Testing total oxidation catalysts for gas cleanup in waste incineration at pilot scale

被引:16
作者
Corella, J [1 ]
Toledo, JM [1 ]
机构
[1] Univ Complutense Madrid, Dept Chem Engn, E-28040 Madrid, Spain
关键词
D O I
10.1021/ie010297p
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Seven different total oxidation catalysts (PRO*CLEAN*500; EF 258 H/D; Siemens A; ZERONOX; and Ru, Pd, and V2O5 on a TiO2 support) have been tested for abatement of principal organic hazardous compounds (POHCs) in the flue gas from a waste incinerator of the fluidized-bed type. These catalysts were placed in a slip flow downstream from the waste incinerator. The catalytic reactors used were both metallic and glass, made for monoliths and for particulates. The temperatures used in the catalytic reactors ranged from 240 to 510 C, and the volumetric gas hourly space velocities (GHSVs) ranged from 1200 to 5700 [(m(gas,normal conditions)(3)/h)/m(catalyst)(3)]. The catalysts operated under a realistic flue gas, which was sampled before and after the catalytic reactor at different times on stream. Condensates after the catalytic reactor were also analyzed for organics and for compounds sometimes lost from the catalyst. Gas sampling and analysis were carried out using standarized methods. Conversions (destructions) of most of the POHCs were 99.99%, but small GHSV values were required. Experimental conditions for an even more refined catalyst comparison are also provided.
引用
收藏
页码:1171 / 1181
页数:11
相关论文
共 42 条
[1]   Comparative study on formations of polychlorinated dibenzo-p-dioxins, polychlorinated dibenzofurans and related compounds in a fluidized bed solid waste incinerator using long term used sand and fresh sand [J].
Akimoto, Y ;
Nito, S ;
Inouye, Y .
CHEMOSPHERE, 1997, 34 (04) :791-799
[2]  
AZNAR MP, 1992, P 6 INT SOL WAST C I, V2
[3]   Selective gas-phase oxidation of polycyclic aromatic hydrocarbons on vanadium oxide-based catalysts [J].
Bruckner, A ;
Baerns, M .
APPLIED CATALYSIS A-GENERAL, 1997, 157 (1-2) :311-334
[4]   Emission of volatile organic compounds from coal combustion [J].
Chagger, HK ;
Jones, JM ;
Pourkashanian, M ;
Williams, A ;
Owen, A ;
Fynes, G .
FUEL, 1999, 78 (13) :1527-1538
[5]   Incineration of doped sludges in fluidized bed. Fate and partitioning of six targeted heavy metals. I. Pilot plant used and results [J].
Corella, J ;
Toledo, JM .
JOURNAL OF HAZARDOUS MATERIALS, 2000, 80 (1-3) :81-105
[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]  
Corella J, 2001, PROGR THERMOCHEMICAL, V1, P887
[8]  
DESAI DL, 1995, P 13 INT C FLUID BED, V1, P65
[9]  
FURRER J, 1999, P IT3 C, P327
[10]   Biomass gasification in fluidized bed at pilot scale with steam-oxygen mixtures. Product distribution for very different operating conditions [J].
Gil, J ;
Aznar, MP ;
Caballero, MA ;
Frances, E ;
Corella, J .
ENERGY & FUELS, 1997, 11 (06) :1109-1118