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Title: Analysis of the SO/sub 2/-lime reaction system: mathematical modeling and experimental studies with emphasis on stoker applications

Thesis/Dissertation ·
OSTI ID:5491829

This study examines the application of the pulverized, dry limestone injection process to stoker-fired boilers using a comprehensive mathematical model of the SO/sub 2/-lime reaction in conjunction with a series of bench-scale experiments. The mathematical model was also used to assess the application of limestone injection for pulverized, coal-fired boilers. Model predictions and SO/sub 2/ capture data led to the conclusion that the best description of the reaction process was one incorporating an intrinsically zero-order chemical sulfation reaction serially with pore and product layer diffusion steps. Model predictions showed that sulfur capture increased linearly with increasing Ca/S molar ratio. The predicted apparent dependence on SO/sub 2/ concentration varied from zero- to first-order depending on particle size and reaction conditions. For time-temperature histories typical of boilers, the model demonstrated that the optimum limestone injection location is at the highest temperature at which sulfation is thermodynamically possible (ca. 2250/sup 0/F at 3000 ppm SO/sub 2/). Bench-scale experiments using a pulverized limestone sorbent showed that SO/sub 2/ capture increased roughly linearly with increasing molar Ca/S ratio. The effects of changes in SO/sub 2/ partial pressure were small. The introduction of cooling coils in the bed region of the test facility had no significant impact on SO/sub 2/ capture. Capture levels obtained with natural gas doped to 3000 ppm of SO/sub 2/ at Ca/S = 2 ranged from 25 to 30%. With high sulfur Illinois coal at Ca/S = 2 the capture was 35%. Comparisons of the model to the data showed good agreement at all conditions.

Research Organization:
Utah Univ., Salt Lake City (USA)
OSTI ID:
5491829
Resource Relation:
Other Information: Thesis (Ph. D.)
Country of Publication:
United States
Language:
English