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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.    2020, Vol. 14 Issue (5) : 902-912    https://doi.org/10.1007/s11705-019-1887-z
RESEARCH ARTICLE
Coextraction of vanadium and manganese from high-manganese containing vanadium wastewater by a solvent extraction-precipitation process
Zishuai Liu1,3,4,5, Yimin Zhang1,3,4,5(), Zilin Dai2, Jing Huang1,3,4,5, Cong Liu1,3,4,5
1. School of Resource and Environmental Engineering, Wuhan University of Science and Technology, Wuhan 430081, China
2. Guangdong Research Institute of Rare-Metal, Guangzhou 510650, China
3. State Environmental Protection Key Laboratory of Mineral Metallurgical Resources Utilization and Pollution Control, Wuhan University of Science and Technology, Wuhan 430081, China
4. Hubei Collaborative Innovation Center for High Efficient Utilization of Vanadium Resources, Wuhan University of Science and Technology, Wuhan 430081, China
5. Hubei Provincial Engineering Technology Research Center of High Efficient Cleaning Utilization for Shale Vanadium Resources, Wuhan University of Science and Technology, Wuhan 430081, China
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Abstract

High-manganese containing vanadium wastewater (HMVW) is commonly produced during the vanadium extraction process from vanadium titano-magnetite. HMVW cannot be reused and discharged directly, and is harmful to the environment and affect product quality due to heavy metals in the wastewater. The wastewater is usually treated by lime neutralization, but valuable metals (especially V and Mn) cannot be recovered. In this study, an efficient and environmentally friendly method was developed to recover valuable metals by using a solvent extraction-precipitation process. In the solvent extraction process, 98.15% of vanadium was recovered, and the V2O5 product, with a purity of 98.60%, was obtained under optimal conditions. For the precipitation process, 91.05% of manganese was recovered as MnCO3 which meets the III grade standard of HG/T 2836-2011. Thermodynamic simulation analysis indicated that MnCO3 was selectively precipitated at pH 6.5 while Mg and Ca could hardly be precipitated. The results of X-ray diffraction and scanning electron microscopy demonstrated that the obtained V2O5 and MnCO3 displayed a good degree of crystallinity. The treated wastewater can be returned for leaching, and resources (V and Mn) in the wastewater were utilized efficiently in an environmentally friendly way. Therefore, this study provides a novel method for the coextraction of V and Mn from HMVW.

Keywords high-manganese containing vanadium wastewater      solvent extraction      carbonate precipitation      vanadium titano-magnetite      valuable metal recovery     
Corresponding Author(s): Yimin Zhang   
Just Accepted Date: 04 September 2019   Online First Date: 15 January 2020    Issue Date: 25 May 2020
 Cite this article:   
Zishuai Liu,Yimin Zhang,Zilin Dai, et al. Coextraction of vanadium and manganese from high-manganese containing vanadium wastewater by a solvent extraction-precipitation process[J]. Front. Chem. Sci. Eng., 2020, 14(5): 902-912.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-019-1887-z
https://academic.hep.com.cn/fcse/EN/Y2020/V14/I5/902
Fig.1  Principle flowsheet of vanadium extraction from vanadium titano-magnetite.
Element V VO2+ VO2+ Mn Mg Ca Fe Al P Si
Concentration /(mg?L?1) 1150 1111 39 15240 6150 455 34 47 16 120
Tab.1  Chemical composition of HMVW
Fig.2  Effect of equilibrium pH on the extraction of V and Mn.
Fig.3  Potential-pH diagram for V-Mn-H2O systems at 25°C.
Fig.4  Extraction isotherm of vanadium.
Items Concentration/(mg?L?1) Extraction efficiency /% Distribution ratios Separation coefficient
V Mn V Mn V Mn
Loaded organic phase 3420 2100 99.13 4.60 327.00 0.14 2335.71
Raffinate 10 14540 0.87 95.40
HMVW 1150 15240 100.00 100.00
Tab.2  Results of a three stages countercurrent simulation experiment
Element V Mn Mg Ca Fe Al P Si
Concentration/(mg?L?1) 10 14540 6010 432 23 44 24 116
Tab.3  Chemical composition of raffinate
Fig.5  Effect of H2SO4 concentration on the stripping of V and Mn.
Fig.6  Stripping isotherm of vanadium.
Items Concentration/(mg?L?1) Stripping efficiency/%
V Mn V Mn
Stripped vanadium solution 16953 549 99.14 5.23
Barren organic phase 147 9951 0.86 94.77
Loaded organic phase 3420 2100 100.00 100.00
Tab.4  Results of four-stage countercurrent stripping
Time of recycle 0 1 2 3 4 5 6
Extraction efficiency 99.14 99.27 99.18 99.36 99.20 99.17 99.08
Tab.5  Results of regeneration of barren organic phase
Fig.7  Effect of equilibrium pH on MnCO3 precipitation.
Fig.8  Speciation distribution of Mn, Mg, and Ca in aqueous carbonic acid solution at 25°C. (a) [Mn] = 0.28 mol/L, [Mg] = 0.26 mol/L, [Ca] = 0.014 mol/L, [CO32?] = 0.28 mol/L; (b) [Mn] = 0.28 mol/L, [Mg] = 0.26 mol/L, [Ca] = 0.014 mol/L, [CO32?] = 0.32 mol/L.
Fig.9  Effect of reaction time on MnCO3 precipitation.
Element V Mn Mg Ca Fe Al Si
Concentration /(mg?L?1) 5 1301 5830 419 15 18 87
Tab.6  Chemical composition of treated wastewater
Fig.10  SEM-EDS and XRD images of the V2O5 product.
Elements V2O5 Si Fe P S As K2O+ Na2O
Product 98.60 0.015 0.008 0.006 0.002 ? 0.75
YB/T 5304-2017 ≥98.0 ≤0.2 ≤0.25 ≤0.03 ≤0.1 ≤0.02 ≤1.0
Tab.7  Purity of the V2O5 product a)
Fig.11  SEM and XRD images of the MnCO3 product.
Elements Mn Cl? SO42? SiO2 Al K Na Ca Mg Pb
Product 44.80 0.001 0.30 0.03 0.26 0.002 0.005 0.10 0.25 0.0001
HG/T 2836-2011 ≥43 ≤0.03 ≤0.50 ≤0.05 ≤0.05 ≤0.02 ≤0.03 ≤1.0 ≤0.50 ≤0.01
Tab.8  Purity of the MnCO3 product a)
Fig.12  A process flowsheet for coextracting V and Mn from HMVW.
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