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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

Postal Subscription Code 80-969

2018 Impact Factor: 2.809

Front. Chem. Sci. Eng.    2023, Vol. 17 Issue (10) : 1450-1459    https://doi.org/10.1007/s11705-023-2310-3
RESEARCH ARTICLE
Synthesis of novel magneto-hybrid polyoxometalate composite membrane with simultaneous photocatalytic self-cleaning and antifouling functionalities
Nee Nee Tan1, Qi Hwa Ng1,2(), Siti Kartini Enche Ab Rahim1,2, Abdul Latif Ahmad3, Peng Yong Hoo1,2, Thiam Leng Chew4,5
1. Faculty of Chemical Engineering & Technology, Universiti Malaysia Perlis (UniMAP), Perlis 02600, Malaysia
2. Centre of Excellent for Frontier Materials Research, Universiti Malaysia Perlis (UniMAP), Perlis 02600, Malaysia
3. School of Chemical Engineering, Engineering Campus, Universiti Sains Malaysia, Penang 14300, Malaysia
4. Department of Chemical Engineering, Faculty of Engineering, Universiti Teknologi PETRONAS, Perak 32610, Malaysia
5. CO2 Research Centre (CO2RES), Institute of Contaminant Management, Universiti Teknologi PETRONAS, Perak 32610, Malaysia
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Abstract

Membrane technology is ideal for removing aqueous humic acid, but humic acid deposits cause membrane fouling, a significant challenge that limits its application. Herein, this work proposed an alternative approach to the controllably magnetically induced magneto-hybrid polyoxometalate (magneto-HPOM) nanocomposite migration toward the polyethersulfone (PES) membrane surface under a magnetic field to enhance the self-cleaning and antifouling functionalities of the membrane. Before incorporating magneto-HPOM nanocomposite into the PES casting solution, functionalized magnetite nanoparticles (F-MNP) were first coated with HPOM photocatalyst to fabricate a magneto-HPOM-PES membrane. It was shown that the apparent impacts of this novel magneto-HPOM-PES membrane on the hydrophilic behavior and photocatalytic properties of the magneto-HPOM nanocomposite improve the hydrophilicity, separation performance, antifouling and self-cleaning properties of the membrane compared with neat PES membrane. Furthermore, after exposure to ultraviolet light, the magneto-HPOM-PES membrane can be recovered after three cycles with a flux recovery ratio of 107.95%, 100.06%, and 95.56%, which is attributed to the temporal super hydrophilicity effect. Meanwhile, the magneto-HPOM-PES membrane could efficiently maintain 100% humic acid rejection for the first and second cycles and 99.81% for the third cycle. This study revealed a novel approach to fabricating membranes with high antifouling and self-cleaning properties for water treatment.

Keywords magneto-hybrid polyoxometalate nanocomposite      composite membrane      antifouling      self-cleaning      magnetic and photocatalytic responsiveness     
Corresponding Author(s): Qi Hwa Ng   
Just Accepted Date: 24 April 2023   Online First Date: 07 June 2023    Issue Date: 07 October 2023
 Cite this article:   
Nee Nee Tan,Qi Hwa Ng,Siti Kartini Enche Ab Rahim, et al. Synthesis of novel magneto-hybrid polyoxometalate composite membrane with simultaneous photocatalytic self-cleaning and antifouling functionalities[J]. Front. Chem. Sci. Eng., 2023, 17(10): 1450-1459.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-023-2310-3
https://academic.hep.com.cn/fcse/EN/Y2023/V17/I10/1450
Fig.1  FESEM images and EDX analysis of the (a, b) HPOM, (c, d) F-MNP, (e, f) magneto-TiO2 and (g, h) magneto-HPOM.
Fig.2  Photocatalytic degradation of the HA solution with different types of photocatalysts.
Fig.3  Linear plot of ln(C0Ct) against the time of various photocatalysts.
Fig.4  ATR-FTIR spectra of neat PES membrane (curve A) and magneto-HPOM-PES membrane (curve B) in the range of (a) 650 to 4000 cm?1 and (b) 650 to 1700 cm?1.
Membrane typeContact angle/(° )
15 wt % PES66.81±7.80
Magneto-HPOM-PES53.24±2.86
Tab.1  Contact angle analysis of the prepared membranes
Fig.5  Normalized flux profiles of the fabricated membrane (region A represents initial pure water, region B represents filtration HA solution, region C represents cleaning with distilled water, and region D represents cleaning with UV light plus distilled water).
Fig.6  Fouling resistance of fabricated membranes.
Fig.7  Normalized flux profile of magneto-HPOM-PES membrane for the 3 cycle experiments (region A represents the initial pure water, region B represents the filtration HA solution, region C represents the cleaning with distilled water, and region D represents cleaning with UV light plus distilled water).
Fig.8  Cyclic experiments of the magneto-HPOM-PES membrane toward the FRR.
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