Direct catalytic decomposition of nitric oxide. Quarterly technical progress report No. 7, April--June 1993
This project investigates a suitable catalyst system for direct NO decomposition in post-combustion gas streams. This process does not use a reductant, such as the ammonia used in Selective Catalytic Reduction (SCR) of NO{sub x} to nitrogen. Therefore, it is greatly simplified process basically involving passing the flue gas through a catalytic converter. Catalysts are prepared by incorporating metal cations into zeolite supports according to ion exchange procedures widely used in preparation of metal/zeolite catalysts. The catalysts of primary interest include copper, palladium, silver and nickel exchanged ZSM-5 catalysts. Particular emphasis is given in this work on promoted Cu-exchanged zeolites, especially the catalyst system Mg/Cu-ZSM-5 and a few others, which are promising for NO conversion to nitrogen at typical flue gas O{sub 2} and NO levels and over the temperature range of 723--873K. The effect of zeolite modification, copper exchange level and catalyst preparation conditions on the catalyst activity are studied in a packed-bed microreactor. Temperature-programmed desorption (TPD) and reduction (TPR) experiments will be carried out in a thermogravimetric analyzer. Kinetic studies of NO and O{sub 2} interaction with catalysts over a wide temperature range as well as catalyst structural investigations are planned.
- Research Organization:
- Massachusetts Inst. of Tech., Cambridge, MA (United States). Dept. of Chemical Engineering
- Sponsoring Organization:
- USDOE, Washington, DC (United States)
- DOE Contract Number:
- FG22-91PC91293
- OSTI ID:
- 10179351
- Report Number(s):
- DOE/PC/91293--T3; ON: DE93040709
- Country of Publication:
- United States
- Language:
- English
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AIR POLLUTION CONTROL
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20 FOSSIL-FUELED POWER PLANTS
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AIR POLLUTION CONTROL
CATALYSTS
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NOXIOUS GAS AND PARTICULATE EMISSIONS
PALLADIUM
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SILVER
TEMPERATURE DEPENDENCE
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