SOLID-LIQUID MASS-TRANSFER IN THE PRESENCE OF MICROPARTICLES DURING DISSOLUTION OF IRON IN A MECHANICALLY AGITATED CONTRACTOR

被引:8
作者
GEETHA, KS [1 ]
SURENDER, GD [1 ]
机构
[1] REG RES LAB,TRIVANDRUM 695019,INDIA
关键词
D O I
10.1016/0304-386X(94)90008-6
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
Mass transfer between solid particles and liquids frequently occurs in the presence of inert micro-particles during iron removal by precipitation. In this investigation, the influence of inert micro-particles on mass transfer between a coarse active particle and liquid is simulated with the aid of a cementation reaction between cast iron particles and copper sulphate solution in a mechanically agitated contactor. Kaolin, silicon carbide, iron oxide and anatase were used as the inert micro-particles. The reaction was carried out under conditions of mass transfer control. The experimental data agreed well with Sano's semiempirical expression for a solid-liquid mass transfer coefficient based on the specific power group. The presence of inert micro-particles was found to reduce the solid-liquid mass transfer coefficient significantly, depending on volume fraction, size and density. The relative mass transfer factor, alpha, defined as the ratio of the solid-liquid mass transfer coefficient with and without the presence of inert micro-particles (k'(sl)/k(sl), was correlated by the expression (SD = 8.66%). alpha = 1 + betaln phi*/phi(mp) where phi(mp) = the volume fraction of inert micro-particles, phi* the threshold volume fraction below which the inert micro-particles do not influence the mass transfer coefficient; and beta = a mass transfer attenuation factor, beta and phi* are functions of density and size of inert micro-particles and can be expressed as: beta = 4.33 x 10(-5) d(mp)-0.32 rho1.05; phi* = 0.17 d(mp)0.12 rho(mp)-0.52. The ranges of variables covered by the correlation are: 1.0 < d(mp) < 13 mum; 2600 < rho(mp) < 5300 kg/m3; 0 < phi(mp) < 0.06. The relative mass transfer factor, alpha, was found to be independent of the coarse active solid phase hold-up to a volume fraction of 0.04.
引用
收藏
页码:231 / 246
页数:16
相关论文
共 27 条
[1]  
AGARWAL RD, 1988, J MINES METALS F MAR, P138
[2]  
ARMANATE PM, 1989, CHEM ENG SCI, V44, P2781
[3]  
ASAI S, 1986, 3RD WORLD CONGR CHEM, V2, P428
[4]  
Au-Yeung S.C.F., 1986, IRON CONTROL HYDROME, P131
[5]  
BECHER RG, 1965, P AUST I MIN METALL, V21, P21
[6]  
BRACANIN BF, 1980, P AUST I MIN METALL, V275, P33
[7]  
CALERBANK PH, 1961, T I CHEM ENG-LOND, V39, P363
[8]   NEGATIVE FOULING RESISTANCES - THE EFFECT OF SURFACE-ROUGHNESS [J].
CRITTENDEN, BD ;
ALDERMAN, NJ .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (04) :829-838
[9]   THE MODELING OF PARTICULATE LEACHING REACTORS - THE POPULATION BALANCE APPROACH [J].
CRUNDWELL, FK ;
BRYSON, AW .
HYDROMETALLURGY, 1992, 29 (1-3) :275-295
[10]   THE OXIDATION OF FERROUS SULFATE BY MOLECULAR-OXYGEN UNDER ZINC PRESSURE-LEACH CONDITIONS [J].
DREISINGER, DB ;
PETERS, E .
HYDROMETALLURGY, 1989, 22 (1-2) :101-119