Combustion of coal, bagasse and blends thereof Part II: Speciation of PAH emissions

• Published in: Fuel (Guildford) 2012-06, Vol.96, p.51-58
• Main Authors: BRAGATO, Marcia, JOSHI, Kulbhushan, CARLSON, Joel B, TENORIO, Jorge A. S, LEVENDIS, Yiannis A
• Format: Article
• Language: English
• Subjects: Applied sciences; Biomass; Energy; Energy. Thermal use of fuels; Exact sciences and technology; Fuels; Gas conditioning and treatments. Desulphurization. Liquefaction; Gas industry; Natural energy
• ISSN: 0016-2361; 1873-7153
• DOI: 10.1016/j.fuel.2011.11.069

This work reports on emissions of unburned hydrocarbon species from batch combustion of fixed beds of coal, sugar-cane bagasse, and blends thereof in a pre-heated two-stage laboratory furnace operated in the temperature range of 800-1000 degree C. The effects of fuel blending, combustion staging, and operating furnace temperatures on emissions of pollutants were assessed. Furnace effluents were analyzed for products of incomplete combustion (PICs) including CO, volatile and semi-volatile hydrocarbons, and particulate matter, as has been reported in Ref. [1]. Emitted unburned hydrocarbons include traces of potentially health-hazardous Polycyclic Aromatic Hydrocarbons (PAHs), which are the focus of this work. Under the batch combustion conditions implemented herein, PAH were only generated during the volatile combustion phase of the fuels. The most prevalent species were in descending order: naphthalene, acenaphthylene, phenanthrene, fluoranthene, pyrene, dibenzofuran, benzofuran, byphenyl, fluorene, 9H-fluoren-9-one, acephenantrylene, benzo[b]fluoranthene, 1-methyl-naphthalene; 2-methyl-naphthalene, benz[a]anthracene and benzo[a]pyrene. PAH yields were the highest from combustion of neat bagasse. Combustion of the blends resulted in lower yields of PAH, than combustion of either of their neat fuel constituents. Increasing the furnace operating temperature enhanced the PAH emissions from bagasse, but had little effect on those from the coal or from the blends. Flue gas treatment in a secondary-stage furnace, upon with additional air, typically reduced PAH yields by promoting oxidation of the primary-stage furnace effluents.