AFBC boilers firing coal are not competitive with oil or gas .. versa. The disadvantage of an EHE is that it complicates the design and operation of the unit . There are more than 42 nos AFBC boilers operating worldwide which were designed as per Doosan Power System design and supplied either directly from the. It would be pointless to put whole Atmospheric Fluidised Bed Combustion (AFBC ) Boiler knowledge here. But from a quick search within Quora and Google you.

Author: Bragore Samushura
Country: Guyana
Language: English (Spanish)
Genre: Education
Published (Last): 7 June 2005
Pages: 153
PDF File Size: 1.97 Mb
ePub File Size: 17.35 Mb
ISBN: 934-2-65721-176-5
Downloads: 10653
Price: Free* [*Free Regsitration Required]
Uploader: Kejora

Data available from commercial operating facilities, although limited, are also presented. Cost Equations for Industrial Boilers. Each algorithm is an algebraic function which projects capital and annual costs for a particular system based on key process parameters e.

Atmospheric Fluidised Bed Combustion Boiler (AFBC)

The development of the FBC algorithm is described in this chapter as well as validation of the algorithm boi,er vendor-developed cost estimates.

This design basis was significantly more elaborate than the ITAR basis. To further test the validity boielr the FBC cost projections, it is desirable to compare them with independent estimates developed by other workers. Issues which have contributed to a lag in the commercial development of PFBC as compared to AFBC technology include 1 the ability of the flue gas cleanup device to reduce solids loadings to the gas turbine to acceptable levels, and 2 the increased complexity of the process.

Fib Up to Fx. Freeboard height at the TVA unit is over 20 feet compared to near 10 feet for a typical industrial fluidized bed opeartion. The current fuel is a 3 percent sulfur coal.

City of Vastervlk Babcock Power Ltd.

Advantages of AFBC (Atmospheric Fluidized Bed Combustion) Boiler – ASKPOWERPLANT

This set of conditions corresponds closely to the FBC boiler design case of 30 percent S02 removal on a Type H coal, as identified in Table 6. These formulas are presented in Table 6. Manufacturers currently offering commercial AFBC units, along with existing and planned units, are presented.

The limestone is added for S02 removal.


The research in the pilot programs is generally directed at the fundamental properties, rates, and mechanisms of AFBC systems as well as testing the feasibility of using low-grade fuels and alternate sorbents.

Insufficient information was provided with the JB cost description to make adjustments for annual costs.

In this range, N0x emissions rise sharply as the air flow is increased. The FBC boiler design operatkon a primary cyclone for solids recycle. The experimental results and theoretical considerations discussed in the ITAR indicate that “small particle sizes in afvc range, of urn and sufficiently long gas phase residence time 0.

These boiler designs have been used for both retrofit and new installations. Heat inputs to the plants were not specified but were estimated from the steam rate, steam conditions, and an assumed boiler efficiency of 85 percent.

Goodstine of Combustion Engineering, Inc.

Gas residence time is the time period required for a unit volume of gas to pass through the bed and is defined as the ratio of the expanded bed height to the superficial velocity. Combuster included a dense bed section to enhance reactivity. The costs associated with waste stream disposal are highly site-specific and are influenced by noiler following parameters: Temperature depends un customer requirements.

Goiler allowance for performance tests 1 percent of total direct costs was added. The model also takes into operatiob factors such as coal-ash alkali sulfur capture, the volume fraction of bed bubbles, bed voidage in the emulsion phase, the fraction of emulsion volume occupied by inerts, and the fraction of bed volume occupied by heat transfer surface.

References 9 and 10 detail the specific equipment lists and assumptions used to develop the boiler algorithms presented in Appendix A and Reference Allowable emissions of particulate matter PM and NO are maintained at consistent levels for all S02 control levels examined.

In addition to the solids recycle provided by the circulating bed, the capability exists for recycle of solid materials collected from the flue gas downstream of the circulating bed.

To achieve the same competitive edge over compliance coal combustion, low sulfur coals prices would have to rise almost 65 percent relative to high sulfur coal, or FBC relative capital costs would have to decline by over 60 percent, or a combination of the two shifts would have to occur.


Conversely, FGD capital costs would have to rise by 73 percent to accomplish the same effect.

As was the case in Table 6. An average fuel combination contains approximately 2 percent sulfur. The CE estimate is based on detailed equipment designs and layout and internal cost files. A complete listing of the algorithms is provided in Appendix A and Reference Research and development conducted by private industry is directed more at the optimization of parameters affecting AFBC operation.

The fluidized bed consisting of unreacted, calcined, and sulfated limestone particles, coal, and ash is suspended in a stream of combustion air blowing upwards from an air distribution plate. Ahlstrom Dy No f. In addition, the fuel prices have been “levelized” over the life of the boiler i. They can be designed to burn either a single or multiple fuels. Emissions of NO averaged 0. For abrasive fuels, special design considerations and provision of sacrificial shields.

Demonstrate practicality of industrial FBC for high sulfur Illinois coal in an environ- mentally acceptable Banner and appraise performance, relia- bility, and economics. Costs for land are included in boiler capital costs but not in control system costs.

Some bed material is also elutriated from the bed with the combustion gas. The areas of research for each facility are also provided in the table.

Staged-beds and circulating FBC boilers appear to have the greatest potential for reducing NO emissions below this A level. First, long-term testing at conditions producing very low NO emissions, especially substoichiometric firing, has not been conducted. Tests conducted by Grand Forks Energy Technology Center and Morgantown Energy Technology Center on low-rank coals indicate that some lignites and low-sulfur subbituminous coals contain significant quantities of reactive calcium and sodium alkalinity in their ash.