Utilization of Water Utility Lime Sludge for Flue Gas Desulfurization in Coal-Fired Power Plants: Part III. Testing at a Higher Scale and Assessment of Selected Potential Operational Issues

Abstract

The feasibility of lime sludge utilization for flue gas desulfurization was evaluated by continuing the previous laboratory-scale studies at a higher scale and investigating two potential operational issues, namely viscosity and metal corrosion. Two lime sludge samples and a baseline limestone sample, which were previously characterized and tested for SO 2 capture from a simulated flue gas at a laboratory scale, were first tested at a 10-fold scale with a simulated flue gas, and then tested with a slipstream of flue gas from a coal-fired power plant. The tested lime sludge and limestone slurries reduced the SO 2 concentration of the simulated flue gas from 2000 to <1 ppm, and they demonstrated similar Hg reemission profiles. Field-testing results revealed that the limestone and lime sludge slurries reduced the SO 2 concentration of the flue gas from ~1500 to <1 ppm. These experiments confirmed our previous smaller scale laboratory results that lime sludge can function as a suitable substitute for limestone for SO 2 removal from the flue gas of coal-fired power plants without negatively affecting Hg reemission. Two operational issues, namely viscosity and metal corrosion, were investigated to evaluate practical issues in the transition from limestone to lime sludge at power plants. Results of Marsh funnel viscosity experiments conducted at different solids contents and temperatures indicated the limestone and lime sludge slurries and their gypsum counterparts had similar flow characteristics. Carbon-steel, stainless-steel, and Hastelloy coupons were tested for corrosion by lime sludge and limestone slurries. Both stainless steel and Hastelloy were resistive to corrosion in slurries made from lime sludge or limestone samples or their gypsum counterparts. A considerable but similar amount of corrosion was observed for carbon-steel coupons exposed to lime sludge and limestone slurries. Adding 5000 ppm of Cl − to slurries considerably increased the corrosion rate of carbon steel.

Experimental Study on the Erosion–Corrosion Characteristics of Desulfurization Slurry on Stainless Steel Pipe Materials

“…Wear removed the passivation film from the surface and destroyed the cementite network, resulting in subsurface cracks and deformable hardening, which exacerbated the corrosion. Aiming et al 23 studied wear and corrosion in the pump and found that uniform corrosion and wear occurred in areas below the critical speed value, resulting in slight quality loss. The region where the speed was higher than the critical value was the region of nonuniform tribocorrosion, and the mass loss increased sharply with a rise in speed.…”

“…Dastgheib et al conducted a feasibility test evaluation on flue gas desulfurization of lime sludge. The corrosion resistances of carbon steel and stainless steel under various conditions were tested, and the results indicated that the corrosion resistance of stainless steel in the limestone slurry was obviously better than that of carbon steel.…”