Performance Characteristics of Pilot-Scale Indirect Plasma and Chemical System Used for the Removal of \hbox From Boiler Emission
The process of removing NO x from the flue gas emitted from a smoke-tube boiler was investigated using an ozonizer, which is used for carrying out the indirect oxidation of NO, and a Na 2 SO 3 chemical scrubber. The flow rate of the flue gas was in the range of 410 - 1480 N·m 3 /h, its temperature w...
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Veröffentlicht in: | IEEE transactions on industry applications 2010-09, Vol.46 (5), p.1707-1714 |
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Hauptverfasser: | , , , , , , |
Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | The process of removing NO x from the flue gas emitted from a smoke-tube boiler was investigated using an ozonizer, which is used for carrying out the indirect oxidation of NO, and a Na 2 SO 3 chemical scrubber. The flow rate of the flue gas was in the range of 410 - 1480 N·m 3 /h, its temperature was in the range of 185°C- 325°C, and the concentration of NO x was approximately 40 ppm during the combustion of city gas. Operational and performance data were obtained from the experiments. The efficiency of the NO x removal process was clearly dependent on the oxidation reduction potential (ORP), and it increased with a decrease in the ORP of the scrubbing solution. To effectively remove the requisite amount of NO x , it is essential to maintain the ORP by controlling the injection rates of the Na 2 SO 3 solution and maintaining an ORP of less than 0 mV and the rate of change in ORP to less than 0 mV/min. More than 4 kg/h of Na 2 SO 3 must be added to the scrubber in order to sustain the aforementioned ORP condition of the scrubbing solution. The amount of NO x emitted from the flue gas was maintained as less than 4 ppm at a flue gas flow rate of 410 N ·m 3 / h during a 300-min continuous system operation by maintaining an ORP of -30 mV and a pH of more than 7.8 for the scrubbing solution. |
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ISSN: | 0093-9994 1939-9367 |
DOI: | 10.1109/TIA.2010.2057490 |