Investigation of amphoteric polybenzimidazole (PBI) nanofiltration hollow fiber membrane for both cation and anions removal

被引:57
作者
Lv, Junwen [1 ]
Wang, Kai Yu [1 ]
Chung, Tai-Shung [1 ]
机构
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore, Singapore
关键词
nanofiltration; hollow fiber; polybenzimidazole; amphoteric; ion separation;
D O I
10.1016/j.memsci.2007.11.050
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The removal of both anions (phosphate, arsenate, arsenite and borate ions) and cations (copper ions) has been investigated by employing a lab-developed amphoteric polybenzimidazole (PBI) nanofiltration (NF) hollow fiber membrane. The amphoteric characteristics are due to the imidazole group within PBI molecules that makes the PBI NF membrane have an isoelectric point near pH 7.0 and show different charge signs based on the media pH. Investigations on the rejection capability of typical anions, e.g. phosphate, arsenate, arsenite, borate anions and typical heavy metal cations, e.g. copper ions, reveal that the PBI NF membrane exhibits impressive rejection performance for various ions removal. However, their rejections are strongly dependent on the chemical nature of electrolytes, solution pHs and the feed concentrations. The experimental results are analyzed by using the Spiegler-Kedem model with the transport parameters of the reflection coefficient (sigma) and the solute permeability (P). The PBI NF membrane may have potential to be used in industrial removal of various environmentally unfriendly ion species. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:557 / 566
页数:10
相关论文
共 47 条
[1]  
Abu Qdais H, 2004, DESALINATION, V164, P105
[2]   Adsorption characteristics of As(III) and As(V) with titanium dioxide loaded amberlite XAD-7 resin [J].
Balaji, T ;
Matsunaga, H .
ANALYTICAL SCIENCES, 2002, 18 (12) :1345-1349
[3]   Transport coefficients cadmium salt rejection in nanofiltration membrane [J].
Ballet, GT ;
Gzara, L ;
Hafiane, A ;
Dhahbi, M .
DESALINATION, 2004, 167 (1-3) :369-376
[4]   An empirical model for kinetics of boron removal from boron-containing wastewaters by ion exchange in a batch reactor [J].
Boncukcuoglu, R ;
Yilmaz, AE ;
Kocakerim, MM ;
Çopur, M .
DESALINATION, 2004, 160 (02) :159-166
[5]  
Chu KH, 2000, J CHEM TECHNOL BIOT, V75, P1054, DOI 10.1002/1097-4660(200011)75:11<1054::AID-JCTB315>3.0.CO
[6]  
2-T
[7]   The effects of current density and phosphate concentration on phosphate removal from wastewater by electrocoagulation using aluminum and iron plate electrodes [J].
Irdemez, Sahset ;
Demircioglu, Nuhi ;
Yildiz, Yalcin Sevki ;
Bingul, Zuleyha .
SEPARATION AND PURIFICATION TECHNOLOGY, 2006, 52 (02) :218-223
[8]   The removal of copper and nickel from aqueous solution using Y zeolite ion exchangers [J].
Keane, MA .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 1998, 138 (01) :11-20
[9]   THERMODYNAMIC ANALYSIS OF THE PERMEABILITY OF BIOLOGICAL MEMBRANES TO NON-ELECTROLYTES [J].
KEDEM, O ;
KATCHALSKY, A .
BIOCHIMICA ET BIOPHYSICA ACTA, 1958, 27 (02) :229-246
[10]   Porous hydrophobic/hydrophilic composite membranes - Application in desalination using direct contact membrane distillation [J].
Khayet, M ;
Mengual, JI ;
Matsuura, T .
JOURNAL OF MEMBRANE SCIENCE, 2005, 252 (1-2) :101-113