This is the fifteenth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. At AEP's Gavin Plant, data from the corrosion probes showed that corrosion rate increased as boiler load was increased. During an outage at the plant, the drop in boiler load, sensor temperature and corrosion rate could all be seen clearly. Restarting …
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This is the fifteenth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. At AEP's Gavin Plant, data from the corrosion probes showed that corrosion rate increased as boiler load was increased. During an outage at the plant, the drop in boiler load, sensor temperature and corrosion rate could all be seen clearly. Restarting the boiler saw a resumption of corrosion activity. This behavior is consistent with previous observations made at a 600MWe utility boiler. More data are currently being examined for magnitudes of corrosion rates and changes in boiler operating conditions. Considerable progress was made this quarter in BYU's laboratory study of catalyst deactivation. Surface sulfation appears to partially suppress NO adsorption when the catalyst is not exposed to NH3; NH3 displaces surface-adsorbed NO on SCR catalysts and surface sulfation increases the amount of adsorbed NH3, as confirmed by both spectroscopy and TPD experiments. However, there is no indication of changes in catalyst activity despite changes in the amount of adsorbed NH3. A monolith test reactor (MTR), completed this quarter, provided the first comparative data for one of the fresh and field-exposed monolith SCR catalysts yet developed in this project. Measurements of activity on one of the field-exposed commercial monolith catalysts do not show significant changes in catalyst activity (within experimental error) as compared to the fresh catalyst. The exposed surface of the sample contains large amounts of Ca and Na, neither of which is present in the fresh sample, even after removal of visibly obvious fouling deposits. However, these fouling compounds do not deactivate the catalyst to the extent that these same poisons do in the deliberately wet-impregnated laboratory-prepared samples (1%V{sub 2}O{sub 5}-9%WO{sub 3}/TiO{sub 2}). At least in this case, the fouling deposits generated by field exposure present little if any chemical deactivation or barrier to mass transfer. During this quarter, the slipstream reactor at Rockport operated for 1000 hours on flue gas. Periodic NO{sub x} reduction measurements were made, showing some decrease in activity relative to fresh catalyst samples. Plans are being made to take the reactor out of service at the Rockport plant and move it to Plant Gadsden. At Gadsden, inlet and outlet ports were installed on Unit 1 for the slipstream reactor during an outage.
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Bockelie, Mike; Davis, Kevin; Linjewile, Temi; Senior, Connie; Eddings, Eric; Whitty, Kevin et al.NOx Control Options and Integration for US Coal Fired Boilers Quarterly Progress Report: January-March 2004,
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March 31, 2004;
United States.
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