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Title: Influence of CO{sub 2} and O{sub 2} on the reaction of Ca(OH){sub 2} under spray-drying flue gas desulfurization conditions

Journal Article · · Industrial and Engineering Chemistry Research
DOI:https://doi.org/10.1021/ie9600506· OSTI ID:404546
; ;  [1]
  1. National Taiwan Univ., Taipei (Taiwan, Province of China). Dept. of Chemical Engineering

The influence of CO{sub 2} and O{sub 2} in the flue gas on the reaction of hydrated lime sorbent with SO{sub 2} was studied using a fixed-bed differential reactor under conditions prevailing in the spray-drying flue gas desulfurization process. With the presence of CO{sub 2}, the sulfation and carbonation reactions of Ca(OH){sub 2} took place simultaneously until Ca(OH){sub 2} ceased to react. The CaCO{sub 3} produced reacted further to form CaSO{sub 3}{center_dot}{1/2}H{sub 2}O. The apparent sulfation rate, total reaction rate, and final total conversion of Ca(OH){sub 2} were greater than those for the case without CO{sub 2}. The final total conversion was about 1.45 times that for the latter case at the conditions of 1,000 ppm SO{sub 2}, 60 C, and 70% relative humidity. The same effect was observed whether CO{sub 2} was present with O{sub 2} or not. Kinetic expressions obtained by assuming chemical reaction control and considering the surface coverage by product crystals best represented the kinetic data.

OSTI ID:
404546
Journal Information:
Industrial and Engineering Chemistry Research, Vol. 35, Issue 11; Other Information: PBD: Nov 1996
Country of Publication:
United States
Language:
English

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