欢迎登录材料期刊网

材料期刊网

高级检索

The acid leaching, ferric leaching, and bioleaching of chaicocite and pyrite minerals were conducted in two sets of 3L stirred reactors. The dissolution rates of copper and iron were correlated with leaching conditions. In the acid leaching process, the dissolution rate of chalcocite was around 40wt.% while that of pyrite was less than 4%. In the ferric leaching process with high ferric concentration, only 10 wt.% of iron in pyrite was leached out at the same retention time though the copper recovery over 60 wt.% in chalcocite. For the bioleaching process, the chalcocite leaching rate was highly increascd, nearly 90 wt.% of copper was leached out, and the iron dissolution of pyrite exceeded 70 wt.%. For the two minerals, the bioleaching shows the highest leaching rate compared with the acid leaching or ferric leaching. In uncontrolled bioleaching process, pyrite could be dissolved effectively. The experimental data were fitted to the shrinking core and particle model. The results show that in all the leaching tests, the chalcocite leaching was mainly controlled by diffusion, while for the pyrite leaching, chemical reaction is the main rate-determining step.

参考文献

[1] Schippers A.;Sand W. .Bacterial leaching of metal sulfides proceeds by two indirect mechanismsvia thiosulfate or via polysulfides and sulfur[J].Applied and Environmental Microbiology,1999(1):319-321.
[2] Braun R.L;Lewis A.E;Wadsworth M.E .In-place leaching of primary sulfide ores:laboratory leaching data and kinetics model[J].Metallurgical and Materials Transactions,1974,5:1717.
[3] Silva G.D .Relative importance of diffusion and reaction control during the bacterial and ferric sulphate leaching of zinc sulphide[J].Hydrometallurgy,2004,73:313.
[4] Liu Xingyu;Wu Biao;Chen Bowei;Wen Jiankang;Ruan Renman;Yao Guocheng;Wang Dianzuo .Bioleaching of chalcocite started at different pH: Response of the microbial community to environmental stress and leaching kinetics[J].Hydrometallurgy,2010(1/4):1-6.
[5] Boon M;Luyben K.C.A.M .and Heijen J.J.The use of online off-gas analyses and stoichiometry in the bio-oxidation kinetics of sulfide minerals[J].Hydrometallurgy,1998,48(01):1.
[6] Boon M;Heijnen J.J .Chemical oxidation kinetics of pyrite in bioleaching processes[J].Hydrometallurgy,1998,48(01):27.
[7] Ruan R;Wen J;Chen J .Bacterial heap-leaching:practice in Zijinshan Copper Mine[J].Hydrometallurgy,2006,83:77.
[8] May N.;Ralph D.E. .DYNAMIC REDOX POTENTIAL MEASUREMENT FOR DETERMINING THE FERRIC LEACH KINETICS OF PYRITE[J].Minerals Engineering,1997(11):1279-1290.
[9] Yunker S.B;Radovieh J.M .Enhancement of growth and ferrous iron oxidation rates of thiobacillus ferrooxidans by electrochemical reduction of ferric iron[J].Biotechnology and Bioengineering,1986,28(12):1867.
[10] Konishi Y;Nishimura H;Asai S .Bioleaching of sphalerite by the acidophilie thermophile Acidianus brierleyi[J].Hydrometallurgy,1998,47(2-3):339.
[11] Herrera M.N;Wiertz J.V;Ruiz P;Neuberg H.J and Badiila-ohlbaum R .A phenomenological model of the bioleaching of complex sulfide ores[J].Hydrometallurgy,1989,22(1-2):193.
[12] Asai S;Konishi Y;Yoshida K .Kinetics model for batch bacterial dissolution of pyrite particles by Thiobacillus ferrooxidans[J].Chemical Engineering Science,1992,47(01):133.
[13] E.Olanipekun .A kinetic study of the leaching of a Nigerian ilmenite ore by hydrochloric acid[J].Hydrometallurgy,1999(1):1-10.
[14] Rohwerder T.;Sand W.;Schippers A. .Determination of reaction energy values for biological pyrite oxidation by calorimetry[J].Thermochimica Acta: An International Journal Concerned with the Broader Aspects of Thermochemistry and Its Applications to Chemical Problems,1998(1/2):79-85.
[15] Samuel A.B .Kinetics of Leaching of Chalcacite in Acid Ferric Sulfate Media:Chemical and Bacterial Leaching[D].University of British Columbia,Canada,1999.
[16] Sand W;Gehrke T;Jozsa P.G;Schippers A .(Bio)chemistry of bacterial leaching-direct vs.indirect bioleaching[J].Hydrometallurgy,2001,59:159.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%