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NOx Control Options and Integration for US Coal Fired Boilers
Author(s) -
Mike Bockelie,
Kristen Davis,
Temi M. Linjewile,
Constance L. Senior,
Eric G. Eddings,
Kevin J. Whitty,
Larry Baxter,
Calvin H. Bartholomew,
William C. Hecker,
Stan Harding
Publication year - 2004
Language(s) - English
Resource type - Reports
DOI - 10.2172/895643
Subject(s) - nox , flue gas , catalysis , boiler (water heating) , sulfation , coal , waste management , selective catalytic reduction , environmental science , chemistry , engineering , organic chemistry , combustion , biochemistry
This is the sixteenth Quarterly Technical Report for DOE Cooperative Agreement No: DEFC26-00NT40753. 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. During an unplanned outage, damage occurred to the electrochemical noise corrosion probes installed at the AEP Gavin plant; testing is expected to resume in August. The KEMCOP corrosion coupons were not affected by the unplanned outage; the coupons were removed and sent for analysis. BYU conducted a series of tests before the ISSR lab was relocated. Ammonia adsorption experiments provided clear evidence of the types of acidic sites present on catalyst surfaces. Data collected this quarter indicate that surface sulfation decreases Lewis acid site concentrations for all catalysts thus far studied, confirming that catalytic activity under commercial coal-based SCR conditions occurs primarily on Br{o}nsted acid sites and would be susceptible to basic impurities such as alkali and alkaline earth oxides, chlorides, and sulfates. SCR activity tests based on MS analysis showed that increasing sulfation generally increases NO reduction activity for both 0% and 1% vanadia catalysts. During this quarter, the slipstream reactor at Rockport operated for 720 hours on flue gas. Catalyst exposure time reached 4500 hours since installation. The reactor is out of service at the Rockport plant and plans are being made to move it to the Gadsden Plant. At Gadsden, modifications have begun in preparation for installation of the slipstream reactor next quarter

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