JP2000274631A - Method and apparatus for waste fluidized bed incineration and air diffusing mechanism used for the apparatus - Google Patents

Abstract

PROBLEM TO BE SOLVED: To improve submersion of waste into a fluidized bed by forming a forcibly circulating flow of fluid medium in the bed. SOLUTION: Air diffusing tubes of a waste fluidized-bed incinerating furnace are divided into a plurality of groups, and airs are supplied from the tubes 24A, 24B, and 24C of the respective groups so that fluidized air amounts are different to form forcibly circulating flows of fluid media in a fluidized bed 22. Then, a waste is introduced into the fluidized bed so that the air amount becomes smallest and the medium become a downflow, and the waste is submerged into the bed 22 by utilizing the circulating flow of the medium.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for efficiently incinerating waste such as municipal solid waste and industrial waste using a fluidized bed furnace, and an air dispersion mechanism used in the apparatus.

[0002]

2. Description of the Related Art FIG. 6 shows an example of a conventional fluidized bed incinerator of a diffuser type. An air supply pipe (not shown) is connected to the diffuser pipe 10 in this furnace, and is configured such that air is uniformly supplied to the entire bottom surface of the fluidized bed 12 to form a fluidized bed. The fluidized medium and the incombustibles are introduced into a classifier 16 such as a vibrating sieve by a discharger 14 such as a screw conveyor, where the incombustibles and the fluidized medium are separated. Circulated.

As an example of a waste fluidized bed combustion technique, Japanese Patent Laid-Open Publication No. 3-267611 discloses an air supply amount adjusting means including an open / close damper connected to each diffuser pipe.
By adjusting the air flow rate and air supply time that are uniformly supplied to the entire surface of the fluidized bed, even if the amount and quality of waste introduced into the furnace fluctuate over time, it will not be affected by the fluctuation. A method is described in which waste can be completely burned at a high burning rate.

[0004]

The above-mentioned JP-A-3-26.
In the technique described in Japanese Patent No. 7611, only the flow rate of the fluidized air uniformly supplied to the entire surface of the fluidized bed and the control of the supply time are controlled via the air diffuser, so that the waste can be sunk into the fluidized bed. Cannot be expected to improve. That is, the waste put into the furnace stays in the vicinity of the fluidized bed interface and does not enter the fluidized bed, so that it is not sufficiently incinerated. In order to cause sneaking, a forced circulation flow of the fluid medium is formed in the fluidized bed, so that the fluid medium at the interface of the refuse bed becomes a downward flow, and the waste flows downward using the circulating flow. It is necessary to put on.

[0005] The present invention has been made in view of the above points,
It is an object of the present invention to form a forced circulation flow of a fluidized medium in a fluidized bed by grouping a plurality of diffuser pipes and not uniformly supplying the amount of fluidizing air from the diffuser pipes of each group, thereby forming a waste stream. It is an object of the present invention to provide a waste fluidized bed incineration method and apparatus capable of improving the infiltration into a fluidized bed. In addition, an object of the present invention is to install a thermometer in the fluidized bed near the upper side of the diffuser pipe of each group, and to set the fluidized bed temperature indication value of each group to a predetermined temperature difference from the diffuser pipe of each group. It is an object of the present invention to provide an air distribution mechanism for controlling the air volume of the air.

[0006]

In order to achieve the above object, a method for incinerating a waste fluidized bed incinerator according to the present invention comprises the steps of dividing a diffuser tube of a waste fluidized bed incinerator into a plurality of groups, The air is supplied so that the amount of fluidized air is different from that of the fluidized medium, and a forced circulating flow of the fluidized medium is formed in the fluidized bed. The waste is put into the fluidized bed and incinerated by utilizing the circulating flow of the fluidized medium (see FIGS. 1 to 4).

