Fly ash penetration through electrostatic precipitator and flue gas condenser in a 6 MW biomass fired boiler

被引:88
作者
Strand, M
Pagels, J
Szpila, A
Gudmundsson, A
Swietlicki, E
Bohgard, M
Sanati, M [1 ]
机构
[1] Vaxjo Univ, Dept Bioenergy Technol, SE-35195 Vaxjo, Sweden
[2] Lund Univ, Div Ergon & Aerosol Technol, SE-22100 Lund, Sweden
[3] Lund Univ, Div Nucl Phys, SE-22100 Lund, Sweden
关键词
D O I
10.1021/ef020076b
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
The effects of an electrostatic precipitator and a flue gas condenser on size resolved fly ash particle concentration and composition were studied in a 6 MW biomass combustion unit, fired with moist forest residue. The boiler was of moving grate type. The fly ash particles were sampled upstream and downstream of the electrostatic precipitator and flue gas condenser, respectively. Fine particle number size distributions were measured using an electric mobility spectrometer (SMPS) and coarse particle number size distributions were measured using a time-of-flight instrument (APS). The mass size distributions were measured using a multi-jet low pressure cascade impactor (DLPI). For chemical analyses of the impactor substrates particle induced X-ray emission analysis (PIXE) was used. After the flue gas passed the electrostatic precipitator (ESP), the fly ash particle concentration was reduced by approximately 96% by number and 83% by mass. After the particles passed the flue gas condenser, particle number concentration was only marginally altered, whereas the mass concentration was reduced by half. Both the ESP and the condenser showed, size dependent particle separation efficiency. The main elements (Z > 12) in the fine fly ash fraction were K, S, and Cl, whereas the main elements in the coarse fraction were Ca, K, S, and Cl. After passing the ESP the mass ratio of Ca decreased in the coarse fraction, while the ratios of K, S, and Cl increased, indicating transference of fly ash material from the fine to the coarse particle fraction. There was no significant difference in the elemental composition for any particle size fraction sampled upstream or downstream of the condenser.
引用
收藏
页码:1499 / 1506
页数:8
相关论文
共 27 条
[1]  
BIEDERMANN F, 1998, P 10 EUR C TECHN EXH, P1340
[2]   Control of toxic metal emissions from combustors using sorbents: A review [J].
Biswas, P ;
Wu, CY .
JOURNAL OF THE AIR & WASTE MANAGEMENT ASSOCIATION, 1998, 48 (02) :113-127
[3]  
BROOKS, 1994, FUEL PROCESS TECHNOL, V39, P219
[4]   Influence of the elemental composition of individual fly ash particles on the efficiency of the electrostatic precipitators [J].
Cereda, E ;
Marcazzan, GMB ;
Pedretti, M ;
Grime, GW ;
Baldacci, A .
JOURNAL OF AEROSOL SCIENCE, 1996, 27 (04) :607-+
[5]   The formation of submicron aerosol particles, HCl and SO2 in straw-fired boilers [J].
Christensen, KA ;
Stenholm, M ;
Livbjerg, H .
JOURNAL OF AEROSOL SCIENCE, 1998, 29 (04) :421-444
[6]   LOW-RESISTIVITY RELATED ESP PERFORMANCE PROBLEMS IN DRY SCRUBBING APPLICATIONS [J].
DURHAM, MD ;
RUGG, DE ;
RHUDY, RG ;
PUSCHAVER, EJ .
JOURNAL OF THE AIR & WASTE MANAGEMENT ASSOCIATION, 1990, 40 (01) :112-124
[7]  
Hasler P, 1998, BIOMASS FOR ENERGY AND INDUSTRY, P1330
[8]   A model for the air emissions of trace metallic elements from coal combustors equipped with electrostatic precipitators [J].
Helble, JJ .
FUEL PROCESSING TECHNOLOGY, 2000, 63 (2-3) :125-147
[9]  
JAKOBSEN HH, 1991, FLUE GAS CONDENSATIO
[10]   The dynamics of aerosols in condensational scrubbers [J].
Johannessen, T ;
Christensen, JA ;
Simonsen, O ;
Livbjerg, H .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (15) :2541-2556