Removal of dioxins and related aromatic hydrocarbons from flue gas streams by adsorption and catalytic destruction

被引:98
作者
Liljelind, P [1 ]
Unsworth, J
Maaskant, O
Marklund, S
机构
[1] Umea Univ, Dept Chem, SE-90287 Umea, Sweden
[2] Shell Res & Technol Ctr, Shell Global Solut, Fuels Business Grp, Chester CH1 3SH, Cheshire, England
[3] CRI Technol Serv BV, NL-2514 AB The Hague, Netherlands
关键词
catalyst; chlorobenzenes; chlorophenols; combustion; conversion; end-of-pipe; incineration; low temperature; PCB; PCDD; PCDF; PAH;
D O I
10.1016/S0045-6535(00)00235-6
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The dioxin removing capacity of the shell dedioxin system (SDDS - a Ti/V oxidative type catalyst) has: been tested using the Umea lab-scale incinerator over the temperature range 100-230 degreesC and at space velocities of 8000 and 40,000 h(-1). Other analogous organic compounds, such as PCBs, PAHs, chlorobenzenes and chlorophenols have also been investigated. Results show a high degree of dioxin removal already at 100 degreesC (82%), which occurs mainly by adsorption. When the temperature is raised a transition towards destruction is seen and at 150 degreesC, gas hour space velocity (GHSV) 8000 and at 230 degreesC, GHSV 40,000 virtually all removal is by destruction. High PCDD/F destruction efficiencies are reported (> 99.9%, based on T-TEQ); the other dioxin-related species and PAHs are also removed and destroyed to a significant extent. The SDDS has proved to be an effective means of destroying organic compounds in the gas phase, particularly dioxins, at temperatures as low as 150 degreesC. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:615 / 623
页数:9
相关论文
共 15 条
[1]  
Andersson P., 1998, ORGANOHALOG COMPD, V36, P109
[2]   PCDD-DESTRUCTION AND PCDF-DESTRUCTION BY A SCR-UNIT IN A MUNICIPAL WASTE INCINERATOR [J].
BOOS, R ;
BUDIN, R ;
HARTL, H ;
STOCK, M ;
WURST, F .
CHEMOSPHERE, 1992, 25 (03) :375-382
[3]   Comparative evaluation of techniques for controlling the formation and emission of chlorinated dioxins/furans in municipal waste incineration [J].
Buekens, A ;
Huang, H .
JOURNAL OF HAZARDOUS MATERIALS, 1998, 62 (01) :1-33
[4]   STUDIES ON SAMPLING METHODS FOR PCDDS AND PCDFS IN STACK EMISSION [J].
FANGMARK, I ;
WIKSTROM, LE ;
MARKLUND, S ;
RAPPE, C .
CHEMOSPHERE, 1990, 20 (10-12) :1333-1340
[5]   INFLUENCE OF POSTCOMBUSTION TEMPERATURE PROFILES ON THE FORMATION OF PCDDS, PCDFS, PCBZS, AND PCBS IN A PILOT INCINERATOR [J].
FANGMARK, I ;
STROMBERG, B ;
BERGE, N ;
RAPPE, C .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1994, 28 (04) :624-629
[6]   CATALYTIC DESTRUCTION OF PCDDS IN FLUE-GAS [J].
HIRAOKA, M ;
TAKEDA, N ;
OKAJIMA, S ;
KASAKURA, T ;
IMOTO, Y .
CHEMOSPHERE, 1989, 19 (1-6) :361-366
[7]  
MARKLUND S, 1992, WASTE MANAGE RES, V10, P21, DOI 10.1177/0734242X9201000104
[8]  
MARKLUND S, 1990, THESIS UMEA U SWEDEN
[9]  
Morsbach B, 1996, VTT SYMP, V163, P77
[10]  
Siret B., 1996, P INT C INC THERM TR, P583