Leaching behavior and kinetics of vanadium extraction from vanadium-bearing steel slag

被引:12
作者
Gao, Minglei [1 ,2 ]
Xue, Xiangxin [1 ]
Li, Lanjie [2 ]
Yang, He [1 ]
Chen, Donghui [2 ]
机构
[1] Northeastern Univ, Sch Met, Shenyang 110004, Liaoning, Peoples R China
[2] HBIS Grp ChengSteel, Inst Vanadium Titanium Technol, Chengde 067102, Hebei, Peoples R China
基金
中国国家自然科学基金;
关键词
vanadium-bearing steel slag; extraction; vanadium; kinetics; sodium hydroxide; SYSTEM;
D O I
10.1051/metal/2018129
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
The vanadium-bearing steel slag as solid waste is also one of valuable vanadium-containing resource. Recovering vanadium from the refractory steel slag is a great challenge in the world. A leaching process study using high concentration sodium hydroxide solution was proposed in this laboratory work. The effects of sodium hydroxide concentration, particle size, leaching temperature and the ratio of alkali to slag on the rate of vanadium leaching were determined and the leaching kinetics was presented. It indicates that the leaching rate is highly sensitive to the sodium hydroxide concentration and leaching temperature and increases with increasing temperature and sodium hydroxide concentration. By studying the reaction mechanisms, it was found that the dicalcium silicate, tricalcium silicate and calcium ferrited which co-exist with calcium vanadate in the vanadium-bearing steel slag were gradually exposed and reacted with NaOH media to form Na3VO4. The leaching kinetics was analyzed which indicated that the leaching rate is controlled by the chemical reaction with the apparent activation energy of 51.34 kJ/mol. On the basis of this process, the vanadium can be effectively extracted with a leaching rate of more than 80%. The leaching medium can be recycled. It is an effective and cleaner process for leaching vanadium.
引用
收藏
页数:9
相关论文
共 28 条
[1]   Leaching of vanadium from LD converter slag using sulfuric acid [J].
Aarabi-Karasgani, M. ;
Rashchi, F. ;
Mostoufi, N. ;
Vahidi, E. .
HYDROMETALLURGY, 2010, 102 (1-4) :14-21
[2]  
Burwell B., 1992, J MET, V13, P562
[3]  
Chaurand P., 2006, HAZARD MAT, V139, P37
[4]   An overview of utilization of slag and sludge from steel industries [J].
Das, B. ;
Prakash, S. ;
Reddy, P. S. R. ;
Misra, V. N. .
RESOURCES CONSERVATION AND RECYCLING, 2007, 50 (01) :40-57
[5]  
[高明磊 Gao Minglei], 2013, [过程工程学报, The Chinese Journal of Process Engineering], V13, P964
[6]  
HAYES ET, 1961, J IND ENG CHEM, V53, P105
[7]   MAGNETIC, ELECTRICAL AND THERMAL STUDIES ON V1-XMOX02 SYSTEM WITH 0 LESS THAN OR EQUAL TO X LESS THAN OR EQUAL TO 0.20 [J].
HORLIN, T ;
NIKLEWSKI, T ;
NYGREN, M .
MATERIALS RESEARCH BULLETIN, 1973, 8 (02) :179-189
[8]  
Huang D., 2000, RE VANADIUM STEEL MA
[9]   Sulfuric acid leaching of South African chromite. Part 2: optimization of leaching conditions [J].
Jiang, Maofa ;
Zhao, Qing ;
Liu, Chengjun ;
Shi, Peiyang ;
Zhang, Bo ;
Yang, Dapeng ;
Saxen, Henrik ;
Zevenhoven, Ron .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 2014, 130 :102-107
[10]  
LAN Yao-zhong, 2005, ENG SCI, V3, P58