Emissions from cofiring coal, biomass and sewage sludge
نویسنده
چکیده
The practice of cofiring biomass in full-scale coal utility plants is increasing, due to the benefits of reduced fossil fuel based CO2 emissions. Biomass also tends to have a lower sulphur content than coal and therefore emissions of SO2 can be reduced. The same is true for NOx emissions from lower fuel nitrogen content. Further, the lower flame temperatures and different combustion stoichiometry of biomass systems can also result in lower thermal NOx production. A reduction in ash, especially when cofiring wood, is another advantage. Increased chlorine and/or changes in ash particle adsorbency can help reduce trace element emissions such as mercury and arsenic. However, some biomass materials, such as straw and grass, can have higher potassium and chlorine than coal which may lead to problems such as slagging and fouling. There are also potential issues with respect to changes in the operation of pollution control technologies. For example: phosphorus in sewage sludge can react with lime to reduce sulphur capture in fluidised bed systems; sewage sludge tends to have higher concentrations of several trace elements such as Cr, Cu, Ni, Pb, Zn and Fe. It has been shown that these elements tend to end up in the fly ash and it is important to ensure that this does not result in limitations on the intended use of such ash. In most cases, the balance between the characteristics of the coal and biomass and the plant operation can control any negative plant effects. In practice, full-scale coal-fired plants such as Drax in the UK and Fiume Santo in Sardinia note little or no detrimental change in trace element emissions following the introduction of biomass as a co-fuel. It would appear that, for the most part, the benefits of cofiring biomass far outweigh any negative effects. In fact, it would seem that the majority of environmental impact assessments regard the production, transport and preparation of the biomass fuels as more important than changes in the stack emissions from the plant as a result of the cofiring. Detrimental effects, however, can be an issue for ash management. ASTM American Standards for Testing and Materials BFBC bubbling fluidised bed combustion CFBC circulating fluidised bed combustion DDGS dried distilled grains with solubles EC European Commission EDF Electricité de France EL emission limit EU European Union ESP electrostatic precipitator FBC fluidised bed combustion FGD flue gas desulphurisation FIP feed-in premium FIT feed-in tariff IEA International Energy Agency IEA CCC IEA Clean Coal Centre IPC Integrated Pollution Control, UK LCPD Large Combustion Plant Directive, EU MBM meat and bone meal MMBtu million British thermal units MSW municipal solid waste Mtoe megatonne of oil equivalent MWe megawatt electric MWth megawatt thermal NOx nitrogen oxides (NO and NO2) OHM Ontario Hydro Method PAH polycyclic aromatic hydrocarbons PCDD polychlorinated dibenzo dioxin PCDF polychlorinated dibenzo furan PFBC pressurised fluidised bed combustion PKS palm kernel shells RDF refuse derived fuel ROC Renewable Obligation Certificate, UK SCEM PS® Analytical continuous emissions monitoring system SCR selective catalytic reduction SFBC swirling fluidised bed combustion TOC total organic carbon WDF waste derived fuel WID Waste Incineration Directive, EU 2 IEA CLEAN COAL CENTRE Acronyms and abbreviations
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Mercury emissions during cofiring of sub-bituminous coal and biomass (chicken waste, wood, coffee residue, and tobacco stalk) in a laboratory-scale fluidized bed combustor.
Four types of biomass (chicken waste, wood pellets, coffee residue, and tobacco stalks) were cofired at 30 wt % with a U.S. sub-bituminous coal (Powder River Basin Coal) in a laboratory-scale fluidized bed combustor. A cyclone, followed by a quartz filter, was used for fly ash removal during tests. The temperatures of the cyclone and filter were controlled at 250 and 150 degrees C, respectively...
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