Scalable dual-layer PVDF loose nanofiltration hollow fiber membranes for treating textile wastewater

被引:16
|
作者
Wang, Chuanfeng [1 ]
Chen, Yingbo [1 ]
Hu, Xiaoyu [2 ]
Guo, Pengfei [1 ]
机构
[1] Tiangong Univ, Sch Mat Sci & Engn, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
[2] Tianjin Motimo Membrane Technol Co Ltd, State Key Lab Membrane Mat & Membrane Applicat, Tianjin 300042, Peoples R China
关键词
Hollow fiber membrane; Loose nanofiltration; Dual-layer membrane; Phase inversion; Dye/salt separation; STEP SPINNING PROCESS; NF MEMBRANE; EFFECTIVE FRACTIONATION; HALLOYSITE NANOTUBES; COMPOSITE MEMBRANE; PHASE INVERSION; DYES; FABRICATION; SEPARATION; SALTS;
D O I
10.1016/j.jwpe.2022.102579
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A dual-layer (DL) PVDF loose nanofiltration (NF) hollow fiber membrane (HFM) with desirable properties was designed via phase inversion process using a continuous online-coating device. By fine-tuning dope formulation and fiber formation, the PVDF coating layer with NF separation capabilities was formed on the shell side of porous matrix-reinforced hollow fiber support while making fiber continuously. The effects of several parameters (e.g., LiCl content, co-solvent ratio (i.e., DMAc:THF) and air-bath distance (evaporation time)) on structures and properties were investigated to manipulate membrane MWCO. It was found that the introduction of volatile co-solvent and the control of evaporation time helped to significantly reduce the PVDF selective layer's thickness. The structure along with performance of the HFM demonstrated the DL ultrafiltration (UF) HFM could be successfully converted into NF HFM only by adjusting the parameters in the production system. After optimizing both phase inversion parameters and coating conditions, the resultant loose NF HFM presented a low MWCO of 1530 Da and a high pure water flux (PWF) of 14.2 L.m(-2).h(-1).bar(-1). Meanwhile, the HFM showed competitive dyes rejection (i.e., 99.9% for Rose bengal and Eriochrome black T, 96.5% for Methylene blue) and low NaCl rejection (3.2%). Furthermore, the prepared membrane also presented good stability and high flux recovery during a continuous NF process. This work provided a simple and economical strategy for engineering scalable loose NF HFM for dye purification.
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页数:16
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