Furnaces – Refuse incinerator – Refuse suspended in or supported by a fluid medium
Reexamination Certificate
1998-12-21
2002-05-21
Lazarus, Ira S. (Department: 3743)
Furnaces
Refuse incinerator
Refuse suspended in or supported by a fluid medium
C110S188000, C110S204000, C110S203000, C110S248000, C122S00400R, C422S146000, C422S147000, C422S143000
Reexamination Certificate
active
06389995
ABSTRACT:
The present invention refers to a method of combustion of a fuel in a combustion chamber enclosing a fluidized bed, comprising the steps of: supplying an oxygen-containing gas to the bed from beneath; supplying a fuel and an absorbent to the bed; collecting combustion gases formed during the combustion; purifying the combustion gases by separating solid material therefrom; and recirculating the solid material separated to the combustion chamber through a channel. Furthermore, the invention refers to a combustion plant comprising: a combustion chamber, which is provided to enclose a fluidized bed and in which a combustion of a fuel is intended to be performed while forming combustion gases and during the supply of an absorbent; and a purification device for purifying said combustion gases, said purification device comprising a separating member, arranged to separate particulate material from said combustion gases, and a channel, connecting the separating member and the combustion chamber and being arranged to recirculate the material separated to the combustion chamber.
It is known to combust different fuels in a bed of particulate, incombustible material, which bed is supplied with combustion air from beneath through nozzles in such a manner that the bed becomes fluidized. There is a difference between different types of such combustion in a fluidized bed, which operate according to different principles and under different conditions. Firstly, there is a difference between an atmospheric bed and a pressurized bed. In comparison with an atmospheric bed, a pressurized fluidized bed is characterized by a small plant size in relation to the effect produced, by a high efficiency, and in that the combustion occurs under advantageous conditions from an environmental and economical point of view. A pressurized bed may have a larger height than atmospheric bed since one may operate with greater pressure drops. Among the atmospheric beds, so-called circulating beds are frequently used, in which the bed material is permitted to circulate through a separating device in order to be recirculated to the bed. This enables unburnt fuel to be recirculated, which improves the efficiency of the combustion, as well as the absorbent material not used for absorption of contaminants, sulfur, which decreases the discharge from the combustion. However, such circulating beds operate with relatively high fluidizing velocities, in typical cases in the order of 5-12 m/s. Fluidizing velocity is the velocity that the gas would have had if it would have flowed through the combustion chamber without the pressure of particles. This high velocity causes problems with erosion of for instance the steam tube arrangement provided in bed in such a way that the lifetime thereof significantly decreases. Furthermore, one may discern the so-called bubbling beds in which the fluidizing velocity is relatively low, in typical cases between 0.5 and 2 m/s. Such a bed is relatively well defined in a vertical direction and there is formed a space, called a freeboard, in the combustion chamber above the bed. In this freeboard a relatively small amount of dust particles are present in comparison with a circulating bed but there is essentially no pressure drop across the freeboard.
In recent time some have tried to provide a certain circulation in pressurized beds by supplying the combustion cases leaving the combustion chamber to a cyclone for separation of solid material, which is recirculated to the combustion chamber. In order to obtain completely the desired effect concerning the degree of utilization of the absorbent and the combustion efficiency by the recirculation, the solid material should be supplied at the bottom of the fluidized bed. This means that one has to overcome the pressure drop which is present in the bed and in the cyclone, in typical cases about 0.5 bars.
In order to overcome this pressure drop it has been suggested to provide a dosing device, for example of a cell feeding type, at the end of a recirculating pipe provided preferably vertically and connecting the cyclone to a combustion chamber. The dosing device may comprise a rotatable shutter provided on the pipe and having a weight which in normal cases keeps the shutter in a closed position. When the amount of material in the pipe is sufficient the weight thereof will overcome the weight of the shutter which means that the shutter is opened and the material is discharged. Such a device leads to an intermittent recirculation of solid material. However, such devices do not function in the way intended in the environment of a fluidized bed due to the movements occurring in the bed and the forces caused by these movements. Furthermore, such devices are rapidly destroyed due to the aggressive, erosive and corrosive environment.
Another solution is an L-valve located in the bed and having a vertical portion in which a column of material is built up. In order to provide a flow of material through the channel such a device requires that gas is injected in the lower portion of the L-valve and in order to provide stability it is necessary to continuously measure the height of the column of material, which is very difficult, if not impossible, in the actual environment.
SE-B-460 148 suggests another way of overcoming this pressure drop. SE-B-460 148 discloses a combustion plant having a combustion chamber enclosing a pressurized fluidized bed for the combustion of a fuel while forming combustion gases. Furthermore, the plant comprises a purification of said combustion gases in several stages. In the stage particulate material is separated by means of a cyclone from the combustion gases and supplied to a collection chamber beneath the cyclone. Via a horizontal recirculating channel, the collected dust particles are fed back to the combustion chamber in order to improve the use of unburnt fuel and absorbent material. The recirculation is accomplished by means of an air driven ejector blowing the material into the combustion chamber. However, such an air injection is very expensive. The increase in the absorbent utilization and the combustion efficiency is lost for the compressor providing primary air to the ejector. In addition, this method leads to erosion.
It should be noted that the recirculation of solid material separated from the combustion gases means that the recirculated fine part may provide as much as 10-40% of the mass of the bed, which strongly influences the heat transfer coefficient to the tubes located in the bed. The fine part is comprised of particles having a largest diameter of about 300-400 &mgr;m and an average particle diameter of about 50-150 &mgr;m.
U.S. Pat. No. 4,021,184 discloses a combustion plant developed for the combustion of waste material. The plant comprises a combustion chamber for a recirculating fluidized bed. The bed disclosed in this document is not pressurized but the plant operates at atmospheric pressure and is of a diluted type (dilute phase fluidized bed), i.e. the fluidized bed fills up the whole combustion chamber. Such a type of bed means that a very large part of the solid, hot bed material will be transported out from the combustion chamber together with the combustion gases formed during the combustion.
Therefore, it is suggested that cyclones for separating dust particles from these gases are provided at the outlet of the combustion chamber and that the separated, hot dust particles are recirculated to the combustion chamber via conduit pipes connecting the cyclones with the combustion chamber. In such a manner it is possible to recover the heat energy in the dust particles leaving the combustion chamber. Thus, a recirculation may be obtained due to the low pressure drop across the bed, i.e. the whole combustion chamber. In addition, the valve mentioned (trickle valve) in the end of the conduit pipe is probably necessary.
EP-B-176 293 discloses another combustion plant having a combustion chamber which encloses a fluidized bed and in which combustion of a fuel is intended to be performed while forming combustion g
Adams Christopher
Anderson Jim
Andersson Mats
Brännström Roine
Weatherby John
ABB Carbon AB
Ciric Liljana V.
Connolly Bove & Lodge & Hutz LLP
Lazarus Ira S.
LandOfFree
Method of combustion and a combustion plant in which... does not yet have a rating. At this time, there are no reviews or comments for this patent.
If you have personal experience with Method of combustion and a combustion plant in which..., we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and Method of combustion and a combustion plant in which... will most certainly appreciate the feedback.
Profile ID: LFUS-PAI-O-2900210