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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

邮发代号 80-973

2018 Impact Factor: 3.883

Frontiers of Environmental Science & Engineering  2019, Vol. 13 Issue (5): 71   https://doi.org/10.1007/s11783-019-1151-2
  本期目录
Adsorption of phosphate on magnetite-enriched particles (MEP) separated from the mill scale
Muhammad Kashif Shahid1, Yunjung Kim2, Young-Gyun Choi1()
1. Department of Environmental Engineering, Chungnam National University, Daejeon 34134, Republic of Korea
2. Mechanical Process Research Group, Engineering Center, POSCO E&C, Incheon 220099, Republic of Korea
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Abstract

MEP were separated from mill scale at low magnetic intensity i.e., 300 to 500 gauss.

The phosphate adsorption capacity of MEP was determined 6.41 mg/g.

MEP packed-bed columns were successfully regenerated with alkaline solution.

Phosphate is a major pollutant in water, causing serious environmental and health consequences. In present study, the phosphate adsorption on novel magnetite-enriched particles (MEP) was comprehensively investigated. A new method and device were introduced for the separation of MEP from the mill scale at low magnetic intensity. Particles were characterized with different techniques such as XRD, XRF, SEM and EDS. The XRD and XRF analysis of MEP identified the dominant existence of crystalline magnetite. Furthermore, the morphological analysis of MEP confirmed the agglomerate porous morphology of magnetite. Oxygen and iron, the main constituents of magnetite were acknowledged during the elemental analysis using EDS. The phosphate adsorption on MEP is well explained using various isotherm and kinetic models, exhibiting the monolayer adsorption of phosphate on the surface of MEP. The maximum adsorption capacity was determined 6.41 mg/g. Based on particle size (45–75 and 75–150 µm) and empty bed contact time (1 and 2 h), four columns were operated for 54 days. MEP were appeared successful to remove all phosphate concentration from the column influent having 2 mg/L concentration. The operated column reactors were successfully regenerated with alkaline solution. The results indicated potential for practical application of the MEP for phosphate removal.

Key wordsAdsorption    Magnetite    Mill-scale    Phosphate    Wastewater treatment
收稿日期: 2019-04-19      出版日期: 2019-08-07
Corresponding Author(s): Young-Gyun Choi   
 引用本文:   
. [J]. Frontiers of Environmental Science & Engineering, 2019, 13(5): 71.
Muhammad Kashif Shahid, Yunjung Kim, Young-Gyun Choi. Adsorption of phosphate on magnetite-enriched particles (MEP) separated from the mill scale. Front. Environ. Sci. Eng., 2019, 13(5): 71.
 链接本文:  
https://academic.hep.com.cn/fese/CN/10.1007/s11783-019-1151-2
https://academic.hep.com.cn/fese/CN/Y2019/V13/I5/71
Fig.1  
Period Column Particle size (µm) EBCT (h) Flow rate (L/h)
0–34 days C1 45–75 1 0.282±0.003
C2 75–150 1 0.285±0.003
C3 45–75 2 0.136±0.006
C4 75–150 2 0.142±0.007
34–50 days C1 45–75 1 0.283±0.001
C2 75–150 1 0.287±0.003
C3 45–75 2 0.147±0.003
C4 75–150 2 0.149±0.003
Tab.1  
Fig.2  
Components Weight %
45–75 µm 75–150 µm 150–300 µm
Fe 98.05 98.50 98.32
Mn 0.80 0.77 0.78
Cr 0.37 0.13 0.14
Cl 0.28 0.22 0.04
Si 0.16 0.12 0.35
Ni 0.15 0.03 0.03
Ca 0.09 0.10 0.08
Cu 0.03 0.05 0.04
Mo 0.03 0.04 0.03
Nb 0.02 0.03 0.03
S 0.02
Ti 0.02 0.03
Al 0.13
Tab.2  
Fig.3  
Fig.4  
Range of size O Fe
45–75 μm 58.71 41.29
75–150 μm 61.77 38.23
150–300 μm 62.13 37.87
Tab.3  
Fig.5  
Model Parameters Value
Langmuir isotherm model qmax 6.414 mg/g
KL 0.021
R2 0.996
Freundlich isotherm model KF 0.329
n 1.711
R2 0.993
Pseudo-first-order kinetic model k1 3.1 × 103 min−1
R2 0.90
Pseudo-second-order kinetic model k2 4 × 104 (g·mg)/min
R2 0.94
Tab.4  
Fig.6  
Adsorbent Adsorption capacity (mg/g) Reference
MEP 6.41 This study
Magnetic iron oxide 5.03 Yoon et al. (2014)
Magnetite based nanoparticles 5.2 Daou et al. (2007)
Agro-waste rice husk ash 0.76 Mor et al. (2016)
Polypyrrole/BOF slag nanocomposite 5.18 Islam et al. (2014)
Magnetite mineral microparticles 0.83 Xiao et al. (2017)
Tab.5  
Fig.7  
Fig.8  
Fig.9  
Fig.10  
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