Abstract

Co-combustion of coal and sewage sludge is known as one of the most effective thermal treatments for sludge use and disposal. However, multiple pollutants emitted from this process, especially heavy metal mercury emission, have become a worldwide concern on the environment and public health. An experimental study on mercury emission and its speciation from co-combustion of sludge and coal was conducted in a circulating fluidized-bed incinerator with a fluidized-bed cross-section of 0.23 x 0.23 m and a total height of 7 m. Mercury speciation in flue gas and mercury contents in fly and bottom ashes were measured on the basis of the Ontario Hydro method. The mercury mass balance of the co-combustion process was calculated. Effects of some major factors, such as Ca/S molar ratio, desulfurization sorbent categories, excess air coefficient, and SO 2 and NO x concentrations, on the distribution of mercury speciation were investigated. Results showed that most of the mercury from the mixed fuel of the coal and sludge went into the flue gas, in which elemental mercury was the major species. A small amount of mercury remained in the fly ash, and none of the mercury was detected in the bottom ash. As desulfurization sorbents, both CaO and CaCO 3 can remove Hg 2+ in flue gas effectively, but CaO had a bigger capacity than CaCO 3 . The percentage of Hg 2+ in flue gas was found added with an increase of SO 2 and NO x concentrations. It can be concluded that an excess air coefficient exerted dominant influences on the distribution of mercury species among flue gas, fly ash, and bottom ash.

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