Co-firing Characteristics and Slagging Behavior of Sewage Sludge with Coal and Wood Pellet in a Bubbling Fluidized Bed 


Vol. 24,  No. 4, pp. 323-331, Dec.  2018
10.7464/ksct.2018.24.4.323


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  Abstract

The results of an experimental investigation on the co-firing characteristics and slagging behavior of dried and hydrothermal carbonization sewage sludge, sub-bituminous coal, and wood pellet in a fluidized bed were presented. Combustion tests were conducted in a lab-scale bubbling fluidized bed system at the uniform fuel-air equivalence ratio, air flow rate, and initial bed temperature to measure bed temperature distribution and combustion gas composition. 4 different fuel blending cases were prepared by mixing sewage sludge fuels with coal and wood pellet with the ratio of 50 : 50 by the heating value. NOx was mostly NO than NO2 and measured in the range of 400 to 600 ppm in all cases. SO2 was considered to be affected mostly by the sulfur content of the sewage sludge fuels. The cases of hydrothermal carbonization sewage sludge mixture showed slightly less SO2 emission but higher fuel-N conversion than the dried sewage sludge mixing cases. The result of fly ash composition analysis implied that the sewage sludge fuels would increase the possibility of slagging/fouling considering the contents of alkali species, such as Na, K, P. Between the two different sewage sludge fuels, dried sewage sludge fuel was expected to have the more severe impact on slagging/fouling behavior than hydrothermal carbonization sewage sludge fuel.

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  Cite this article

[IEEE Style]

A. HJ, K. DH, L. YJ, "Co-firing Characteristics and Slagging Behavior of Sewage Sludge with Coal and Wood Pellet in a Bubbling Fluidized Bed," Clean Technology, vol. 24, no. 4, pp. 323-331, 2018. DOI: 10.7464/ksct.2018.24.4.323.

[ACM Style]

Ahn HJ, Kim DH, and Lee YJ. 2018. Co-firing Characteristics and Slagging Behavior of Sewage Sludge with Coal and Wood Pellet in a Bubbling Fluidized Bed. Clean Technology, 24, 4, (2018), 323-331. DOI: 10.7464/ksct.2018.24.4.323.