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A laboratory study of Hg oxidation catalyzed by SCR catalysts Karin Madsen on 05.10.2010 at CHEC Annual Day Anker Degn Jensen Joakim Reimer Thøgersen Flemming Frandsen
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DTU Chemical Engineering Technical University of Denmark Outline •Background •Laboratory Study •Conclusions
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DTU Chemical Engineering Technical University of Denmark Background •1930 tons of mercury was emitted in 2005 (Pacyna, 2010) –45% comes from combustion of fossil fuels •Existing air pollution control devices offers an economically feasible option for mercury control •Mercury species in flue gases from power plants –Hg 0 : Volatile, difficult to capture –Hg 2+ : Water soluble, can be captured in a wet scrubber –Hg p : Can be captured in particulate control devices •Mercury speciation is highly dependent on coal type/rank and operating conditions
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DTU Chemical Engineering Technical University of Denmark Mercury oxidation and the SCR •Mercury is oxidized by halogens in the flue gas •(Potential) net reaction Hg 0 + 2 HCl + 1/2 O 2 = HgCl 2 + H 2 O •SCR catalysts for NOx-control also have catalytic activity on the mercury oxidation –The combination SCR + wet FGD can offer >90% mercury capture
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DTU Chemical Engineering Technical University of Denmark Laboratory Setup at Topsoe A/S
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DTU Chemical Engineering Technical University of Denmark Mercury oxidation and Chlorine
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DTU Chemical Engineering Technical University of Denmark Mercury Oxidation and Ammonia
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DTU Chemical Engineering Technical University of Denmark Mercury Oxidation: Laboratory versus Pilot-scale data
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DTU Chemical Engineering Technical University of Denmark Conclusion: Close Gap between Laboratory and Pilot- Scale Data •Difference in gas matrix –Laboratory Simulated flue gas containing Hg 0, O 2, H 2 O, NH 3, HCl and N 2 –Pilot Real flue gas from subbituminous coal combustion including NO, SO 2, and fly ash •Factor 10-20 difference in catalyst activity must be due to difference in gas matrix •Future work involves testing of more complex gas matrices including NO and SO 2
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