Leaching Behavior of Lead and Silver from Lead Sulfate Hazardous Residues in NaCl-CaCl2-NaClO3 Media

被引:6
作者
Zhang, Yuhui [1 ]
Jin, Bingjie [1 ,2 ]
Song, Qinghe [1 ]
Chen, Buming [1 ,2 ]
Wang, Chengyan [3 ]
机构
[1] Kunming Univ Sci & Technol, Fac Met & Energy Engn, Kunming 650093, Yunnan, Peoples R China
[2] Kunming Univ Sci & Technol, State Key Lab Complex Nonferrous Met Resources Cl, Kunming 650093, Yunnan, Peoples R China
[3] Univ Sci & Technol Beijing, Sch Met & Ecol Engn, Beijing 100083, Peoples R China
基金
中国国家自然科学基金;
关键词
SODIUM-CARBONATE; ZINC; RECOVERY; CONCENTRATE; EXTRACTION; TAILINGS;
D O I
10.1007/s11837-019-03472-1
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
The leaching behavior of lead and silver from lead sulfate residues in NaCl-CaCl2-NaClO3 media was studied systematically. The results indicate that Cl- concentration, NaClO3 concentration, leaching time and temperature had significant effects on lead and silver leaching, whilst agitation speed and the liquid-solid ratio had a secondary effect on silver leaching but little effect on lead leaching. The Ca2+ concentration had an important effect on SO42- removal but little effect on lead and silver leaching. The optimum parameters for lead and silver leaching were: initial Cl- concentration: 207.5g/L; NaClO3 concentration: 12g/L; Ca2+ concentration: 1.3 times of stoichiometric quantity; temperature: 90 +/- 2 degrees C; time: 1h; liquid-solid ratio: 8:1-10:1; and agitation speed: 450rpm. The lead and silver leaching were>98% and 95%, respectively. The removal ratio of SO42- was>98%. The leaching kinetics of lead follow the shrinking core model of mixed control, and the apparent activation energy was 13.4kJ/mol.
引用
收藏
页码:2388 / 2395
页数:8
相关论文
共 20 条
  • [1] Atanasova D, 2008, J U CHEM TECHNOL MET, V2, P262
  • [2] Chen GF, 2000, LEAD METALLURGY, P90
  • [3] Dutrizac J.E., 1998, ACTA METALL SLOVACA, V1, P5
  • [4] Brine leaching of lead-bearing zinc plant residues: Process optimization using orthogonal array design methodology
    Farahmand, Fariba
    Moradkhani, Davood
    Safarzadeh, Mohammad Sadegh
    Rashchi, Fereshteh
    [J]. HYDROMETALLURGY, 2009, 95 (3-4) : 316 - 324
  • [5] Lead recovery from a typical Brazilian sludge of exhausted lead-acid batteries using an electrohydrometallurgical process
    Ferracin, LC
    Chácon-Sanhueza, AE
    Davoglio, RA
    Rocha, LO
    Caffeu, DJ
    Fontanetti, AR
    Rocha, RC
    Biaggio, SR
    Bocchi, N
    [J]. HYDROMETALLURGY, 2002, 65 (2-3) : 137 - 144
  • [6] THE CONVERSION OF LEAD SULFATE TO LEAD CARBONATE IN SODIUM-CARBONATE MEDIA
    GONG, Y
    DUTRIZAC, JE
    CHEN, TT
    [J]. HYDROMETALLURGY, 1992, 28 (03) : 399 - 421
  • [7] Optimization of brine leaching of metals from hydrometallurgical residue
    Guo Zhao-hui
    Pan Feng-kai
    Xiao Xi-yuan
    Zhang Long
    Jiang Kai-qi
    [J]. TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 2010, 20 (10) : 2000 - 2005
  • [8] Top submerged lance direct zinc smelting
    Hoang, J.
    Reuter, M. A.
    Matusewicz, R.
    Hughes, S.
    Piret, N.
    [J]. MINERALS ENGINEERING, 2009, 22 (9-10) : 742 - 751
  • [9] Zinc and lead extraction from complex raw sulfides by sequential bioleaching and acidic brine leach
    Liao, MX
    Deng, TL
    [J]. MINERALS ENGINEERING, 2004, 17 (01) : 17 - 22
  • [10] Desulphurization of damped battery paste by sodium carbonate and sodium hydroxide
    Lyakov, Nedialko K.
    Atanasova, Dimitrina A.
    Vassilev, Venceslav S.
    Haralampiev, Georgi A.
    [J]. JOURNAL OF POWER SOURCES, 2007, 171 (02) : 960 - 965