JP2572398Y2 - Fluidized bed furnace - Google Patents

Fluidized bed furnace

Info

Publication number
JP2572398Y2
JP2572398Y2 JP1993050437U JP5043793U JP2572398Y2 JP 2572398 Y2 JP2572398 Y2 JP 2572398Y2 JP 1993050437 U JP1993050437 U JP 1993050437U JP 5043793 U JP5043793 U JP 5043793U JP 2572398 Y2 JP2572398 Y2 JP 2572398Y2
Authority
JP
Japan
Prior art keywords
air
fluidized bed
tube
pipe
heat transfer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP1993050437U
Other languages
Japanese (ja)
Other versions
JPH0722206U (en
Inventor
善嗣 岡田
征矢 伊藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP1993050437U priority Critical patent/JP2572398Y2/en
Publication of JPH0722206U publication Critical patent/JPH0722206U/en
Application granted granted Critical
Publication of JP2572398Y2 publication Critical patent/JP2572398Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は、ガス分散板及び流動層
をそれぞれ複数段有する流動層炉において、下段流動層
による燃料、廃棄物などの被焼却物の部分燃焼ガス、又
は熱分解排ガスなどの可燃物質を含有するガスを、上段
流動層で燃焼させるのに適するガス分散板を備えた流動
層炉に関する。
BACKGROUND OF THE INVENTION The present invention relates to a fluidized bed furnace having a gas dispersion plate and a fluidized bed in each of a plurality of stages. The present invention relates to a fluidized bed furnace equipped with a gas dispersion plate suitable for burning a gas containing a combustible substance in an upper fluidized bed.

【0002】[0002]

【従来の技術】可燃物質を流動層で燃焼させるために
は、空気を流動層の下部から供給する必要がある。この
場合、流動層温度が、一般的には700〜900℃と高
いので、空気供給管を高温耐食性に優れた材料、例え
ば、ステンレス鋼、耐熱鋼などの高価な材料で製作する
必要があった。このために、例えば、実公平3−249
70号公報に記載されているように、ガス分散板を上下
に複数段設け、複数の流動層が別個に形成されるように
し、2次空気配管を上段側のガス分散板に付設されてい
る水冷管(伝熱管)に並置して設けて、2次空気配管を
水冷管によって冷却でき、高温耐食性の低い材質のもの
を採用できるようにした流動床ボイラが提案されてい
る。
2. Description of the Related Art In order to burn combustible substances in a fluidized bed, it is necessary to supply air from below the fluidized bed. In this case, since the fluidized bed temperature is generally as high as 700 to 900 ° C., the air supply pipe has to be made of a material excellent in high-temperature corrosion resistance, for example, an expensive material such as stainless steel or heat-resistant steel. . For this purpose, for example, Japanese Utility Model 3-249
As described in Japanese Patent Publication No. 70, a plurality of gas dispersion plates are provided vertically, so that a plurality of fluidized beds are formed separately, and a secondary air pipe is attached to the upper gas dispersion plate. A fluidized-bed boiler has been proposed which is provided side by side with a water-cooled tube (heat transfer tube) so that a secondary air pipe can be cooled by the water-cooled tube and can be made of a material having low high-temperature corrosion resistance.

【0003】上記の実公平3−24970号公報記載の
流動床ボイラにおける上段のガス分散板は、図6に示す
ように、多数の水冷管(伝熱管)10とこれらの水冷管
10を気密に接続する鋼板等の板状部材12とからな
り、水冷管10の下部に接するように空気管14を設け
たものである。16は板状部材に設けられたガスノズル
である。
As shown in FIG. 6, an upper gas dispersion plate in a fluidized-bed boiler described in Japanese Utility Model Publication No. 3-24970 discloses a large number of water cooling tubes (heat transfer tubes) 10 and these water cooling tubes 10 are hermetically sealed. An air pipe 14 is provided so as to be in contact with a lower part of the water cooling pipe 10. Reference numeral 16 denotes a gas nozzle provided on the plate member.

