Fluidized bed Combustion (FBC) is a method of burning fuel, which is continually fed into a bed of inert material such as sand, silica, alumina or ash and/ or limestone. These materials are kept suspended through the action of the primary air distributor below the combustion floor. The furnace chamber floor is slotted, perforated or fitted with nozzles to uniformly distribute the up flowing air. Turbulence in the chamber is induced by the fluidization of the particles at the airflow rate required for combustion. Improved mixing generates heat at a substantially lower and more uniformly distributed temperature.
When fluidization takes place, the bed of material exhibits the properties of a liquid. As the air velocity increases, added turbulence is achieved and offers several advantages, such as less volatization of alkali compounds, fewer hot spots, and less sensitivity to the quantity and nature of ash in the fuel. As soon as the fuel ignition temperature is achieved, fuel can be fed into or over the bed to achieve the desired operating temperature.
Major categories of Fluidized Bed Boilers include Bubbling-Bed Units, Circulatory-Bed Units and Transport-Reactor Units.
The fundamental distinguishing feature of all FBC units is the velocity of air through the bed. Bubbling-Bed has lower fluidization velocities to prevent solids from carrying over, or elutriating from the bed into the convecture passages. As the air passes through the bed, large particles fall back while the fine particles are either captured by the dust collectors or removed in a baghouse. Circulating-Bed Boilers require partial recirculation or reinjection of solids escaping the bed, to obtain satisfactory performance without substantially increases the size of the combustor. This is achieved by merely increasing and maintaining continuous high air velocities to lift the particles to the combustion chamber where they continue recirculate, thereby increasing the residence time and combustion efficiency avoiding many problems associated with under-bed and over-bed feeding of the fuel.
FBC maybe classified as semi entrained or fully entrained reactors.
A few areas of the boiler system require regular maintenance during scheduled outages to ensure high availability. The maintenance addresses wear caused by the erosive nature of the bed material mainly due to high ash fuel content.
Typical water cooled Holo-Scru Coolers provide proven reliability to drain and cool bed material from the FBC. A typical Holo- Scru Cooler design is shown in Fig. 1. Hot ashes and some inert material such as sand discharges at the bottom of and enter the screw cooler through the flooded inlet. The hot product is then continuously conveyed into the discharge at an angle and dumped into the ash handling system.
Cooling of ash commences as soon as it comes in contact with a water-cooled surface such as the screw and the housing.
Substantial exchange of heat occurs between the hot product and the rotating screw and housing. Efficient cooling of product is accomplished by particle contact with the heat exchange surface, therefore, a relatively long total time of retention of the particle in contact with the rotor surfaces is required. Contact must be continuous and short duration, so that all particles may come in contact with the heat exchange surface area. The ideal condition would be for the product to be in a fluidized state and highly flowable.
Therma-Flite provides a wide range of models and types of Holo-Scru Coolers custom designed and built according to customer provided specifications.
Ash cooling screws are typically designed to handle boiler ash with a discharge temperature of up to 2000 F and cooling it down to 400 F or less so it can enter the ash handling system.
Typical screw design pressures vary from 75 psig to 250 psig while the jacketed U-trough housing runs usually from 15 to 50 psig. Recent developments in the FBC design require a product chamber pressure 300 psig or higher. Therma-Flite has provided FBC manufacturers with jacketed tubular housing equipped with patented Shaft Rider Seals to contain product chamber pressures of 300 psig or higher.
Most processors are built with single pad construction as opposed to a Twin Pad design. Although both constructions are employed to overcome the thermal stresses brought about by the expansion of the screws at elevated temperature.
The advantages of Single Pad over the Twin Pad Design
Perhaps the most area of concern when operating with Ash Screw Coolers is erosion of screw flights and housing interior liners. Many boilers experience unscheduled shutdowns because of wear problems particularly at the inlet zone where the screw flights find itself underneath a column of abrasive material constantly bearing down on the screws.
A new design replacing the hollow flights at the inlet section with solid stainless steel flights with hardface overlay extends the life by three or four times.
By adding rifle bars at the interior lining of the housing minimizes wear as well.
Since nearly any combustible products, including such difficult fuels as oil shales, anthracite wastes, and residual oils, can be effectively burned, Fluidized Bed Combustion has gained worldwide commercial status. Environmentally, its competitiveness with flue gas desulfurization, coal cleaning and advanced technologies such as liquefaction has been established. Besides the front-end technologies of fuel preparation and handling, processing equipment and combustion design, recent improvements in the ash handling technology should also be considered.
|Customer||Product Description||Model No.|
|ABT (UK) Ltd.||Ash Coolers||24-20-5, Style B|
|Air Products||Ash Coolers||12-16-4, Style B|
|Arizona Public Services||Lime Coolers||18-20-4, Style B|
|Alstom Power (ABB)||Ash Coolers||24-20-6, Style B|
|Babcock and Wilcox||Ash Coolers||24-20-5, Style B|
|Beaumont Birch Co.||Ash Coolers||24-10-5, Style B|
|Berlie Technologies||Ash Coolers||24-20-5, Style B|
|Coal Technology Corp.||Char Coolers||36-10-6, Style B|
|City of Los Angeles||Ash Coolers||9-15-3, Style B|
|Denver Equipment||Ash Coolers||7-10-2, Style B|
|Foster Wheeler USA Corp.||Ash Coolers||18-20-4, Style B|
|GDC Engineering||Ash Coolers||12-20-3, Style B|
|GWF Power Systems||Ash Coolers||12-16-5, Style B|
|Heyl and Patterson||Ash Coolers||9-10-3, Style B|
|Kellogg Co.||Pressurized Ash Coolers||36-20-6, Style B|
|Pyropower||Ash Coolers||12-15-3, Style B|
|Reilly Industries||Ash Coolers||20-20-4, Style B|
|Ridge International||Ash Coolers||12-15-3, Style B|
|Rollins Environmental||Ash Coolers||18-22-4, Style B|
|RUST Environmental||Ash Coolers||24-20-5, Style|
|Separation and Recovery Systems||Ash Coolers||12-20-2, Style A|
|Southern Company Services, Inc.||Pressurized Ash Coolers||12-16-3, Style B|
|Tampella Power Co.||Ash Coolers||24-20-5, Style B|
|Westinghouse||Ash Coolers||18-18-4, Style B|
The successful operation of a Hollow Screw Processor for cooling ash in Fluidized Bed Combustion Technologies is dependant upon the ability to overcome the extreme environment at the inlet section of the screw rotor.
Secondary in the design, you must consider the heat transfer capabilities of the processor as a time dependant variable and all factors must be taken in consideration. These factors vary from heat transfer surface area requirements, performance per square foot of area, fouling of the rotor due to ash buildup and fouling of internal heat transfer area due to scale and oxidation.