In the method of the present invention, the wind box below the air dispersion plate of the waste fluidized bed incinerator is divided into a plurality of air boxes, and air is supplied so that the amount of fluidized air from each of the divided wind boxes is different. To form a forced circulating flow of the fluidized medium in the fluidized bed, put waste into the fluidized bed where the amount of fluidized air is the smallest and the fluidized medium descends, and utilize the circulated flow of the fluidized medium to generate waste. Is infiltrated into a fluidized bed for incineration (see FIG. 5).

In the incineration method using the diffuser type fluidized bed furnace described above (see FIGS. 1 to 4), a thermometer is attached to the fluidized bed near the upper side of the diffuser tube of each group, and the temperature reading of each thermometer is It is preferable to control the air flow rate of the diffuser tube so that a predetermined temperature difference is obtained. In this case, the temperature difference is 100 ° C. or less, preferably 50 to 30 ° C. In this method, the air flow rate of each group of diffuser tubes is controlled so that the temperature of the fluidized bed into which the waste is charged is lower than the temperatures of the other fluidized beds (see FIGS. 1 to 4). Instead of uniformly introducing the amount of fluidized air introduced into the bottom of the fluidized bed through the diffuser pipe over the entire bottom of the fluidized bed, a certain pattern (for example, a central part of the furnace: small, a peripheral part of the furnace: many) is set. Then, a circulating flow of the fluid medium is formed in which the upflow around the furnace and the downflow at the center of the furnace are formed, and the waste is injected into the vicinity of the downflow of the fluid medium and sunk into the fluidized bed.

In the waste fluidized bed incinerator according to the present invention, the diffuser tubes of the waste fluidized bed incinerator are divided into a plurality of groups including at least one diffuser tube, and the air flow control means ( For example, an air supply system equipped with an air flow control damper) is connected, a thermometer is attached to the fluidized bed near the upper side of the diffuser pipe of each group, and the diffuser pipes are set so that the indicated value of each thermometer becomes a predetermined temperature difference. In order to control the air volume, a thermometer and air volume control means corresponding to the same group are connected via an arithmetic unit, and the temperature of the fluidized bed of the group to which waste is charged is set to the temperature of the fluidized bed of another group. It is characterized in that it is controlled so as to be lower than the above, so that the inputted waste is sunk into the fluidized bed by the circulating flow of the fluidized medium (see FIGS. 1 to 4). The number of air diffusers in each group is one or more as described above,
The number of air diffusers in each group does not need to be the same.

In the air distribution mechanism of the present invention, the air diffuser is divided into a plurality of groups including at least one air diffuser, and an air supply system having air volume control means is connected to each of the air diffusers, The fluidized bed thermometers corresponding to the same group and the air volume control means are linked and connected so that each air volume control means is controlled by the detection value of the fluidized bed thermometer corresponding to the same group as the air volume control means. (See FIGS. 1 to 4).

[0011]

DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below, but the present invention is not limited to the following embodiments and can be implemented with appropriate modifications. In the following embodiment, the air diffusers are grouped into three groups A, B, and C as an example, and thermometers 20 _A and 2 _A are arranged in the fluidized bed near the upper side of the air diffusers in each group.
0 _B , 20 _C , and temperature indication values T _A , T _B , T
It is configured to control the air flow rate of the diffuser tube so that _C has a predetermined temperature difference. The pattern of the temperature difference is, for example,
It can be as follows. _{T B <T A ≒ T C} ( see FIG. _{1) T B> T A ≒} T C ( see FIG. _{2) T A> T B>} T C ( see FIG. _{3) T A <T B <} T C ( FIG. 4 reference)

