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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2019, Vol. 13 Issue (4) : 61    https://doi.org/10.1007/s11783-019-1142-3
RESEARCH ARTICLE
Nanoscale zero-valent iron supported on biochar for the highly efficient removal of nitrobenzene
Gaoling Wei2, Jinhua Zhang1(), Jinqiu Luo1, Huajian Xue1, Deyin Huang2, Zhiyang Cheng1, Xinbai Jiang1
1. Jiangsu Key Laboratory of Chemical Pollution Control and Resources Reuse, School of Environmental and Biological Engineering, Nanjing University of Science and Technology, Nanjing 210094, China
2. Guangdong Key Laboratory of Integrated Agro-environmental Pollution Control and Management, Guangdong Institute of Eco-Environmental Science and Technology, Guangzhou 510650, China
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Abstract

• Biochar supported nanoscale zero-valent iron composite (nZVI/BC) was synthesized.

• nZVI/BC quickly and efficiently removed nitrobenzene (NB) in solution.

• NB removal by nZVI/BC involves simultaneous adsorption and reduction mechanism.

• nZVI/BC exhibited better catalytic activity, stability and durability than nZVI.

The application of nanoscale zero-valent iron (nZVI) in the remediation of contaminated groundwater or wastewater is limited due to its lack of stability, easy aggregation and iron leaching. To address this issue, nZVI was distributed on oak sawdust-derived biochar (BC) to obtain the nZVI/BC composite for the highly efficient reduction of nitrobenzene (NB). nZVI, BC and nZVI/BC were characterized by scanning electron microscopy (SEM), X-ray diffraction (XRD) and X-ray photoelectron spectroscopy (XPS). For nZVI/BC, nZVI particles were uniformly dispersed on BC. nZVI/BC exhibited higher removal efficiency for NB than the simple summation of bare nZVI and BC. The removal mechanism was investigated through the analyses of UV-Visible spectra, mass balance and XPS. NB was quickly adsorbed on the surface of nZVI/BC, and then gradually reduced to aniline (AN), accompanied by the oxidation of nZVI to magnetite. The effects of several reaction parameters, e.g., NB concentration, reaction pH and nZVI/BC aging time, on the removal of NB were also studied. In addition to high reactivity, the loading of nZVI on biochar significantly alleviated Fe leaching and enhanced the durability of nZVI.

Keywords Biochar      Nanoscale zero-valent iron      Nitrobenzene      Reduction      Adsorption      Synergistic effec     
Corresponding Author(s): Jinhua Zhang   
Issue Date: 01 July 2019
 Cite this article:   
Gaoling Wei,Jinhua Zhang,Jinqiu Luo, et al. Nanoscale zero-valent iron supported on biochar for the highly efficient removal of nitrobenzene[J]. Front. Environ. Sci. Eng., 2019, 13(4): 61.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-019-1142-3
https://academic.hep.com.cn/fese/EN/Y2019/V13/I4/61
Fig.1  SEM patterns of (a) BC (×5000), (b) BC (×50000), (c) nZVI (×80000), and (d) nZVI/BC (×150000).
Fig.2  XRD patterns of (a) BC, (b) nZVI, (c) fresh and (d) used nZVI/BC.
Sample SSA (m2/g) Total pore volume (cm3/g) Micro pore volume (cm3/g) Pore size/nm
BC 481.6 0.2152 0.1604 3.16
nZVI 6.4 0.0063 0.0024 21.69
nZVI/BC 264.9 0.1611 0.1084 10.69
Tab.1  Textural characteristics of samples
Fig.3  Removal efficiencies of NB and aniline generation (inset) from NB reduction at room temperature. Reaction condition: NB concentration: 100 mg/L, nZVI dosage: 0.15 g/L, BC dosage: 0.15 g/L, nZVI/BC dosage: 0.30 g/L, initial pH: 8.0.
Fig.4  The fitting of NB removal processes using the pseudo-second-order kinetic model.
Sample qexp(mg/g) Pseudo-first-order Pseudo-second-order
k1 (min-1) R2 qe (mg/g) k2 (g/(mg·min)) h (mg/(g·min)) R2
BC 190 4.7 × 10-3 0.495 191 1.7 × 10-3 63 0.999
nZVI 248 4.5 × 10-3 0.889 255 2.6 × 10-4 17 0.998
nZVI/BC 314 4.6 × 10-3 0.723 314 1.1 × 10-3 113 0.999
Tab.2  Kinetics parameters for NB removal by various materials
Fig.5  (a) Effect of initial NB concentration on reduction efficiency by nZVI (inset figure) and nZVI/BC at room temperature. (b) The variation of removal rate (r0) as a function of initial NB concentration (C0). Reaction condition: nZVI dosage: 0.15 g/L, nZVI/BC dosage: 0.30 g/L, initial pH: 8.0.
Sample K (mg/(L·min)) b (L/mg) R2
nZVI 8.813 3.088 × 10?3 0.923
nZVI/BC 49.145 3.935 × 10?3 0.998
Tab.3  Fitting results of the NB removal by nZVI and nZVI/BC using the Langmuir-Hinshelwood Equation
Fig.6  Effect of initial pH on the removal of NB by nZVI/BC and the generation of aniline (inset) at room temperature. Reaction condition: NB concentration: 100 mg/L, nZVI/BC dosage: 0.30 g/L.
Fig.7  Fe leaching from nZVI and nZVI/BC after 6 h of NB reduction under different pH at room temperature. Reaction condition: NB concentration: 100 mg/L, nZVI dosage: 0.15 g/L, nZVI/BC dosage: 0.30 g/L, initial pH: 8.0.
Fig.8  Effect of nZVI and nZVI/BC aging on the removal efficiency of NB and aniline generation (inset figure) at room temperature. Reaction condition: NB concentration: 100 mg/L, nZVI dosage: 0.15 g/L, nZVI/BC dosage: 0.30 g/L, initial pH: 8.0, reaction time: 6 h.
Fig.9  The mass balance of NB and aniline during the adsorption and reduction by nZVI/BC as a function of time at room temperature. Reaction condition: NB concentration: 100 mg/L, nZVI/BC dosage: 0.30 g/L, initial pH: 8.0.
Fig.10  Schematic diagram for the removal mechanism of NB by nZVI/BC (a), and well dispersed nZVI/BC (b) and nZVI/BC separated by a magnet (c).
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