The combustion of polymer pellets in a bubbling fluidised bed

被引:41
作者
Baron, J.
Bulewiez, E. M.
Kandefer, S.
Pilawska, M.
Zukowski, W.
Hayhurst, A. N.
机构
[1] Univ Cambridge, Dept Chem Engn, Cambridge CB2 3RA, England
[2] Krakow Tech Univ, Fac Chem Engn & Technol, PL-31155 Krakow, Poland
[3] Krakow Tech Univ, Fac Environm Engn, PL-31155 Krakow, Poland
关键词
combustion of polymers; pyrolysis; fluidised beds;
D O I
10.1016/j.fuel.2006.05.004
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Wastes burned in incinerators usually contain polymers, whose combustion can be associated with noxious emissions, unless the conditions are properly selected. This paper investigates how polymers burn in a fluidised bed; in fact, the combustion of a number of polymers, including several types of polyethylene, polystyrene and a polyamide, was studied in a laboratory-size, bubbling, fluidised bed, filled with quartz sand, with no external heating. Pellets of a polymer were mostly thrown into such a bed of sand, fluidised and maintained hot by a fuel-lean mixture of propane, methane or hydrogen in air, which burned soon after entering the bed. In addition, polymers were also used as the only fuel, i.e., added to a hot bed fluidised by only air. Visual observations of burning polymer pellets up to similar to 240 mg were made, as well as video records obtained and the flue gas composition monitored, when the combustor was run at 800-1000 degrees C with 1.1-2.0 times more O-2 than required for complete combustion. It is clear that a polymer burns as if its volatile content were 100%. The polymer pellet first melts at a rate controlled by heat transfer. However, the melt and the gaseous products of thermal decomposition are dispersed, albeit sometimes slowly, in a fluidised bed. Although the high U/U-mf of above 10 caused some back-mixing of the gas leaving the bed and the combustion efficiency was high (assessed from O-2 consumption and CO2 production), long streaks or plumes of fuel-rich gases (from each polymer pellet) did reach the freeboard, i.e., these plumes burned as transient diffusion flames at a rate controlled by mixing. By increasing the temperature and the residence times of gas in the bed and freeboard, the observed emissions of CO and hydrocarbons could be considerably reduced. The concentrations of NO were low, except when the polymer contained chemically-combined nitrogen, as in a polyamide. It is concluded that bubbling fluidised beds can be good for incinerating polymers, possibly together with other wastes. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2494 / 2508
页数:15
相关论文
共 44 条
[1]  
Bagri R, 2002, J I ENERGY, V75, P117
[2]   Combustion of hydrocarbon fuels in a bubbling fluidized bed [J].
Baron, J ;
Bulewicz, EM ;
Zukowski, W ;
Kandefer, S ;
Pilawska, M .
COMBUSTION AND FLAME, 2002, 128 (04) :410-421
[3]   O+NNH - A POSSIBLE NEW ROUTE FOR NOX FORMATION IN FLAMES [J].
BOZZELLI, JW ;
DEAN, AM .
INTERNATIONAL JOURNAL OF CHEMICAL KINETICS, 1995, 27 (11) :1097-1109
[4]   Self-segregation of high-volatile fuel particles during devolatilization in a fluidized bed reactor [J].
Bruni, G ;
Solimene, R ;
Marzocchella, A ;
Salatino, P ;
Yates, JG ;
Lettieri, P ;
Fiorentino, M .
POWDER TECHNOLOGY, 2002, 128 (01) :11-21
[5]  
BULEWICZ EM, 2003, 4 INT C GERM TECHN A, P339
[6]  
BULEWICZ EM, 1997, 14 INT C FLUID BED C, P1103
[7]  
BULEWICZ EM, 1989, 10 INT C FBC NEW YOR, P85
[8]   BURNING OF POLYMERS [J].
BURGE, SJ ;
TIPPER, CFH .
COMBUSTION AND FLAME, 1969, 13 (05) :495-&
[9]   The combustion of solid wastes as studied in a fluidized bed [J].
Cooke, RB ;
Goodson, MJ ;
Hayhurst, AN .
PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2003, 81 (B3) :156-165
[10]  
Cullis C. F., 1981, COMBUSTION ORGANIC P