Abstract

Slagging combustors with injected lime or limestone are being considered as replacements for conventional coal burners. They have advantages in that they can be staged to reduce NO{sub x} and SO{sub x} emissions. Iron oxide, as an alternative to lime or limestone may be effective not only as a desulfurizing agent, but under the right conditions of oxygen potential and after combination with sulfur, the reaction products of coal gases with iron oxide can act as a flux to produce a fluid phase. The thermodynamic conditions for optimum removal of sulfur from the first stage of a coal combustor are being determined by experiment and by use of existing data. Analysis of the phase equilibria indicates that optimum conditions for deployment of the reducing stage of a multi-stage burner operating with iron injection are close to the boundary of the liquid iron oxysulfide phase with iron-saturation. In this quarter, three sets of experiments are being conducted: Equilibration at 1400{degree}C between gas atmospheres containing oxygen and sulfur at controlled chemical potentials over oxysulfide melts to determine activity/composition relationships for the ternary isotherm in the Fe-O-S system, Kinetics of reactions on milligram-scale between magnetite in a thermogravimetric device in simulated coal/gas atmospheres which are optimum for desulfurization, and Studies on a 3 million btu per hour burner located at a local utility plant (Northern States Power, High-Bridge Plant in Saint Paul, MN) in which magnetite is injected into simulated coal gas atmospheres (produced by combustion of acetylene [C{sub 2}H{sub 2}]) under reducing conditions.

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