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Advanced Coal Gasification System—Eltron Research Inc., 4600 Nautilus Court South, Boulder, CO  80301-3241; 303-530-0263, http://www.eltronresearch.com

Dr. James H. White, Principal Investigator, eltron@eltronresearch.com

Mr. James Steven Beck, Business Official, contracts@eltronresearch.com

DOE Grant No. DE-FG02-05ER84200

Amount:  $750,000

 

The efficient, clean, and cost effective conversion of coal is a principal goal of the U.S. energy industry and the DOE.  Although still costly, coal gasification remains the most effective method for converting the raw feedstock into syngas for liquid fuel production, for hydrogen production (for fuel cell use), or for combustion in a gas turbine generator.  In order to reduce capital costs, this project will develop technology for integrating fluidized bed gasification with chemical looping to allow gasification under less severe conditions.  In particular, the technology eliminates cryogenic air separation and enables CO2 sequestration.  Phase I identified oxygen carrier materials and demonstrated the integration of air separation and coal gasification in chemical looping.  Preferred catalyst materials not only were extremely inexpensive, but also exhibited an oxygen storage capacity as high as 30 wt% and proved to be rugged even with minimal processing.  When incorporated into a fluidized bed reactor, the gasification system exhibited carbon conversion greater than 98% and cold gas efficiency greater than 70%, at a bed temperature less than 850°C.   These results easily exceeded the performance of other fluidized bed gasification processes while enabling CO2 sequestration.  Phase II will consist of the final selection and development of catalyst materials; design, fabrication, and testing of a pilot scale chemical looping system; and employment of the system in chemical looping coal gasification and other potential applications. 

 

Commercial Applications and other Benefits as described by the awardee:   The technology should provide capital savings in coal gasification processes by eliminating the air separation unit, reducing plant cost by a significant amount (~20%).  These savings should make the technology attractive in combined cycle, hydrogen production, coal-to-liquids, commodity chemical production, and other applications.