【0004】[0004]

【考案が解決しようとする課題】図6に示す構造では、
空気管14と水冷管10とは、A部のみでの線接触でし
かなく、伝熱面積が少ないので、水冷管10での空気管
14の冷却効果が殆ど発揮できないという問題点があ
る。本考案は上記の点に鑑みなされたもので、本考案の
目的は、空気供給管(空気管)、水冷管(伝熱管)及び
板状部材を同一平面状に配置した一体構造とし、水冷管
(伝熱管)と空気供給管(空気管)とを板状部材を介し
て面接触させることにより、伝熱面積を大きくして、
冷管(伝熱管)による空気供給管の冷却効果を十分に発
揮することができ、空気供給管を耐食性の低い安価な材
料で製作できる構造のコンパクトで簡単な構成である
ス分散板を備えた流動層炉を提供することにある。
[Problems to be Solved by the Invention] In the structure shown in FIG.
Since the air pipe 14 and the water cooling pipe 10 are only in line contact only at the portion A and have a small heat transfer area, there is a problem that the cooling effect of the air pipe 14 in the water cooling pipe 10 can hardly be exhibited. The present invention has been made in view of the above points, and an object of the present invention is to provide an air supply pipe (air pipe), a water cooling pipe (heat transfer pipe) and
Water cooling tube with integrated structure with plate members arranged in the same plane
(Heat transfer tube) and air supply tube (air tube) via a plate-like member
By making surface contact, the heat transfer area can be increased and the cooling effect of the air supply tube by the water cooling tube (heat transfer tube) can be sufficiently exhibited, and the air supply tube can be made of an inexpensive material with low corrosion resistance. It is an object of the present invention to provide a fluidized-bed furnace having a gas dispersion plate having a compact and simple structure.

【0005】[0005]

【課題を解決するための手段及び作用】上記の目的を達
成するために、本考案の流動層炉は、ガス分散板を複数
段有し、該ガス分散板上にそれぞれ流動層が形成される
流動層炉において、上段流動層のガス分散板を、伝熱管
と空気管とこれらの管を気密に接続する板状部材とで
空気管の中心軸、伝熱管の中心軸及び板状部材が同一平
面上に配置されるように一体に構成し、空気管の軸方向
の両側が板状部材を介して伝熱管の軸方向の側面と面接
するように空気管と伝熱管とを規則的に配置し、この
板状部材に下方からのガスが通過するガスノズルを一体
に設け、前記空気管に空気を噴出する空気ノズルを設け
たことを特徴としている(図1、図3、図4、図5参
照)。空気ノズルは、上段流動層に向かって空気を噴出
するように(図3参照)、又は下段フリーボードに向か
って空気を噴出するように(図4参照)、あるいは上段
流動層乃び下段フリーボードに向かって空気を噴出する
ように(図5参照)、空気管に設けられる。
In order to achieve the above object, the fluidized bed furnace of the present invention has a plurality of gas dispersion plates, on each of which a fluidized bed is formed. in a fluidized bed furnace, the gas distribution plate of the upper fluidized bed, the heat transfer tube and air tube the tubes with the plate-like member to be connected hermetically,
The center axis of the air tube, the center axis of the heat transfer tube, and the plate
To be arranged on the surface, and to the axial direction of the air pipe .
Sides are in contact with the axial side surface of the heat transfer tube through the plate-shaped member.
The air pipe and the heat transfer pipe are regularly arranged so as to touch, a gas nozzle through which gas from below passes is provided integrally with this plate-shaped member, and an air nozzle for jetting air into the air pipe is provided. (See Figs. 1, 3, 4, and 5)
See) . The air nozzle may blow air toward the upper fluidized bed (see FIG. 3) , or blow air toward the lower freeboard (see FIG. 4) , or the upper fluidized bed and the lower freeboard. The air pipe is provided so as to blow air toward the air pipe (see FIG. 5) .

