Continuous NO and NH3 measurements in deNOx installations
Conference
·
OSTI ID:560481
The ammonia (NH{sub 3})/aqueous urea injection concept has been used extensively as a secondary deNO{sub x} method for many years. The basic technology involves spraying ammonia or aqueous urea into the flue gas either over a catalyst or in a temperature zone, encouraging the oxides of nitrogen to dissociate into atomic nitrogen and water vapor. Although this injection results in a beneficial reduction in NO{sub x}, it comes with its own set of drawbacks. At some point, additional NH{sub 3} will no longer react with NO{sub x} and will pass, or {open_quotes}slip{close_quotes} by the catalyst and/or temperature zone. This is commonly termed {open_quotes}ammonia slip.{close_quotes} Monitoring this {open_quotes}slip{close_quotes} is an important control parameter for any deNO{sub x} system, given the costs of commercially available ammonia and the fact that ammonia is defined as a pollutant by many of the regulatory authorities. Plant attempt to operate with the lowest {open_quotes}slip{close_quotes} possible while maintaining an acceptable deNO{sub x} effect. In addition, ammonia is an aggressive and elusive substance, proving very difficult to measure in a flue gas scenario. It partitions with particulate material and also forms a variety of salts with other flue gas constituents. This requires the gas measurement close to the secondary deNO{sub x} process. This cost, along with the detrimental physical and environmental effects of ammonia, make {open_quotes}ammonia slip{close_quotes} control important, thus the focus of this paper.
- OSTI ID:
- 560481
- Report Number(s):
- CONF-961232--
- Country of Publication:
- United States
- Language:
- English
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