Recovery of metals from copper converter slag by leaching with K2Cr2O7-H2SO4

被引:0
|
作者
Boyrazli, M [1 ]
Altundogan, HS
Tümen, F
机构
[1] Firat Univ, Dept Met & Mat Engn, TR-23279 Elazig, Turkey
[2] Firat Univ, Dept Chem Engn, TR-23279 Elazig, Turkey
关键词
D O I
暂无
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
In this study, the effects of some parameters on the extraction of metals from copper converter slag by using a sulphuric acid/potassium dichromate lixiviant were investigated. The leaching kinetic of copper from converter slag was also investigated. The results indicated that increasing the time and temperature have positive effects on the extraction of metals. The best results were obtained by the leaching of converter slag (-200 mesh, 10 g/L of slag/solution ratio) with a lixiviant containing 0.25 M H2SO4 and 0.1 M K2Cr2O7 for 120 minutes at 70 degrees C. Under these conditions, 99.66% Cu extraction yield was achieved. The kinetic evaluations showed that the extraction of Cu from the converter slag is well represented by the shrinking core model controlled by diffusion through the slag matrix. The activation energy of the leach process was calculated as 33.66 kJ/mol for the temperature range of 25 to 70 degrees C (298 to 343 K). Also, reaction order with respect to dichromate was determined as first order in the concentration range of 0.025 to 0.1 M at 25 degrees C (298 K).
引用
收藏
页码:145 / 151
页数:7
相关论文
共 50 条
  • [41] SOLUBILITY IN THE VOSO4-K2SO4-H2SO4-H2O SYSTEM
    IVAKIN, AA
    CHUFAROVA, IG
    GLAZYRIN, MP
    PETUNINA, NI
    ZHURNAL NEORGANICHESKOI KHIMII, 1986, 31 (02): : 491 - 495
  • [42] Thermodynamic study of the NaCl-Na2SO4-Na2Cr2O7-H2Osystem at the temperature 298.15 K
    Christov, C
    CALPHAD-COMPUTER COUPLING OF PHASE DIAGRAMS AND THERMOCHEMISTRY, 2001, 25 (01): : 11 - 17
  • [43] (Solid plus liquid) metastable equilibria in quaternary system (Li2SO4+K2SO4+Li2B4O7+K2B4O7+H2O) at T=288 K
    Sang, SH
    Yin, HA
    Xing, WZ
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2006, 38 (02): : 173 - 178
  • [44] Cobalt recovery from spent lithium-ion batteries by leaching in H2SO4-N2 and H2SO4-O2 systems followed by electrochemical deposition
    Medic, Dragana, V
    Tasic, Zaklina Z.
    Nujkic, Maja M.
    Dimitrijevic, Silvana B.
    Dordievski, Stefan S.
    Alagic, Sladana C.
    Milic, Snezana M.
    HEMIJSKA INDUSTRIJA, 2024, 78 (03) : 281 - 290
  • [45] Thermodynamic evaluation and optimization of the (Na2SO4+K2SO4+Na2S2O7+K2S2O7) system
    Lindberg, Daniel
    Backman, Rainer
    Chartrand, Patrice
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2006, 38 (12): : 1568 - 1583
  • [46] Leaching of enargite in H2SO4-NaCl-O2 media
    Padilla, R
    Girón, D
    Ruiz, MC
    HYDROMETALLURGY, 2005, 80 (04) : 272 - 279
  • [47] Leaching of sulfidized chalcopyrite with H2SO4-NaCl-O2
    Padilla, R
    Zambrano, P
    Ruiz, MC
    METALLURGICAL AND MATERIALS TRANSACTIONS B-PROCESS METALLURGY AND MATERIALS PROCESSING SCIENCE, 2003, 34 (02): : 153 - 159
  • [48] Leaching of sulfidized chalcopyrite with H2SO4-NaCl-O2
    R. Padilla
    P. Zambrano
    M. C. Ruiz
    Metallurgical and Materials Transactions B, 2003, 34 : 153 - 159
  • [49] Desulfurization of fuel by leaching using H2O2 and H2SO4
    Karaca, H
    Yildiz, Z
    PETROLEUM SCIENCE AND TECHNOLOGY, 2005, 23 (3-4) : 285 - 298
  • [50] SOLUBILITY IN K2SO4-(NH4)2SO4-H2O AND K2SO4-COSO4-H2O SYSTEMS AT 25 DEGREES
    SHEVCHUK, VG
    PAVLENKO, AI
    ZHURNAL PRIKLADNOI KHIMII, 1971, 44 (01) : 183 - +