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NETL National Energy Technology

Haslbeck XL., Black X, Knehn N., Lewis E., Rutkowski M.D., Woods M., Vaysman V. Pnlverized coal oxy-combustion power plants , US DOE-NETL (National Energy Technology Laboratory) Final report 2007/1291, Revision 2, 2008. [Pg.452]

Penn State University Researchers Discover Inexpensive Way to Clean Up Sulfur Dioxide from Coal Plants. U.S. Department of Energy, National Energy Technology Laboratory, http //www.netl.doe.gov/newsroom/media rel/mr pennst.html... [Pg.48]

The Advanced Gasification Combustion (AGC) project was developed by the National Energy Technology Laboratory (NETL) and General Electric and Environmental Research Corporation (GE-EER), etc. The AGC process is considered to have three fluidized bed reactors. In reactor 1, coal is partly gasified with steam in the presence of a C02 sorbent. The remaining char together with the C02 sorbent is sent to reactor 2. In reactor 2, char is... [Pg.123]

Production Impacts, Mitigation and Risk Management. US Department of Energy (DOE), National Energy Technology Laboratory (NETL). [Pg.43]

Selected Fuel Cell Related URLs DOE National Energy Technology Laboratory www.netl.doe.gov... [Pg.329]

EG G Technical Services, Inc. Fuel Cell Handbook 6th Edition, DOE/NETL-2002/1179 U.S. Department of Energy, Office of Fossil Energy, National Energy Technology Laboratory Morgantown, WV p 2.1-2.26... [Pg.625]

National Energy Technology Laboratory and the United States Department of Energy (NETL-DOE). World wide gasification database online. Pittsburgh, PA. 2002. http //www.netl.doe.gov/publications/ brochures/pdfs/SFAgasifi.pdf (accessed September 16, 2009). [Pg.216]

National Energy Technology Laboratory U.S. Department of Energy 626 Cochrans Mill Road Pittsburgh, PA 15236-0940 412-386-6537 (telephone) 412-386-5920(fax) gamwo netl.doe.gov (email)... [Pg.8]

The next task was to model the reformer itself to understand design issues and be able to predict performance of various reactor/catalyst types and transient behavior. However, upon trying to obtain kinetic rate expressions for the reforming reactions, it was found that very little information existed in the public domain. This led to the decision/need to develop reaction kinetics for catalytic partial oxidation and steam reforming at National Energy Technology Laboratory s (NETL s) onsite research facility. [Pg.338]

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