【0006】上記のように、伝熱管(水冷管)と空気管
(空気供給管)と鋼板等の板状部材とを同一平面上に配
し、伝熱管(水冷管)と空気管(空気供給管)とをこの
板状部材を介して溶接により一体構造とすることによっ
て、空気管の両側は板状部材を介して伝熱管と管の軸方
向の広い面積で接触することになり、空気管は伝熱管
によって十分に冷却されることになる。また、空気管
(空気供給管)と伝熱管(水冷管)とガスノズルとを一
体構造としてガス分散板を構成することにより、構成が
簡単になり、経済的な効果が大きい。なお、空気ノズル
が設けられた空気管の数、ガスノズルの数は、必要に応
じてその比率を変えることができる。例えば、空気管の
数が1に対して、ガスノズルの数を2としたり、空気管
の数が2に対して、ガスノズルの数を1としたりするこ
とができる。また、空気管(空気供給管)の両側が板状
部材を介して伝熱管(水冷管)と管の軸方向の広い面積
で面接触するようにして冷却効果を高めるために、図3
〜図5に示すような、空気管が伝熱管(水冷管)2本毎
に規則的に配置される構成としたり、あるいは、空気管
が伝熱管(水冷管)と交互に規則的に配置される構成、
空気管が伝熱管(水冷管)3本毎に規則的に配置される
構成などとすることができる。
As described above, a heat transfer tube (water cooling tube) and an air tube
(Air supply pipe) and a plate-like member such as a steel plate are placed on the same plane.
And by an integral structure by welding the air pipe and the heat transfer tubes (cooling water pipe) and (air supply pipe) through the <br/> plate-like member, on both sides of the air tubes through the plate-like member Den The heat pipe comes into surface contact with a large area in the axial direction of the pipe, and the air pipe is sufficiently cooled by the heat transfer pipe. Further, by forming the gas distribution plate by integrally forming the air pipe (air supply pipe), the heat transfer pipe (water cooling pipe), and the gas nozzle, the configuration is simplified, and the economic effect is large. The ratio of the number of air pipes and the number of gas nozzles provided with air nozzles can be changed as necessary. For example, the number of gas nozzles can be set to two for the number of air pipes, or the number of gas nozzles can be set to one for two air pipes. Both sides of the air pipe (air supply pipe) are plate-shaped
Heat transfer tube (water-cooled tube) and a large area in the axial direction of the tube through the member
In order to increase the cooling effect by making the surfaces contact with each other, FIG.
-As shown in Fig. 5, the air pipe is every two heat transfer pipes (water cooling pipes)
Or regularly arranged in the air pipe
Are arranged regularly and alternately with heat transfer tubes (water cooling tubes),
Air tubes are regularly arranged every three heat transfer tubes (water cooling tubes)
It can be a configuration or the like.

【0007】[0007]

【実施例】以下、図面を参照して本考案の好適な実施例
を詳細に説明する。ただし、この実施例に記載されてい
る構成部材の材質、形状、その相対配置などは、とくに
特定的な記載がない限りは、本考案の範囲をそれらのみ
に限定する趣旨のものではなく、単なる説明例にすぎな
い。図1は、本考案の流動層炉の一実施例を示し、図2
は、図1における上段のガス分散板まわりを示し、図3
は、図1及び図2におけるガス分散板の拡大断面を示し
ている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below in detail with reference to the drawings. However, the materials, shapes, relative arrangements, and the like of the constituent members described in this embodiment are not intended to limit the scope of the present invention only to them, unless otherwise specified. This is just an example. FIG. 1 shows an embodiment of the fluidized bed furnace of the present invention, and FIG.
FIG. 3 shows the periphery of the upper gas dispersion plate in FIG.
2 shows an enlarged cross section of the gas distribution plate in FIGS. 1 and 2.

