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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) : 1581-1592    https://doi.org/10.1007/s11705-023-2327-7
RESEARCH ARTICLE
Enhanced activation of persulfate using mesoporous silica spheres augmented Cu–Al bimetallic oxide particles for bisphenol A degradation
Fulong Wang, Liang Sun(), Ziyu Zhang, Fengkai Yang, Jinlong Yang, Weijian Liu()
School of Environment and Safety Engineering, Qingdao University of Science and Technology, Qingdao 266042, China
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Abstract

Herein, Cu–Al bimetallic oxide was synthesized and mixed with mesoporous silica spheres via a simple hydrothermal method. The prepared sample was then analyzed and employed to activate potassium peroxydisulfate for bisphenol A removal. Based on the results of X-ray diffraction, scanning electron microscopy, and energy dispersion spectroscopy, Cu–Al bimetallic oxide was determined as CuO-Al2O3, and mesoporous silica spheres were found around the these particles. At 30 min, a bisphenol A degradation level of 90% was achieved, and it remained at over 60% after five consecutive cycles, indicating the catalyst’s superior capacity and stability. In terms of removal performance, the radical pathway (including SO4•‒, OH •, and O2•‒) and singlet oxygen (1O2) played minor roles, while electron migration between bisphenol A, potassium peroxydisulfate, and the catalyst played a dominant role. The introduction of Al2O3 promoted the formation of surface oxygen vacancies, which improved ligand complex formation between potassium peroxydisulfate and the catalyst, thereby facilitating electron migration. Furthermore, mesoporous silica spheres augment not only enhanced bisphenol A adsorption but also alleviated Cu leaching. Overall, this work is expected to provide significant support for the rational development of catalysts with high catalytic activity for persulfate activation via surface electron migration.

Keywords Cu–Al bimetallic oxides      mesoporous silica spheres      peroxydisulfate      bisphenol A     
Corresponding Author(s): Liang Sun,Weijian Liu   
Just Accepted Date: 26 May 2023   Online First Date: 11 July 2023    Issue Date: 07 October 2023
 Cite this article:   
Fulong Wang,Liang Sun,Ziyu Zhang, et al. Enhanced activation of persulfate using mesoporous silica spheres augmented Cu–Al bimetallic oxide particles for bisphenol A degradation[J]. Front. Chem. Sci. Eng., 2023, 17(10): 1581-1592.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-023-2327-7
https://academic.hep.com.cn/fcse/EN/Y2023/V17/I10/1581
Fig.1  XRD patterns of Cu–Al and Cu–Al/MSSs.
ItemMSSsCu–AlCu–Al/MSSs
The specific surface area/(m2·g?1)34.0256.2883.00
Pore volume/(cm3·g?1) 0.09 0.11 0.20
Pore size/nm10.41 3.05 4.95
Tab.1  The characterization data of the prepared materials
Fig.2  (a) Nitrogen sorption isotherms, and (b) the pore size distribution of MSSs, Cu–Al and Cu–Al/MSSs.
Fig.3  Micrographs images and EDS element distribution of (a) Cu–Al, and (b) Cu–Al/MSSs.
Fig.4  (a) The removal performances via different processes, and (b) the comparison of the apparent reaction rate constant between CuO/MSSs + PDS and Cu–Al/MSSs + PDS (conditions: [BPA] = 50 mg·L?1, [material] = 0.5 g·L?1, [PDS] = [H2O2] = 100 mmol·L?1, pH = neutral, temperature = 25 °C).
Fig.5  Effect of the initial pH on BPA removal: (a) the removal efficiency, and (b) the pseudo-first-order kinetic model (conditions: [BPA] = 50 mg·L?1, [Cu–Al/MSSs] = 0.5 g·L?1, [PDS] = 100 mmol·L?1, temperature = 25 °C).
Fig.6  The removal performances with (a) different catalyst amount after 30 min and (b) different PDS dosage after 30 min; (c) the effect of the reaction temperature on the BPA removal (inset showing plot of ln(k×102) versus 103/T); and (d) the reusability of Cu–Al and Cu–Al/MSSs (conditions: [BPA] = 50 mg·L?1, [catalyst] = 0.5 g·L?1 for (b), (c), and (d), [PDS] = 100 mmol·L?1 for (a), (c), and (d), pH = neutral, temperature = 25 °C for (a), (b), and (d)).
Fig.7  BPA removal in different scavenger systems: (a) the removal efficiency after 30 min, and (b) the apparent reaction rate constant k (conditions: [BPA] = 50 mg·L?1, [Cu–Al/MSSs] = 0.5 g·L?1, [PDS] = 100 mmol·L?1, [scavenger] = 100 mmol·L?1, pH = neutral, temperature = 25 °C); EPR spectra of the Cu–Al/MSSs + PDS system: (c) DMPO for OH? and SO4?? and (d) TEMP for 1O2.
Fig.8  (a) Cu 2p, and (b) O 1s for Cu–Al and Cu–Al/MSSs fresh and used for five cycles.
Fig.9  (a) LSV curves under different conditions, and (b) it curve of Cu–Al/MSSs (conditions: [BPA] = 50 mg·L?1, [Cu–Al/MSSs] = 0.5 g·L?1, [PDS] = 100 mmol·L?1, pH = neutral, temperature = 25 °C).
Fig.10  Mechanism scheme of BPA removal in Cu–Al/MSSs + PDS process.
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