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Combined NO sub x /SO sub 2 removal in spray-dryer FGD systems

Conference ·
OSTI ID:6146414
A combination of modified process conditions and addition of caustic soda to a lime-based spray-dryer system was evaluated for its value in promoting combined NO{sub x}/SO{sub 2} removal from flue gas resulting from the combustion of high-sulfur coal. Small-scale tests at the Pittsburgh Energy Technology Center identified key process parameters. Subsequently, two test series, each about one month in duration, were carried out at Argonne National Laboratory in 1986 and 1988 using a commerical-scale (20 MW electric equivalent) spray-dryer/fabric-filter system. Sprayer-dryer outlet temperature was identified as a key factor, with NO{sub x} removal becoming significant above about 180 F and gradually increasing up to the maximum temperature investigated (210 F). No upper limit on removal with increasing temperature was observed. Removal of NO{sub x} was strongly proportional to baghouse filter-cake thickness; nearly all NO{sub x} removal occurred in the baghouse, with a small net production of NO{sub 2}(<15 ppm). The NO{sub x} removal was also proportional to the SO{sub 2}/NO{sub x} ratio, with little NO{sub x} observed at SO{sub 2}/NO{sub x} ratios less than 2:1. Caustic soda addition improved NO{sub x} removal, at least partially through creation of a more porous and reactive filter cake. Steady-state removals of 70% for SO{sub 2} and 35% for NO{sub x} were easily attained. 10 refs., 9 figs., 3 tabs.
Research Organization:
Argonne National Lab., IL (USA)
Sponsoring Organization:
DOE; USDOE, Washington, DC (USA)
DOE Contract Number:
W-31109-ENG-38
OSTI ID:
6146414
Report Number(s):
ANL/CP-72548; CONF-910331--1; ON: DE91008835
Country of Publication:
United States
Language:
English