FIG. 1 shows a fluidized bed waste incinerator according to a first embodiment of the present invention. Numeral 22 denotes a fluidized bed of a waste fluidized bed incinerator. The diffuser tubes at the bottom of the fluidized bed 22 are divided into, for example, two groups A, B and C.
The number of air diffusers in each group may be one or three or more, and the number of air diffusers in each group may be different. The diffuser tubes 24 _A , 24 _B , and 24 _C of each group include:
Each air volume control dampers 26 _A, 26 _B, 26 air supply line 28 with a _{C A,} 28 _B, 28 _C are connected. Reference numeral 30 denotes a forced blower. The fluidized layer of the diffusing pipe upper vicinity of each group is provided thermometer 20 _A, 20 _B, 20 _C are indicated value T _A of the thermometer, T _B, the temperature difference T _C is given, for example, 50-30 In order to control the air flow rate of the diffuser tube so that the temperature becomes 20 ° C., the thermometers 20 _A located in the same group,
20 _B, 20 _C and dampers 26 _A, 26 _B, 26 _C and is calculator M _A, M _B, are interlocked connected via the M _C.

In the waste fluidized bed incinerator configured as described above, the central group B into which the waste is charged is provided.
Diffuser tube 24 reduces the fluidizing air quantity from _B, groups of peripheral portions A, many fluidizing air volume from the air diffusing pipe 24 _A, 24 _C and C, and approximately equal quantities supplied. At this time, the fluidized bed temperature T _A of the peripheral portion fluidized bed temperature T _B of the central portion, the predetermined temperature from T _C, for example 50-30 ° C. lower so as to dampers 26 _A, 26 _B, of 26 _C the opening Control. In this way, by controlling the temperature so that T _B <T _A ≒ T _C , a forced circulation flow of the fluid medium in the direction indicated by the arrow in FIG. 1 is formed, and the fluid medium in the central fluid bed is formed. Is generated. Therefore, the waste put into the fluidized bed in the central part immediately enters the fluidized bed by the circulating flow (downflow) of the fluidized medium, and is efficiently incinerated.

FIG. 2 shows a fluidized bed waste incinerator according to a second embodiment of the present invention. In the present embodiment, the temperatures T _A and T _C of the peripheral fluidized bed are equal to the temperature T T of the central fluidized bed.
_B , that is, T _B > T _A ≒ T _C
And the waste is injected into one or both of the peripheral fluidized beds. Other configurations and operations are the same as those in the first embodiment.

FIG. 3 shows a waste fluidized bed incinerator according to a third embodiment of the present invention. This embodiment, the temperature T _A of the grouped fluidized layer, T _B, T _C is such that in turn decreases, i.e. controlled to be _{T A> T B> T C} , the lowest flow temperature is It is configured to put waste into the layer. Other configurations and operations are the same as those in the first embodiment.

FIG. 4 shows a waste fluidized bed incinerator according to a fourth embodiment of the present invention. This embodiment, the temperature T _A of the grouped fluidized layer, T _B, T _C is such that order higher, that is controlled so that _{T A <T B <T C} , the lowest flow temperature is It is configured to put waste into the layer. Other configurations and operations are the same as those in the first embodiment.

The above first to fourth embodiments relate to a diffused tube type fluidized bed furnace, but it is also possible to use an air dispersion plate type fluidized bed furnace. FIG. 5 shows a waste fluidized bed incinerator according to a fifth embodiment of the present invention. The air box below the air distribution plate 32 at the bottom of the fluidized bed 22 is divided into a plurality of parts, and air is supplied so that the amount of fluidized air from each of the divided air boxes 34 _A , 34 _B , and 34 _C is different. A forced circulating flow of the fluidized medium is formed in the bed, and the waste is put into a fluidized bed (fluidized bed with the lowest temperature) in which the amount of fluidized air is the smallest and the fluidized medium flows downward, and the circulated flow of the fluidized medium is changed. Utilization is used to infiltrate waste into the fluidized bed and incinerate efficiently. Other configurations and operations are the same as those in the first to fourth embodiments.

