Incineration of doped sludges in fluidized bed. Fate and partitioning of six targeted heavy metals. I. Pilot plant used and results

被引:62
作者
Corella, J
Toledo, JM
机构
[1] Department of Chemical Engineering, University 'Complutense' of Madrid
关键词
incineration; sewage sludge; industrial sludge; heavy metals; fluidized bed; combustion; environment;
D O I
10.1016/S0304-3894(00)00280-6
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Incineration of sewage sludge doped with several heavy metals was studied at small pilot plant scale in a bubbling fluidized bed of 15 cm i.d. and 5.2m height. Some ceramic and metallic filters were tested at a relatively high temperature (600-700 degreesC) to check their usefulness for partitioning of heavy metals in the hue gas. The work was focused on the fate of six selected heavy metals (Cr, Cd, Ni, Zn, Cu, Pb). In this process, there were four exit flows or discharges for these metals: bottom ash, coarse fly ash, cake filter or fine fly ash and flue exit gas. The distribution or partitioning of each heavy metal (HM) among these four exit hows was studied. Only cadmium and sometimes lead showed any difference between the different HMs considered. All other HMs seems to have the same fate, distribution or partitioning. Such distribution is governed or ruled by the fluid dynamics in the incinerator, cyclone and ceramic filter. Most of the HMs do not have enough residence time in this incinerator type to diffuse out of the ash particle and so remain in the particle. The amount of each HM in each exit how in this process is governed by fluid dynamics and kinetics and not at all by thermodynamics. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:81 / 105
页数:25
相关论文
共 38 条
[1]  
ALBRECHT J, 1997, P 1997 INT C FLUID B, V2, P997
[2]  
BARTON RG, 1991, PROCESS SAF ENVIRON, V69, P29
[3]   Effect of incineration temperature on lead emission from a fixed bed incinerator [J].
Chang, YM ;
Chang, TC ;
Lin, JP .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1999, 32 (05) :626-634
[4]   Theoretical and experimental study of metal capture during incineration process [J].
Chen, JC ;
Wey, MY ;
Yan, MH .
JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 1997, 123 (11) :1100-1106
[5]  
CORELLA J, 1988, RESEARCH IN THERMOCHEMICAL BIOMASS CONVERSION, P384
[6]   On the selection of the catalyst among the commercial platinum-based ones for total oxidation of some chlorinated hydrocarbons [J].
Corella, J ;
Toledo, JM ;
Padilla, AM .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2000, 27 (04) :243-256
[7]   DETERMINATION OF METAL BEHAVIOR DURING THE INCINERATION OF A CONTAMINATED MONTMORILLONITE CLAY [J].
EDDINGS, EG ;
LIGHTY, JAS ;
KOZINSKI, JA .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1994, 28 (11) :1791-1800
[8]   FUNDAMENTAL-STUDIES OF METAL BEHAVIOR DURING SOLIDS INCINERATION [J].
EDDINGS, EG ;
LIGHTY, JS .
COMBUSTION SCIENCE AND TECHNOLOGY, 1992, 85 (1-6) :375-390
[9]  
HO TC, 1994, P 1994 INT INC C UC, P559
[10]  
HO TC, 1996, P 1996 INT C IT3 SAV, P415