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Recovery of vanadium from acid leaching solutions of spent oil hydrotreating catalyst using solvent extraction with D2EHPA (P204)
Wang, Hongjun1; Feng, Yali1; Li, Hailong1; Li, Haoran2; Wu, Hao1
2020-08-01
Source PublicationHYDROMETALLURGY
ISSN0304-386X
Volume195Pages:7
AbstractIn this paper, a process of selective extraction and separation of vanadium (IV) from acid leaching solution of spent oil hydrotreating catalyst by a solvent extraction method with P204 as an extractant was proposed. Because the leaching solution contained a large amount of elements such as nickel, aluminium and iron, the effects of various conditions on the separation of vanadium from nickel, aluminium and iron were investigated and the optimum conditions were determined. At the same time, the thermodynamic discussion on the extraction process of vanadium in the system was carried out. Using kerosene as a diluent and 20% (v/v) P204 as an extractant, the single-stage maximum extraction ratio of 93.47% for vanadium was obtained under the optimum extraction conditions of O/A ratio of 2, oscillation time of 8 min, extraction temperature of 298 k(25 degrees C) and pH value of initial aqueous phase of 2. After three stages of countercurrent extraction experiments, the concentration of vanadium, iron, nickel and aluminium in the loaded organic phase were 0.377, 0.001, 0.005 and 0.02 g/L, respectively, and their extraction ratios were determined to be 99.21%, 1.02%, 2.857% and 1.942%, respectively, realizing the selective extraction and separation of vanadium. With 2 mol/L of sulfuric acid as a stripping reagent, the complete removal of vanadium from the loaded organic phase could be achieved at O/A ratio of 2 by three stages of countercurrent experiments of vanadium removal. The thermodynamic calculation showed that the enthalpy change of the vanadium extraction in the system was -20.37 kJ.mol(-1). This demonstrated that the extraction of vanadium from acid leaching solution of spent oil hydrotreating catalyst with P204 as the extractant was an exothermic reaction.
KeywordSolvent extraction Di (2-ethylhexyl) phosphoric acid (P204) Vanadium Spent oil hydrotreating catalyst Thermodynamics
DOI10.1016/j.hydromet.2020.105404
Language英语
WOS KeywordSEPARATION ; MOLYBDENUM ; MEDIA ; THERMODYNAMICS ; TITANIUM ; MIXTURE ; METALS ; NICKEL ; WASTE ; SLAG
Funding ProjectChina Ocean Mineral Resource RD Association[DY135-B2-15] ; Major science and technology program for water pollution control and treatment[2015ZX07205-003] ; National Natural Science Foundation of China[21176242] ; National Natural Science Foundation of China[21176026]
WOS Research AreaMetallurgy & Metallurgical Engineering
WOS SubjectMetallurgy & Metallurgical Engineering
Funding OrganizationChina Ocean Mineral Resource RD Association ; Major science and technology program for water pollution control and treatment ; National Natural Science Foundation of China
WOS IDWOS:000549135400038
PublisherELSEVIER
Citation statistics
Document Type期刊论文
Identifierhttp://ir.ipe.ac.cn/handle/122111/41427
Collection中国科学院过程工程研究所
Corresponding AuthorWang, Hongjun; Feng, Yali
Affiliation1.Univ Sci & Technol Beijing, Civil & Resource Engn Sch, Beijing 100083, Peoples R China
2.Chinese Acad Sci, Inst Proc Engn, State Key Lab Biochem Engn, Beijing 100190, Peoples R China
Recommended Citation
GB/T 7714
Wang, Hongjun,Feng, Yali,Li, Hailong,et al. Recovery of vanadium from acid leaching solutions of spent oil hydrotreating catalyst using solvent extraction with D2EHPA (P204)[J]. HYDROMETALLURGY,2020,195:7.
APA Wang, Hongjun,Feng, Yali,Li, Hailong,Li, Haoran,&Wu, Hao.(2020).Recovery of vanadium from acid leaching solutions of spent oil hydrotreating catalyst using solvent extraction with D2EHPA (P204).HYDROMETALLURGY,195,7.
MLA Wang, Hongjun,et al."Recovery of vanadium from acid leaching solutions of spent oil hydrotreating catalyst using solvent extraction with D2EHPA (P204)".HYDROMETALLURGY 195(2020):7.
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