In the first to fifth embodiments of the present invention,
As the fluidized bed 22, a combustion fluidized bed, a partial combustion fluidized bed, or a gasification combustion fluidized bed can be used. In an experiment where municipal solid waste was gasified and incinerated using a gasification furnace and ash melting treatment was performed, the conventional fluidized air was supplied uniformly from a diffuser pipe to the flammable gas (gasified gas) from the gasification furnace. of the oxygen concentration was 2 vol%, combustible gas from the gasification furnace when the temperature difference 40 ° C. with gasifier T _B and T _a structure (≒ T _C) shown in FIG. 1 ( The oxygen concentration in the gasified gas was reduced to 0.5 to 1 vol%.

[0019]

As described above, the present invention has the following effects. (1) Waste introduced into the fluidized bed incinerator efficiently and quickly enters the fluidized bed along the circulating flow (downflow) of the fluidized medium, and reacts efficiently with fluidized air and the like in the fluidized bed for incineration. It is processed. (2) In a fluidized-bed partial combustion furnace or a fluidized-bed gasification furnace, residual oxygen hardly remains in the bed due to the effect of (1). As a result, the combustion reaction in the freeboard portion of the fluidized bed furnace hardly occurs, and the temperature of the freeboard portion is prevented from rising. Therefore, a coaching trouble due to the inorganic chloride is avoided, and stable continuous operation is possible.

[Brief description of the drawings]

FIG. 1 is a schematic sectional view of a main part of a waste fluidized bed incinerator according to a first embodiment of the present invention.

FIG. 2 is a schematic cross-sectional configuration diagram of a main part of a waste fluidized bed incinerator according to a second embodiment of the present invention.

FIG. 3 is a schematic cross-sectional configuration diagram of a main part of a waste fluidized bed incinerator according to a third embodiment of the present invention.

FIG. 4 is a schematic cross-sectional view of a main part of a waste fluidized bed incinerator according to a fourth embodiment of the present invention.

FIG. 5 is a schematic cross-sectional view of a main part of a waste fluidized bed incinerator according to a fifth embodiment of the present invention.

FIG. 6 is an elevational view showing an example of a conventional waste fluidized bed incinerator.

[Explanation of symbols]

REFERENCE SIGNS LIST 10 diffuser tube 12, 22 fluidized bed 14 discharger 16 classifier 18 fluidized medium transfer line 20 _A , 20 _B , 20 _C thermometer 24 _A , 24 _B , 24 _C diffuser tube 26 _A , 26 _B , 26 _{C for} each group Air volume control dampers 28 _A , 28 _B , 28 _C Air supply system 30 Push-in blower 32 Air distribution plate 34 _A , 34 _B , 34 _C split wind box

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[Procedure amendment]

[Submission Date] January 14, 2000 (2000.1.1)
4)

[Procedure amendment 1]

[Document name to be amended] Statement

[Correction target item name] Claims

[Correction method] Change

[Correction contents]

[Claims]

3. The air diffuser of the waste fluidized bed incinerator is divided into a plurality of groups including at least one air diffuser, and an air supply system having air volume control means is connected to the air diffuser of each group. A thermometer is attached to the fluidized bed near the upper part of the diffuser pipe of each group, and the thermometer and air flow corresponding to the same group are used to control the diffuser pipe air volume so that the indicated value of each thermometer becomes a predetermined temperature difference. The control means is connected via an arithmetic unit, and the temperature of the fluidized bed of the group into which the waste is charged is controlled so as to be lower than the temperature of the fluidized bed of the other group, and the input waste is controlled. The fluidized bed waste incinerator characterized in that the wastewater is infiltrated into the fluidized bed without staying near the fluidized bed interface by the circulating flow of the fluidized medium.

4. The air diffuser is divided into a plurality of groups including at least one air diffuser, and an air supply system provided with an air flow controller is connected to the air diffuser of each group, and each air flow controller is provided with an air supply system. A waste characterized in that a fluidized bed thermometer corresponding to the same group and an air flow control means are linked and connected so as to be controlled by a detection value of a fluidized bed thermometer corresponding to the same group as the air flow control means. Air dispersion mechanism used in fluidized bed incinerator.

