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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 (2) : 236-248    https://doi.org/10.1007/s11705-022-2193-8
RESEARCH ARTICLE
Fluoride ions adsorption from water by CaCO3 enhanced Mn–Fe mixed metal oxides
Xinyuan Wang1, Heriberto Pfeiffer2, Jiangjiang Wei1, Jinyu Wang1(), Jinli Zhang1,3()
1. School of Chemistry and Chemical Engineering/Key Laboratory for Green Processing of Chemical Engineering of Xinjiang Bingtuan, Shihezi University, Shihezi 832003, China
2. Institute of Materials, National Autonomous University of Mexico, Mexico City 04510, Mexico
3. School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China
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Abstract

Novel CaCO3-enhanced Mn–Fe mixed metal oxides (CMFC) were successfully prepared for the first time by a simple-green hydrothermal strategy without any surfactant or template combined with calcination process. These oxides were then employed as an adsorbent for adsorptive removal of excess fluoride ions. The adsorbent was characterized by SEM, XPS, XRD, FTIR, and BET analysis techniques. The adsorption property of CMFC toward fluoride ion was analyzed by batch experiments. In fact, CMFC exhibited adsorption capacity of 227.3 mg∙g‒1 toward fluoride ion. Results showed that ion exchange, electrostatic attraction and chemical adsorption were the main mechanism for the adhesion of large amount of fluoride ion on the CMFC surface, and the high adsorption capacity responded to the low pH of the adsorption system. When the fluoride ion concentration was increased from 20 to 200 mg∙L‒1, Langmuir model was more in line with experimental results. The change of fluoride ion adsorption with respect to time was accurately described by pseudo-second-order kinetics. After five cycles of use, the adsorbent still maintains a performance of 70.6% of efficiency, compared to the fresh adsorbent. Therefore, this material may act as a potential candidate for adsorbent with broad range of application prospects.

Keywords mesoporous materials      metal oxides      fluoride ion      adsorption mechanism     
Corresponding Author(s): Jinyu Wang,Jinli Zhang   
About author:

Changjian Wang and Zhiying Yang contributed equally to this work.

Online First Date: 11 October 2022    Issue Date: 27 February 2023
 Cite this article:   
Xinyuan Wang,Heriberto Pfeiffer,Jiangjiang Wei, et al. Fluoride ions adsorption from water by CaCO3 enhanced Mn–Fe mixed metal oxides[J]. Front. Chem. Sci. Eng., 2023, 17(2): 236-248.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-022-2193-8
https://academic.hep.com.cn/fcse/EN/Y2023/V17/I2/236
Fig.1  (a) XRD patterns, (b) N2 adsorption−desorption isotherms, and (c) BJH pore-size distribution curves of the MFC and CMFC samples; (d) the pHZPC data of the CMFC.
Sample 2θ/(° ) FWHM D/nm(Scherrer equation) d/nmBragg’s Law
Standard-Fe2O3 35.611
MFC-Fe2O3 35.682 0.320 28.99 0.250
CMFC-Fe2O3 35.662 0.212 43.76 0.250
Standard-Mn2O3 32.951
CMFC-Mn2O3 33.092 0.431 19.02 0.270
Standard-CaCO3 29.400
MFC-CaCO3 29.586 0.239 34.01 0.302
CMFC-CaCO3 29.525 0.212 38.34 0.302
Tab.1  Crystal size parameters (XRD)
Sample SBET/(m2?g?1) Pore volume/(cm3?g–1) Average pore size/nm
MFC 10.7 0.0502 15.7
CMFC 17.3 0.0874 16.8
Tab.2  Textural parameters of samples obtained by BET and BJH models from the N2 adsorption–desorption technique
Fig.2  SEM images of (a) the MFC and (b) CMFC samples; (c–e) HRTEM images and (f) EDX mapping results for the CMFC sample.
Fig.3  (a) XRD pattern, (b) secondary electron images and (c) EDX mapping results for the FCMFC sample.
Adsorbent Qmax/(mg?g?1) Ref.
MIL-100(Fe) 23.53 [30]
Hydroxyapatite/sodium alginate 50.00 [31]
MIL-101(Al) 62.20 [32]
zinc-zirconium oxide 107.41 [33]
Fe-modified MgO 135.10 [34]
Zr MOFs 204.08 [35]
CMFC 227.27 This work
Tab.3  Fluoride ion adsorption capacity of various adsorbents reported in literature
Fig.4  Effects of (a) CMFC concentration, (b) the initial pH value, and (c) coexisting metal ions on fluoride ion adsorption; (d) fluoride ion adsorption performance of CMFC during five adsorption–regeneration cycles.
Fig.5  (a) Fluoride ion adsorption isotherms on CMFC samples (adsorbent dosage = 0.5 g?L?1, T = 298 K, contact time = 24 h, pH = 7), and (b) Langmuir and (c) Freundlich isothermal modeling; (d) adsorption kinetics of CMFC samples towards fluoride ion (adsorbent dosage = 0.5 g?L?1, initial fluoride ion concentration = 100 mg?L?1, T = 298 K, pH = 7), and (e) pseudo-first-order and (f) pseudo-second-order fitting models.
Sample Langmuir Freundlich
qmax/(mg?g?1) KL R2 KF 1/n R2
CMFC 227.27 0.015 0.9603 6.7298 0.6688 0.9410
Tab.4  Parameters of the Langmuir and Freundlich isothermal models for fluoride ion adsorption on the CMFC sample
Sample qe/(mg?g?1) Pseudo-first-order Pseudo-second-order
K1 R2 K2 R2
CMFC 104.19 0.0616 0.9808 0.0088 0.9876
Tab.5  Fluoride ion adsorption kinetics parameters of pseudo-first- and pseudo-second-order kinetics models
Fig.6  FTIR spectra of the initial samples (MFC and CMFC), and the sample after the fluoride ion adsorption process (FCMFC).
Fig.7  (a) XPS survey spectra of the CMFC and FCMFC samples; (b) XPS F 1s spectrum of the CMFC after fluoride ion adsorption; XPS (c) O 1s, (d) Ca 2p, (e) Mn 2p, and (f) Fe 2p spectra of the CMFC sample, before and after fluoride ion adsorption.
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