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Title: Removal of SO/sub 2/ and NO/sub x/ from stack gas by reaction with calcium hydroxide solids

Conference ·
OSTI ID:6264694

Previous workers have shown that simultaneous SO/sub 2//NO/sub x/ removal can be obtained in a dry scrubbing system with Ca(OH)/sub 2/ promoted by an additive such as NaOH, and that fly ash and product recycle improve the reactivity of the solids toward SO/sub 2/. To test SO/sub 2//NO/sub x/ removal with fly ash and product recycle, bench-scale experiments with a packed bed reactor were performed at bag filter conditions. The most reactive solid for NO/sub x/ removal was prepared by slurrying Ca(OH)/sub 2/ with fly ash, CaSO/sub 3/, and NaOH. The best conditions for NO/sub x/ removal were the highest temperature (125/sup 0/C) and greatest concentrations of SO/sub 2/ (1500 ppm) and O/sub 2/ (20%). At the best conditions, NO/sub x/ removed in 1 hour was 3 - 4 moles per 100 moles Ca(OH)/sub 2/, compared to 5 - 10 moles SO/sub 2/ removed per 100 moles Ca(OH)/sub 2/. The best SO/sub 2/ removal was obtained at the highest relative humidities/lowest temperatures (55% RH/65/sup 0/C) with solids prepared by slurrying Ca(OH)/sub 2/ with flyash and NaOH. At these conditions, SO/sub 2/ removed in 1 hour was 60 - 80 moles per 100 moles Ca(OH)/sub 2/, compared to 0.5 to 1 moles NO/sub x/ removed per 100 moles Ca(OH)/sub 2/.

OSTI ID:
6264694
Report Number(s):
CONF-870323-
Resource Relation:
Conference: American Institute of Chemical Engineers spring national meeting, Houston, TX, USA, 29 Mar 1987; Other Information: Technical Paper 78E
Country of Publication:
United States
Language:
English

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