Wet dispersion of graphene assisted constructing multiple interface pores of PVDF hollow fiber membranes via melt-spinning and stretching

被引:6
作者
Ji, Dawei [1 ,2 ]
Lin, Weijia [1 ,2 ]
Sun, Guangwu [1 ,2 ,3 ]
Tian, Xuyong [1 ,2 ]
Ma, Xixian [1 ,2 ]
Xiao, Changfa [1 ,2 ,4 ]
机构
[1] Shanghai Univ Engn Sci, Fiber Mat Res Ctr, Shanghai 201620, Peoples R China
[2] Shanghai Univ Engn Sci, Sch Text & Fash, Shanghai 201620, Peoples R China
[3] Hainan Vocat Univ Sci & Technol, Sch Mech & Elect Engn, Haikou 571126, Hainan, Peoples R China
[4] Tiangong Univ, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2023年 / 11卷 / 05期
基金
中国国家自然科学基金;
关键词
Solvent-free; Hollow fiber membranes; Wet dispersion; Multiple interface pores; Melt spinning; SOLVENT; WATER;
D O I
10.1016/j.jece.2023.110968
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this work, in order to further improve the permeability of poly(vinylidene fluoride) (PVDF) hollow fiber microfiltration membranes through melt-spinning and stretching (MS-S), we doped graphene (GE) in the forming membrane system of the previous work via wet dispersion and successfully prepared PVDF hollow fiber microfiltration membranes with multiple interface pores. GE could be uniformly dispersed and embedded in the PVDF matrix through the wet dispersion, which could obviously improve the interface layer between the matrix phase (PVDF) and the dispersed phase (GE) due to their poor compatibility of organic/inorganic phases. In addition, the stress concentration would be generated at the interface between GE and PVDF, which resulted in PVDF forking to many tiny fibers. Thus, the multiple interface pores between organic/organic (PVDF/polysulfone(PSf)) and organic/inorganic (PVDF/GE) phases could occur and be controlled precisely through the further stretching. The results showed that GE could improve the pore size and porosity of the prepared membranes obviously. In addition, the pore size of the prepared membranes could be controlled from 0.258 to 1.066 mu m by changing the stretching ratios. Accordingly, pure water flux increased from 174.5 to 2782.9 L m(-2) h(-1). Applied to filter the active sludge suspension, the prepared PVDF microfiltration membranes exhibited a high rejection (>99.5%), and the turbidity decreased obviously (<0.5 NTU). In particular, there were not any hazardous solvents used in the preparation process, which could achieve green preparation of PVDF membranes.
引用
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页数:7
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