[Procedure amendment 2]

[Document name to be amended] Statement

[Correction target item name] 0006

[Correction method] Change

[Correction contents]

[0006]

SUMMARY OF THE INVENTION In order to achieve the above object, a waste fluidized bed incineration method according to the present invention divides a diffuser pipe of a waste fluidized bed incinerator into a plurality of groups,
Attach a thermometer to the fluidized bed near the upper side of the diffuser tube, and
Of the fluidized bed into which the waste is
The temperature of the fluidized bed should be lower by a predetermined temperature difference
Supply air so that the amount of fluidized air from the air diffusers in each group is different, and control the air flow in each group.
Then, a forced circulating flow of the fluidized medium is formed in the fluidized bed, the waste is put into the fluidized bed in which the fluidized air amount is the smallest and the fluidized medium is a downward flow, and the circulating flow of the fluidized medium is used.
It is configured such that the waste does not stay near the interface of the fluidized bed and the waste is sunk into the fluidized bed and incinerated (see FIGS. 1 to 4).

[Procedure amendment 3]

[Document name to be amended] Statement

[Correction target item name] 0007

[Correction method] Change

[Correction contents]

Further, the method of the present invention is to divide the waste air distribution plate below the windbox of a fluidized bed incinerator in a plurality, on each windbox
Attach a thermometer to the fluidized bed near the
The reading indicates that the temperature of the fluidized bed into which waste is
Air is supplied so that the amount of fluidized air from each divided wind box is different so as to be lower by a predetermined temperature difference than the temperature of Waste is put into the fluidized bed where the fluidized air amount is the smallest and the fluidized medium flows down, and the circulating flow of the fluidized medium is used.
It is characterized in that waste is sunk into the fluidized bed and incinerated so that the waste does not stay near the fluidized bed interface (see FIG. 5).

[Procedure amendment 4]

[Document name to be amended] Statement

[Correction target item name] 0008

[Correction method] Change

[Correction contents]

[0008] As described above, in the incineration method using a fluidized bed furnace for diffusing tube type (see FIGS. 1 to 4), fitted with a thermometer in a fluidized layer of diffusing pipe upper vicinity of each group, the temperature of the thermometer indicated value that controls the diffusion pipe air flow to a predetermined temperature difference. In this case, the temperature difference is 100 ° C. or less, preferably 50 to 30 ° C. In this method, the air flow rate of each group of diffuser tubes is controlled so that the temperature of the fluidized bed into which the waste is charged is lower than the temperatures of the other fluidized beds (see FIGS. 1 to 4). Instead of uniformly introducing the amount of fluidized air introduced into the bottom of the fluidized bed through the diffuser pipe over the entire bottom of the fluidized bed, a certain pattern (for example, the central part of the furnace:
Small, peripheral part of the furnace: many) to form a circulating fluid medium flow with the ascending flow around the furnace and the descending flow at the center of the furnace. Let go into.

[Procedure amendment 5]

[Document name to be amended] Statement

[Correction target item name] 0009

[Correction method] Change

[Correction contents]

In the waste fluidized bed incinerator according to the present invention, the diffuser tubes of the waste fluidized bed incinerator are divided into a plurality of groups including at least one diffuser tube, and the air flow control means ( For example, an air supply system equipped with an air flow control damper) is connected, a thermometer is attached to the fluidized bed near the upper side of the diffuser pipe of each group, and the diffuser pipes are set so that the indicated value of each thermometer becomes a predetermined temperature difference. In order to control the air volume, a thermometer and air volume control means corresponding to the same group are connected via an arithmetic unit, and the temperature of the fluidized bed of the group to which waste is charged is set to the temperature of the fluidized bed of another group. , So that the input waste does not stay in the vicinity of the interface of the fluidized bed due to the circulating flow of the fluidized medium. <br/> (Fig. 1 See Fig. 4). The number of diffuser tubes in each group is one or more as described above, and the number of diffuser tubes in each group does not need to be the same.

