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Kinetics of dissolution of silver present in precious metal scraps in HNO3 was studied in temperature range of 26~85℃. Dissolution rate of silver was much faster than that of copper at all temperatures. Effects of particle size, stirring speed, acid concentration and temperature on the rate of dissolving of silver were evaluated.Dissolution rate decreases with particle size and increases with temperature. Dissolving was accelerated with acid concentrations less than 10 mol/L. Concentrations greater than 10 mol/L resulted in slowing down of the dissolution rate. Shrinking core model with internal diffusion equation t/τ=1-3(1-x)2/3+2(1-x)could be used to explain the mechanism of the reaction. Silver extraction resulted in activation energies of 33.95 k J/mol for Ag-Au0.04-Cu0.10 and 68.87 k J/mol for Ag-Cu0.23 particles. Inter-diffusion of silver and nitrate ions through the porous region of the insoluble alloying layer was the main resistance to the dissolving process. Results were tangible for applications in recycling of the material from electronic silver-bearing scraps, dental alloys,jewelry, silverware and anodic slime precious metal recovery.

参考文献

[1] A Vaskelis;A Jagminiene;L T Tamasiunaite;R Juskenas .[J].Electrochimica Acta,2005,50:4586.
[2] T.W.H. Oates;L. Ryves;M.M.M. Bilek;D.R. McKenzie .Accurate determination of optical and electronic properties of ultra-thin silver films for biosensor applications[J].Sensors and Actuators, B. Chemical,2005(1):146-152.
[3] M S Oncel;M Ince;M Bayramoglu.[J].Ultrasonics Sonochemistry,2005(12):237.
[4] R Raghavan;P K Mohanan;S C Patnaik .[J].HYDROMETALLURGY,1998,48:225.
[5] M. Wang;Y. Zhang;T. Deng .Kinetic modeling for the bacterial leaching of chalcopyrite catalyzed by silver ions[J].Minerals Engineering,2004(7/8):943-947.
[6] T Rubcuminintara;P Tasaso .[OL].http:∥www.capecanterburyacnz,2005.
[7] F M El-Cheikh;S A Khalil;M A E1-Manguch;A O Hadi .[J].Journal of Chemical Education,1985,62(09):761.
[8] R A Stairs;W D Hill;F M El-Cheikh .[J].Journal of Chemical Education,1987,64:1069.
[9] J D Carr;W D Hill;F M El-Cheikh .[J].Journal of Chemical Education,1990,67(02):183.
[10] C Ozmetin;M Copur;A Yarta;s(y) and M M Kocakerim .[J].Chemical Engineering and Technology,2000,23(08):707.
[11] C H Schack;B H Clemmons.Extractive Processes:Silver,Economics,Metallurgy and Use[M].D Van Nostrand Company,Inc,Princeton,New Jersey,1967:57.
[12] L L Martinez;M Segarra;M Fernandez;F Espiel .[J].Metallurgical and Materials Transactions B:Process Metallurgy and Materials Processing Science,1993,24:827.
[13] T Jiang;Y Yang;B Zhang;Z Huang and G Qiu .[J].Hydrometallurgy,2004,72:129.
[14] W Kunda.[A].Chicago,Illinois,1972
[15] M Salim Oncel;M Ince;M Bayramoglu.[J].Ultrasonics Sonochemistry,2005(12):237.
[16] W Wang;Y C Hoh;W S Chuang;I S Shaw .[P].US 4293332,1981.
[17] A.M. Amer .Processing of copper anodic-slimes for extraction of valuable metals[J].Waste Management,2003(8):763-770.
[18] H Demir;C Ozmetin;M M Kocakerim;S Yartasi and M Copur .[J].Chemical Engineering Progress,2004,43:1095.
[19] C Ozmetin;M Copur;A Yartasi;M M Kocakerim .[J].Industrial and Engineering Chemistry Research,1998,37:4641.
[20] H E Hilliard.U S Geological Survey,Version 1 0,U S Department of the Interior[M].Reston,Virginia,2003
[21] M Harper;J M Siegel .[J].Air and Waste Management Association,53:434.
[22] A Gherrou;H Kerdjoudj;R Molinari;E Drioli .[J].Desalination,2001,139:317.
[23] Y C Hoh;I S Shaw;W K Wang.[A].San Francisco,USA,1979
[24] A Butts;C D Coxe.Silver-Economics:Metallurgy and Use[M].R E Krieger Publ Comp,Huntington,USA,1975
[25] C H P Lupis;J F Elliot .[J].Acta Materialia,1966,14:529-1019.
[26] O Levenspiel.Chemical Reaction Engineering[M].New York:John Wiley and Sons,Inc,1972:578.
[27] [OL].http:∥www.ualbrtaca/jplampec/che/data/indexhtm,2005.
[28] A James;M Lord.Index of Chemical and Physical Data[M].Van Nostrand Reinhold,NY,USA,1992:98.
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