Continuous running test of the solvent extraction separation of Mo and W by H2O2-complexation with TRPO/TBP

被引:20
作者
Guan, Wenjuan [1 ,2 ,3 ]
Zhang, Guiqing [2 ,3 ]
Xiao, Liansheng [2 ,3 ]
Wang, Dezhi [1 ]
机构
[1] Cent S Univ, Sch Mat Sci & Engn, Changsha 410083, Hunan, Peoples R China
[2] Cent S Univ, Sch Met & Environm, Changsha 410083, Hunan, Peoples R China
[3] Key Lab Hunan Prov Met & Mat Proc Rare Met, Changsha 410083, Hunan, Peoples R China
关键词
Tungsten; Molybdenum; Solvent extraction separation; TRPO; TBP; H2O2; MACRO AMOUNTS; ION-EXCHANGE; MOLYBDENUM; TUNGSTEN; PRECIPITATION; RESIN;
D O I
10.1016/j.hydromet.2015.07.002
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
An unusual multi-stage extraction and stripping continuous running test was carried out in a mixer-settler. The test of the solvent extraction separation of molybdenum (Mo) and tungsten (W) from ammonium tungstate solution containing high content of Mo was carried out by using a mixture of tri-alkyl phosphine oxide (TRPO) and tributyl phosphate (TBP) as extractant, hydrogen peroxide (H2O2) as complex agent and ammonium bicarbonate (NH4HCO3) solution as stripping agent. According to the effect of pH distribution and storage time on extraction and the poor phase separation of the stripping system, the improvements such as acid addition into middle one stage of extraction, 2-section countercurrent extraction and 2-section concurrent stripping were proposed in order to improve the Mo/W separation effect and phase separation property. The ammonium paratungstate (APT) product was prepared by evaporating crystallization from the 2nd-section raffinate. The continuous running test had successfully and continuously run for more than 98 h. The results indicated that the system was very stable and the separation property good. The Mo/WO3 (mass ratio) in the 2nd-section raffinate was less than 1 x 10(-4) under optimal conditions using the aqueous solution containing 110-150 g/L WO3 and Mo/WO3 (mass ratio) 10%-15%. The APT product could meet the requirement of 0 grade of APT of the national standards GB/T 10116-2007 of China. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 8
页数:8
相关论文
共 32 条
[1]   SOLVENT-EXTRACTION OF MOLYBDENUM AND TUNGSTEN BY ALAMINE-336 AND DEHPA [J].
COCA, J ;
DIEZ, FV ;
MORIS, MA .
HYDROMETALLURGY, 1990, 25 (02) :125-135
[2]   SEPARATION OF TUNGSTEN AND MOLYBDENUM IN DILUTE HYDROCHLORIC-ACID SOLUTION BY EXTRACTION WITH SULFOXIDES [J].
DAI, GS ;
XUAN, BY ;
SU, YF .
HYDROMETALLURGY, 1984, 13 (02) :137-153
[3]   Precursor solution prepared by evaporation deamination complex method for solvent separation of Mo and W by H2O2-complexation [J].
Guan, Wen-juan ;
Zhang, Gui-qing ;
Gao, Cong-jie .
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 2013, 23 (04) :1139-1146
[4]  
Guan Wen-juan, 2011, Chinese Journal of Nonferrous Metals, V21, P1756
[5]  
Guan Wenjuan, 2013, Journal of Central South University (Science and Technology), V44, P1766
[6]   Solvent extraction separation of molybdenum and tungsten from ammonium solution by H2O2-complexation [J].
Guan, Wenjuan ;
Zhang, Guiqing ;
Gao, Congjie .
HYDROMETALLURGY, 2012, 127 :84-90
[7]   Tungsten removal from molybdate solutions using ion exchange [J].
Huo, Guangsheng ;
Peng, Chao ;
Song, Qiong ;
Lu, Xiaoying .
HYDROMETALLURGY, 2014, 147 :217-222
[8]  
Jiang A.R., 1988, RARE METALS, V12, P245
[9]  
Klimenko G.L., 2001, RUSS METALL+, V3, P49
[10]  
KONG Zhao-qing, 2009, CHINESE TUNGSTEN IND, V24, P1