[Procedure amendment 6]

[Document name to be amended] Statement

[Correction target item name] 0019

[Correction method] Change

[Correction contents]

[0019]

As described above, the present invention has the following effects. (1) waste thrown into the fluidized bed incinerator, fluidized bed boundary
The liquid is efficiently and quickly sunk into the fluidized bed along the circulating flow of the fluid medium (downflow) without staying in the vicinity of the surface, and efficiently reacts with fluidized air and the like in the fluidized bed to be incinerated. (2) In a fluidized-bed partial combustion furnace or a fluidized-bed gasification furnace, residual oxygen hardly remains in the bed due to the effect of (1). As a result, the combustion reaction in the freeboard portion of the fluidized bed furnace hardly occurs, and the temperature of the freeboard portion is prevented from rising. Therefore, a coaching trouble due to the inorganic chloride is avoided, and stable continuous operation is possible.

Continued on the front page (72) Inventor Taro Kawamura 1-1, Kawasaki-cho, Akashi-shi, Hyogo Kawasaki Heavy Industries, Ltd. Inside Akashi Factory (72) Inventor Hiroshi Fujiyama 1-3-1, Higashi-Kawasaki-cho, Chuo-ku, Kobe-shi Kawasaki Heavy Industries Kobe Head Office

Claims (6)

[Claims] 1. A diffuser pipe of a waste fluidized bed incinerator is divided into a plurality of groups, and air is supplied so that the amount of fluidized air from the diffuser pipes of each group is different, thereby forcing a fluid medium in the fluidized bed. A circulating flow is formed, and the waste is put into a fluidized bed in which the amount of fluidized air is the smallest and the fluidized medium flows downward, and the waste is sunk into the fluidized bed using the circulating flow of the fluidized medium and incinerated. A fluidized bed waste incineration method characterized by the above-mentioned. 2. A wind box below an air dispersion plate of a waste fluidized bed incinerator is divided into a plurality of air boxes, and air is supplied so that the amount of fluidized air from each of the divided wind boxes is different. A forced circulating flow of the fluidized medium is formed, and the waste is put into the fluidized bed in which the amount of fluidized air is the smallest and the fluidized medium flows downward, and the waste is sunk into the fluidized bed using the circulating flow of the fluidized medium. Waste fluidized bed incineration method characterized by incineration. 3. The waste according to claim 1, wherein a thermometer is attached to the fluidized bed near the upper side of the diffuser pipe of each group, and the air flow rate of the diffuser pipe is controlled such that the temperature indicated value of each thermometer has a predetermined temperature difference. Fluidized bed incineration method. 4. The waste fluidized bed incineration according to claim 3, wherein the air flow rate in each group is controlled so that the temperature of the fluidized bed into which the waste is charged is lower than the temperatures of the other fluidized beds. Method. 5. The air diffuser of the waste fluidized bed incinerator is divided into a plurality of groups including at least one air diffuser, and the air diffuser of each group is connected to an air supply system provided with air volume control means; A thermometer is attached to the fluidized bed near the upper part of the diffuser pipe of each group, and the thermometer and air flow corresponding to the same group are used to control the diffuser pipe air volume so that the indicated value of each thermometer becomes a predetermined temperature difference. The control means is connected via an arithmetic unit, and the temperature of the fluidized bed of the group into which the waste is charged is controlled so as to be lower than the temperature of the fluidized bed of the other group, and the input waste is controlled. The fluidized bed incineration device is characterized in that the wastewater is infiltrated into the fluidized bed by the circulating flow of the fluidized medium. 6. The air diffuser is divided into a plurality of groups including at least one air diffuser, and an air supply system having an air volume controller is connected to the air diffuser of each group, and each air volume controller is provided with an air supply system. A waste characterized in that a fluidized bed thermometer corresponding to the same group and an air flow control means are linked and connected so as to be controlled by a detection value of a fluidized bed thermometer corresponding to the same group as the air flow control means. Air dispersion mechanism used in fluidized bed incinerator.