SBIR-STTR Award

Development of a rotary combustor for refiring pulverized coal boilers
Award last edited on: 3/25/2002

Sponsored Program
SBIR
Awarding Agency
DOE
Total Award Amount
$674,842
Award Phase
2
Solicitation Topic Code
-----

Principal Investigator
Michael J Virr

Company Information

Spinheat Limited

1222 Bronson Road
Fairfield, CT 06824
   (203) 259-6101
   virrmj@prodigy.net
   N/A
Location: Single
Congr. District: 04
County: Fairfield

Phase I

Contract Number: ----------
Start Date: ----    Completed: ----
Phase I year
1993
Phase I Amount
$75,000
The rotary combustor (RC) is being developed to refireconventional pulverized coal burners in order to reduce sulfuroxides (SO.) and nitrogen oxides (NO.) in utility boilers bymeans of combustion modification. The burner comprises a slowlyrevolving, perforated drum. Granular coal and limestone areintroduced into the revolving drum, where they are fluidizedagainst the artificial gravity caused by centrifugal(centripetal) force; the coal gasifies, and sulfur combines withthe limestone in the normal way. The resultant coal gas is thenpassed through a DENO tube, where the fuel nitrogen is fixed,before being introduced into the original combustion chamber withfinal (tertiary) air and burned in a conventional flame. The RCis installed on the burner wall of a conventional coal boiler toreplace the existing burners and milling equipment, thuseliminating the power consumption of the mills and raisingefficiency. Limestone is fed in with the coal to capture thesulfur within the RC which is very effective as the temperaturerange of the rotating fluidbed is controlled. Thus, sulfur capturein excess of 90% is predicted. The RC incorporates a cooledfiretube with secondary and tertiary air admission, therebyreducing NO. to significantly lower levels than conventionalburners. The Phase I objective is to demonstrate the feasibilityof using the RC by establishing the design details and costs, demonstrating mechanical details on a cold model, and developingthe design to a practical stage. The design of a unit to test-fireon a 500 lbs/hr (coal) combustion rig would be completed.Anticipated Results/Potential Commercial Applications as described by the awardee:The successful completion of the Phase Idevelopment of the RC would prove the viability of demonstratingthe burner on a reasonably sized boiler test facility with goodinstrumentation. The successful development of the RC would offerutilities the opportunity of refiring their existing coal-firedsteam boilers with burners which would comply with the 1990 CleanAir Act, while realizing a power gain. Both capital and runningcosts of the RC will be substantially less than current flue gasdesulfurization and NO. control, probably being under $1OO/Kw.

Phase II

Contract Number: ----------
Start Date: ----    Completed: ----
Phase II year
1994
Phase II Amount
$599,842
The objective of this project is to demonstrate the feasibility of using the Rotary Combustor (RC) to replace conventional pulverized coal burners as a means of reducing plant emissions on utility and industrial boilers. The RC consists of a slowly revolving, perforated drum in which a shallow bed of coal ash and limestone is held in suspension by substoichiometric air. Granular coal and limestone are introduced into the drum where coal is partially burned and limestone is calcined. The resultant fuel gas is then blown through a firetube where secondary air is added and nitrogen is fixed by disassociating the NOX precursors before the gas is allowed into the combustion chamber. Combustion is then completed in a conventional flame. The RC is installed on the burner wall of the coal boiler to replace the existing burners and milling equipment, thus eliminating the power consumption of the mills and raising overall plant efficiency. Limestone is fed in with the coal to capture the sulfur in the rotary gasifier section, which is very effective as the temperature window is controlled. Thus, sulfur capture of over 90% is achievable. The RC incorporates a firetube which stages combustion, thereby reducing NOy to significantly lower levels than other burners, that is, below 100 parts per million by volume. Therefore, the RC addresses both SOx and NOX reduction in the same burner. The Phase II objective is to complete the detailed design of a 6.8 mBTU/hour unit, then manufacture and test the RC on a commercial manufacturer's package boiler test rig. A test schedule has been drawn up in cooperation with the Pittsburgh Energy Technology Center in which it is intended to test the unit on both medium and high sulfur coal while simultaneously measuring both SOx and NOy, as well as the combustion performance indicator CO. A series of parametric tests will be carried out with professional emission monitoring. The RC will also be demonstrated to utilities, coal companies, and other interested parties. Anticipated Results /Potential Commercial Applications as described by the awardee:The demonstration of the RC by firing into a package boiler with simultaneous low emissions of SOx and NOX should be a convincing demonstration of the burner. The successful development of the RC should offer utilities and industrial boiler users the opportunity of refiring existing coalfired steam boilers with burners that should comply with Phase II of the Clear Air Act Amendment of 1990, while realizing a power gain. Both capital and running costs of the RC will be substantially less than current fuel gas desulfurization and DeNOx control of approximately $100Aiw.