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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.    2023, Vol. 17 Issue (6) : 71    https://doi.org/10.1007/s11783-023-1671-7
RESEARCH ARTICLE
Facile fabrication of dolomite-doped biochar/bentonite for effective removal of phosphate from complex wastewaters
Huan Xi1, Fanlu Min2(), Zhanhu Yao3, Jianfeng Zhang1()
1. College of Mechanics and Materials, Hohai University, Nanjing 211100, China
2. Key Laboratory of Geomechanics and Embankment Engineering (Ministry of Education), Hohai University, Nanjing 210098, China
3. CCCC First Highway Engineering Group Co., Ltd., Beijing 100102, China
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Abstract

● Dolomite-doped biochar/bentonite was synthesized for phosphate removal.

● DO/BB exhibited a high phosphate adsorption capacity in complex water environments.

● PVC membrane incorporated with DO/BB can capture low concentration phosphate.

● Electrostatic interaction, complexation and precipitation are main mechanisms.

The removal of phosphate from wastewater using traditional biological or precipitation methods is a huge challenge. The use of high-performance adsorbents has been shown to address this problem. In this study, a novel composite adsorbent, composed of dolomite-doped biochar and bentonite (DO/BB), was first synthesized via co-pyrolysis. The combination of initial phosphate concentration of 100 mg/L and 1.6 g/L of DO/BB exhibited a high phosphate-adsorption capacity of 62 mg/g with a removal efficiency of 99.8%. It was also stable in complex water environments with various levels of solution pH, coexisting anions, high salinity, and humic acid. With this new composite, the phosphate concentration of the actual domestic sewage decreased from 9 mg/L to less than 1 mg/L, and the total nitrogen and chemical oxygen demand also decreased effectively. Further, the cross-flow treatment using a PVC membrane loaded with DO/BB (PVC-DO/BB), decreased the phosphate concentration from 1 to 0.08 mg/L, suggesting outstanding separation of phosphate pollutants via a combination of adsorption and separation. In addition, the removal of phosphate by the PVC-DO/BB membrane using NaOH solution as an eluent was almost 90% after 5 cycles. The kinetic, isotherm and XPS analysis before and after adsorption suggested that adsorption via a combination of electrostatic interaction, complexation and precipitation contributed to the excellent separation by the as-obtained membranes.

Keywords Biochar-bentonite composite      Dolomite doping      Phosphate adsorption      Polymeric matrix membrane      Adsorption-filtration dual functions      Low-concentration phosphate     
Corresponding Author(s): Fanlu Min,Jianfeng Zhang   
Issue Date: 22 December 2022
 Cite this article:   
Huan Xi,Fanlu Min,Zhanhu Yao, et al. Facile fabrication of dolomite-doped biochar/bentonite for effective removal of phosphate from complex wastewaters[J]. Front. Environ. Sci. Eng., 2023, 17(6): 71.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-023-1671-7
https://academic.hep.com.cn/fese/EN/Y2023/V17/I6/71
Fig.1  Schematic of the fabrication procedure for the new materials developed in this study (a) DO/BB and (b) PVC-DO/BB membrane.
Fig.2  (a) XRD patterns, (b) FTIR spectra, (c) N2 adsorption/desorption isotherms and (d) BJH pore size distributions of BB900, DO900 and DO/BB.
Characteristics BB900 DO900 DO/BB
BET specific surface area (m2/g) 213.91 10.33 68.77
Average pore radius (nm) 5.37 12.31 12.24
Total pore volume (cm3/g) 0.053 0.015 0.043
Tab.1  BET specific surface area and pore characteristics of BB900, DO900 and DO/BB
Fig.3  Optical images, cross-sectional and surface SEM images, anti-tensile performances, contact angles, film thicknesses and 2D/3D AFM test images: (a) PVC and (b) PVC-20%DO/BB.
Fig.4  Effects of (a) DO/BB dosage, (b) solution pH, (c) coexisting anions, (d) high salinity and (e) humic acid on phosphate adsorption.
No. Time pH Total phosphorus (mg/L) Phosphate (mg/L) Total nitrogen (mg/L) COD (mg/L)
1 Before treatment 7.58 9.67 9.46 107.21 105.3
After treatment 9.42 0.88 0.77 64.58 66.22
2 Before treatment 7.52 7.70 7.05 106.91 90.3
After treatment 9.64 0.67 0.62 80.00 34.61
Tab.2  Water quality parameters of domestic sewage before and after treatment
Fig.5  (a) Pure water permeabilities and BSA rejection of PVC membranes with different DO/BB doping amount; (b) effect of recycling times on the adsorption-desorption behaviors of PVC-20%DO/BB; cross-flow experiments with different initial concentrations using PVC membranes with different DO/BB doping amount: (c) 1 mg/L and (d) 5 mg/L.
Membrane EM a) Water flux (L/(m2·h)) pH IC (mg/L) b) Time (h) RE (%) c) Ref.
Zr/PVA modified flat-sheet PVDF membrane Filtration 95.5 2.0 0.216 38.6 88 Zhao and Chen (2016)
La-based porous PAN nanofiber membrane Batch adsorption / 5.0 100 20 24.42 Jia et al. (2022)
La/C nanocomposite-doped membrane Filtration 110 / 0.2 0.37 50 Xia et al. (2021)
Cu(II) polyethersulfone-type membrane Continuous adsorption / 5.1 3 4.1 90 Song et al. (2016)
Membrane with zirconium sulfate mesostructured Cycle filtration 1765 5.0 50 1.1 12.4 Furuya et al. (2017)
Biochar incorporated polymeric matrix membrane Cross-flow filtration 43.1 / 80 0.25 71 Mohammadi et al. (2021)
PVC-DO/BB Cross-flow filtration 412 5.0 1 20 92 This work
5 20 74
Tab.3  Affinity membranes loaded with adsorbents for phosphate removal
Parameters Before treatment After treatment
pH 8.42 9.19
Dissolved oxygen (DO, mg/L) 6.14 6.55
Electroconductibility (μS/cm) 357 373
Chemical oxygen demand (COD, mg/L) 22.57 33.18
Total phosphorus (TP, mg/L) 1.12 0.47
Phosphare (mg P/L) 0.96 0.33
Total nitrogen (mg N/L) 1.21 0.98
Tab.4  Water quality parameters of Hongfeng Lake before and after treatment
Fig.6  Adsorption kinetics: (a) pseudo-first-order, pseudo-second-order, Richie n_th-order and Elovich models; (b) intraparticle diffusion model. (c) Adsorption isotherms using Langmuir, Freundlich, Langmuir_Freundlich and Temkin models.
Fig.7  XPS patterns of PVC-DO/BB before and after adsorption: (a) survey scan, (b) P 2p (c) Mg 1s and (d) Ca 2p.
Fig.8  Schematic diagram of the filtration and adsorption dual functional mechanisms of PVC-20%DO/BB membrane.
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