Scale-up study on combustibility and emission formation with two biomass fuels (B quality wood and pepper plant residue) under BFB conditions

被引:41
作者
Khan, Atif Ahmed [1 ]
Aho, Martti [2 ]
de Jong, Wiebren [1 ]
Vainikka, Pasi [2 ]
Jansens, Peter Johannes [1 ]
Spliethoff, Hartmut [3 ]
机构
[1] Delft Univ Technol, Fac 3ME, Sect Energy Technol, Dept Proc & Energy, NL-2628 CA Delft, Netherlands
[2] VTT Proc, Jyvaskyla 40101, Finland
[3] Tech Univ Munich, Lehrstuhl Therm Kraftanlagen, D-85748 Garching, Germany
关键词
Fluidized bed; Biomass; Toxic emissions; Particulates; Heavy metals; Capsicum annuum;
D O I
10.1016/j.biombioe.2008.03.011
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Combustion of two biomass fuels: demolition wood (DW) and pepper plant residue (PPR), was investigated from an emission viewpoint in a 20kW(th) fluidized bubbling bed reactor and a 1MW(th) fluidized bubbling bed test boiler. Fluidization velocity and boiler output were varied in the larger facility whereas they were kept constant in the smaller reactor. Traditional flue gases were analyzed. In addition, impactor measurements were carried out to determine the mass flow of the finest fly ash and toxic elements. These measurements were compared with EU emission directives for biomass co-incineration. It was possible to combust DW without operational problems. However, the DW was contaminated with lead, which tended to get strongly enriched in the fine fly ash. Pb tends to be adsorbed on the measurement line surfaces stronger than many other toxic elements and therefore proved difficult to collect and measure. Enrichment of Pb in the fine fly ash can be weakened by cofiring DW with PPR. Increasing the share of PPR up to 50% markedly reduces the toxic metal concentration in the finest fly ash. This, however, leads to increased mass flow of fine fly ash and increases the potential risks of operational problems such as bed agglomeration and fouling. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1311 / 1321
页数:11
相关论文
共 21 条
[1]   DEFINITION OF BIOMASS SAMPLES INVOLVING WOOD, BARK AND FOLIAGE [J].
BARTON, GM .
BIOMASS, 1984, 4 (04) :311-314
[2]   SOME ASPECTS OF FLUIDIZED-BED COMBUSTION OF PADDY HUSK [J].
BHATTACHARYA, SC ;
SHAH, N ;
ALIKHANI, Z .
APPLIED ENERGY, 1984, 16 (04) :307-316
[3]  
DEJONG W, 2005, CLEAN AIR 2005 8 INT
[4]  
*FAO, 2004, KEY STAT FOOD AGR EX
[5]   Circulating fluidised bed co-combustion of coal and biomass [J].
Gayan, P ;
Adanez, J ;
de Diego, LF ;
García-Labiano, F ;
Cabanillas, A ;
Bahillo, A ;
Aho, M ;
Veijonen, K .
FUEL, 2004, 83 (03) :277-286
[6]   Fuel nitrogen conversion in solid fuel fired systems [J].
Glarborg, P ;
Jensen, AD ;
Johnsson, JE .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2003, 29 (02) :89-113
[7]  
Grubor B. G., 1995, P 13 INT C FLUID BED, V1, P515
[8]   Analysis of heavy metal emission data from municipal waste combustion [J].
Hasselriis, F ;
Licata, A .
JOURNAL OF HAZARDOUS MATERIALS, 1996, 47 (1-3) :77-102
[9]   Interaction of fuels in co-firing in FBC [J].
Hupa, M .
FUEL, 2005, 84 (10) :1312-1319
[10]   Combustion properties of biomass [J].
Jenkins, BM ;
Baxter, LL ;
Miles, TR ;
Miles, TR .
FUEL PROCESSING TECHNOLOGY, 1998, 54 (1-3) :17-46