Construction of a gelatin scaffold with water channels for preparing a high performance nanofiltration membrane

被引:36
作者
Lan, Hongling [1 ]
Li, Pengfei [1 ]
Wang, Hao [1 ]
Wang, Ming [1 ]
Jiang, Chi [1 ]
Hou, Yingfei [1 ]
Li, Peng [1 ]
Niu, Q. Jason [1 ,2 ]
机构
[1] China Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
[2] Shenzhen Univ, Inst Adv Study, Shenzhen 518060, Peoples R China
基金
中国国家自然科学基金;
关键词
Nanofiltration membrane; Gelatin scaffold; Water channel; High permeability; High selectivity; FILM COMPOSITE MEMBRANES; INTERFACIAL POLYMERIZATION; POLYAMIDE MEMBRANES; FABRICATION; LAYER; SEPARATION; INTERLAYER; REJECTION; TRANSPORT; STRATEGY;
D O I
10.1016/j.seppur.2021.118391
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In order to realize energy saving and resource recovery in desalination and waste-water treatment, it is urgent to develop nanofiltration (NF) membranes with high permeability and selectivity. Therefore, many researchers devote to designing different hydrophilic polymer-interlayers for the thin-film composite (TFC) membranes, targeting to prepare NF membranes with outstanding separation performance. However, the thin polymerinterlayer (<10 nm) can only slow down the diffusion rate of aqueous monomer and affect the interfacial polymerization (IP) process, forming a thin and defect-free polyamide (PA) layer. Herein, we constructed a hydrophilic and homogeneous gelatin (GT) scaffold with a thickness of over 100 nm on polysulfone (PSF) substrate and prepared a PA separation layer by IP process to obtain a high-performance TFC based NF membrane. The scaffold can not only affect the diffusion rate of piperazing (PIP) in IP process to form a thin PA layer, but also provide additional channels for water diffusion, which would significantly improve the permeability of NF membranes. Moreover, the fabricated PA layer has a high cross-linking degree and a negative surface potential, endowing the NF membrane with a high salts rejection rate, especially for divalent anions. Hence the permeability of the resulting NF membrane (up to 16.95 +/- 1.18 L m(-2) h(-1) bar(-1)) is about 2.5 times as compared with the controlled membrane, while achieving a high Na2SO4 rejection of 99.3% +/- 0.2%. In addition, the coefficient of selectivity for NF membrane are 97.73 for alpha(NaCl/Na2SO4) and 45.66 for alpha(NaCl/MgSO4) respectively, which are several times higher than those of the controlled NF membrane. This work provides a low-cost and facile method to prepare a TFC based NF membrane with a high permeability and selectivity.
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页数:8
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