contact membrane distillation (DCMD) experiments using water and salty solution 0.6 M (NaCl) as feed, were performed for selected supported membranes. The obtained fluxes ranged between 3 and 22 kg/m(2)h, depending on DEG concentration, at the same immersion time, and on the feed temperatures (40-60 degrees C). Rejection (R%) was comprised from 94.95 to 99.82%. In particular, the N-ECTFE 7-0-7 membrane, with the highest R%, showed a stable deionized water flux before and after the experiments, indicating its ability to recover its original performance.
引用
收藏
页数:10
相关论文
共 63 条
[1]  
Alsebaeai MK, 2020, J IND ENG CHEM, V86, P13
[2]   Challenges and trends in membrane technology implementation for produced water treatment: A review [J].
Alzahrani, Salem ;
Mohammad, Abdul Wahab .
JOURNAL OF WATER PROCESS ENGINEERING, 2014, 4 :107-133
[3]   A novel Ru-polyethersulfone (PES) catalytic membrane for highly efficient and selective hydrogenation of furfural to furfuryl alcohol [J].
Bagnato, G. ;
Figoli, A. ;
Ursino, C. ;
Galiano, F. ;
Sanna, A. .
JOURNAL OF MATERIALS CHEMISTRY A, 2018, 6 (12) :4955-4965
[4]   Fluorinated Polymers as Smart Materials for Advanced Biomedical Applications [J].
Cardoso, Vanessa F. ;
Correia, Daniela M. ;
Ribeiro, Clarisse ;
Fernandes, Margarida M. ;
Lanceros-Mendez, Senentxu .
POLYMERS, 2018, 10 (02)
[5]   Recent progress in fluoropolymers for membranes [J].
Cui, Zhaoliang ;
Drioli, Enrico ;
Lee, Young Moo .
PROGRESS IN POLYMER SCIENCE, 2014, 39 (01) :164-198
[6]   Stable Superhydrophobic Ceramic-Based Carbon Nanotube Composite Desalination Membranes [J].
Dong, Yingchao ;
Ma, Lining ;
Tang, Chuyang Y. ;
Yang, Fenglin ;
Quan, Xie ;
Jassby, David ;
Zaworotko, Michael J. ;
Guiver, Michael D. .
NANO LETTERS, 2018, 18 (09) :5514-5521
[7]   Membrane distillation: Recent developments and perspectives [J].
Drioli, Enrico ;
Ali, Aamer ;
Macedonio, Francesca .
DESALINATION, 2015, 356 :56-84
[8]   The impact of hydrophobic coating on the performance of carbon nanotube bucky-paper membranes in membrane distillation [J].
Dumee, Ludovic ;
Campbell, Jos L. ;
Sears, Kallista ;
Schuetz, Juerg ;
Finn, Niall ;
Duke, Mikel ;
Gray, Stephen .
DESALINATION, 2011, 283 :64-67
[9]   A framework for better understanding membrane distillation separation process [J].
El-Bourawi, M. S. ;
Ding, Z. ;
Ma, R. ;
Khayet, M. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :4-29
[10]   Self-sustained webs of polyvinylidene fluoride electrospun nanofibers at different electrospinning times: 1. Desalination by direct contact membrane distillation [J].
Essalhi, M. ;
Khayet, M. .
JOURNAL OF MEMBRANE SCIENCE, 2013, 433 :167-179