Abstract:The feasibility of the regenerative limestone slurry process was demonstrated on a bench scale. CaCOB and H2S were recovered from waste sludge from the limestone slurry flue gas desulfurization process. CaC03 would be recycled to the scrubber. H2S would be converted to elemental sulfur in a Clause plant. At 950-980 "C in the presence of coke or coal, 95% of the Cas04 and Cas03 in the dry sludge was reduced to Cas. The rate-determining reaction was the reduction of Cas04 to Cas. The estimated rate constant for … Show more
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