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Kinetics of the reduction of calcium sulfate with carbon monoxide and hydrogen

Technical Report ·
OSTI ID:6593993
The reductive decomposition of calcium sulfate pellets with both hydrogen and carbon monoxide was studied experimentally in the range of 900 to 1100/sup 0/C. The conditions of the reaction were controlled in order to enhance the formation of calcium oxide while the production of the undesirable calcium sulfide was inhibited; carbon dioxide was used to prevent calcium sulfide formation. Cylindrical calcium sulfate pellets were prepared at a constant compression pressure and reduction was carried out initially at a constant temperature and various reductant gas concentrations. Additional experiments were made with a constant gas phase concentration and various reaction temperatures. Stabilization of the pellet through heating prior to initiating the reduction process was required in order to obtain reliable data. Treatment of the pellet at elevated temperatures caused sintering which reduced the pellet surface area to a value that changed little with additional heating time. Conversions of about 100% were obtained in several hours with both reductant gases at temperatures around 1000/sup 0/C and higher. The rate of calcium sulfate reduction with hydrogen was consistently found to be higher than that with carbon monoxide. The grain model was used to first determine the mechanism controlling the reduction process, then the grain shape factor was evaluated by fitting the data, and finally the parameters involved in the controlling mechanism were calculated. A first-order chemical reaction was found to be the predominant resistance limiting the rate of reduction. The highest correlation factors, around 0.99, were always obtained when a spherical grain shape factor was used in plotting the numerical solution of the governing equation. 42 figures, 3 tables.
Research Organization:
Ames Lab., IA (USA)
DOE Contract Number:
W-7405-ENG-82
OSTI ID:
6593993
Report Number(s):
IS-T-1007; ON: DE83004963
Country of Publication:
United States
Language:
English