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Title: Tests to produce and recover carbon dioxide by burning coal in oxygen and recycled flue gas: Black Hills Power and Light Company Customer Service Center Boiler No. 2, Rapid City, South Dakota

Technical Report ·
DOI:https://doi.org/10.2172/5500326· OSTI ID:5500326

Experiments were conducted using a modified stoker-fired boiler (2.2 x 10/sup 6/ Btu/h) instrumented to examine the feasibility of producing and recovering carbon dioxide by burning coal in oxygen and recycled flue gas in a utility environment. The tests demonstrated that the boiler can be operated in the oxygen-blown/flue-gas-recirculation mode without any noticeable effects on coal combustion, heat delivery to the water, or the coal-feed or ash-handling systems. Pretest calculations showed that a feasible set of operating parameters for a carbon-dioxide-producing combustor system tightly sealed against air infiltration and containing no more than about 5% O/sub 2/ (dry basis) at the furnace exit would be a flue-gas recycling ratio between 0.6 and 0.7 and an oxygen feed rate of 1.17 g-moles per g-atom of carbon, yielding an exhaust gas composition (wet basis) of approximately 46.9% CO/sub 2/, 50.6% H/sub 2/O, and 2.5% O/sub 2/. This composition corresponds to a product gas containing 95% CO/sub 2/ and 5% O/sub 2/ (dry basis). However, because air leaked into the test combustor and the flue-gas handling system, the highest carbon dioxide concentration achieved in the exhaust gas was 48.5% (dry basis). Major sources of inleakage were the furnace brickwork, the gas-handling system, and the coal-feed and ash-extraction systems. 40 figs.

Research Organization:
Argonne National Lab. (ANL), Argonne, IL (United States)
DOE Contract Number:
W-31109-ENG-38
OSTI ID:
5500326
Report Number(s):
ANL/CNSV-61; ON: DE88005570
Resource Relation:
Other Information: Portions of this document are illegible in microfiche products
Country of Publication:
United States
Language:
English