Production of Anhydrite From Limestone with Smelter Gases in a Three-Stages Fluidised Bed Reactor

Canadian Institute of Mining, Metallurgy and Petroleum
I Wilkomirsky
Organization:
Canadian Institute of Mining, Metallurgy and Petroleum
Pages:
16
File Size:
1096 KB
Publication Date:
Jan 1, 2007

Abstract

The neutralization of S02 from copper smelter gases to produce calcium sulphate (anhydrite) is considered an attractive alternative to sulphuric acid production. To develop the required technology for the process, a three-stages fluidized bed reactor prototype was designed and operated using both high and low grade limestone and gases with 2, 8 and 12 vol -% S02. The results obtained shows that at 800°C and up to 8 vol-% S02 in the gases, the capture of S02 reaches near 99% with limestone conversion to anhydrite of 45 to 48%. A larger pilot plant is presently being built at the Codelco El Teniente-Caletones Smelter to demostrate the technology and to evaluate the economics of the process. Cu2007
Citation

APA: I Wilkomirsky  (2007)  Production of Anhydrite From Limestone with Smelter Gases in a Three-Stages Fluidised Bed Reactor

MLA: I Wilkomirsky Production of Anhydrite From Limestone with Smelter Gases in a Three-Stages Fluidised Bed Reactor. Canadian Institute of Mining, Metallurgy and Petroleum, 2007.

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