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Kinetic Model for the Reaction of Ca(OH)2/Fly Ash Sorbents with SO2 at Low Temperatures
Author(s) -
Chiung-Fang Liu,
ShinMin Shih,
Ren-Bin Lin
Publication year - 2004
Publication title -
industrial and engineering chemistry research
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.878
H-Index - 221
eISSN - 1520-5045
pISSN - 0888-5885
DOI - 10.1021/ie030840x
Subject(s) - sorbent , fly ash , flue gas desulfurization , flue gas , relative humidity , chemistry , reaction rate , chemical engineering , analytical chemistry (journal) , adsorption , chromatography , organic chemistry , thermodynamics , catalysis , physics , engineering
Sorbents prepared with different Ca(OH)2/fly ash weight ratios were reacted with SO2 under conditions similar to those in the bag filters in the spray-drying flue gas desulfurization system. The reaction kinetics was well described by a generalized surface coverage model developed in this study. The model assumes that the sorbent was made up of plate grains and the rate was controlled by the chemical reaction on the grain surface and takes into account the variation in sorbent Ca molar content (M-1) and the surface coverage byproducts. The effect of Ca(OH)2/fly ash weight ratio on the reaction was represented by the effects of the initial specific surface area (Sg0) and M-1 of the sorbent on the kinetic parameters. Under the same reaction conditions, the sorbents with weight ratios ≥ 30/70 had about the same initial reaction rate per unit surface area of the sorbent; their ultimate conversions increased linearly with increasing Sg0, being independent of M-1. The effects of relative humidity, SO2 concentra...

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