【0008】20は本考案の流動層炉で、下段ガス分散
板22及び上段ガス分散板24を有し、これらの分散板
22、24上に、それぞれ下段流動層26、上段流動層
28が形成される。30は風箱、32は1次空気供給管
で風箱30に接続される。34は2次空気供給管で、上
段ガス分散板24の空気管36に接続される。38は下
段フリーボード、40は上段フリーボード、42は2次
空気入口管である。
Reference numeral 20 denotes a fluidized bed furnace according to the present invention, which has a lower gas dispersion plate 22 and an upper gas dispersion plate 24, on which a lower fluidized bed 26 and an upper fluidized bed 28 are formed, respectively. Is done. Reference numeral 30 denotes a wind box, and 32 denotes a primary air supply pipe connected to the wind box 30. A secondary air supply pipe 34 is connected to the air pipe 36 of the upper gas dispersion plate 24. 38 is a lower free board, 40 is an upper free board, and 42 is a secondary air inlet pipe.

【0009】上段ガス分散板24は図2及び図3に示す
ように、伝熱管(水冷管)10と空気管36とこれらの
管を気密に接続する鋼板等の板状部材12とで、空気管
36の横断面からみた中心軸が伝熱管(水冷管)10の
横断面からみた中心軸と板状部材12における同一平面
上に配置されるように一体に構成される。また、図2及
び図3に示すように、空気管36は伝熱管(水冷管)1
0が2本毎に規則的に配置され、空気管36の両側が板
状部材12を介して伝熱管(水冷管)10と管の軸方向
の広い面積で面接触して冷却効果が高くなるように構成
されている。なお、空気管が伝熱管(水冷管)と交互に
規則的に配置される構成や、空気管が伝熱管(水冷管)
3本毎に規則的に配置される構成などとすることも勿論
可能である。板状部材12には、下方からのガスが上方
に通過するガスノズル16が設けられ、前記空気管36
には、上段流動層28に向かって空気を噴出する空気ノ
ズル44が設けられている。46は空気ヘッダ、48は
伝熱管ヘッダである。
[0009] In the upper gas distribution plate 24, as shown in FIGS. 2 and 3, the heat transfer tube (the cooling water pipe) 10 and an air pipe 36 and the plate-like member 12 such as a steel plate that connects the tubes hermetically air tube
The central axis of the heat transfer tube (water cooling tube) 10 as viewed from the cross section of 36 is
The same plane in the plate member 12 as the central axis viewed from the cross section
It is configured integrally so as to be placed on top . In addition, FIG.
As shown in FIG. 3 and FIG. 3, the air pipe 36 is a heat transfer pipe (water cooling pipe) 1.
0 are regularly arranged every two lines, and both sides of the air pipe 36 are
Heat transfer tube (water-cooled tube) 10 and the axial direction of the tube
It is configured to increase the cooling effect by making surface contact with a large area
Have been. In addition, the air tube alternates with the heat transfer tube (water cooling tube).
Regularly arranged structure and air tube is heat transfer tube (water cooling tube)
Of course, it is also possible to adopt a configuration that is arranged regularly every three
It is possible. The plate member 12 is provided with a gas nozzle 16 through which gas from below passes upward,
Is provided with an air nozzle 44 for ejecting air toward the upper fluidized bed 28. 46 is an air header and 48 is a heat transfer tube header.

【0010】図3は、2次空気を噴出する空気ノズル4
4が、空気管36の上部に設けられる場合を示している
が、図4に示すように、2次空気を下段フリーボード3
8へ向かって噴出するように、空気管36に下向きの空
気ノズル50を設けたり、図5に示すように、空気管3
6に上向きの空気ノズル44及び下向きの空気ノズル5
0を設けたりするように構成することもある。なお、図
示していないが、1本の空気管に上向きの空気ノズル及
び下向きの空気ノズルを設けることも可能である。空気
管36の熱は、両側の板状部材12を介して伝熱管(水
冷管)10に伝わり、空気管36は効率よく冷却され
る。
FIG. 3 shows an air nozzle 4 for ejecting secondary air.
4 is provided above the air pipe 36, but as shown in FIG.
The air pipe 36 is provided with a downward air nozzle 50 so as to blow out toward the air pipe 8, or as shown in FIG.
6 has an upward air nozzle 44 and a downward air nozzle 5
In some cases, 0 may be provided. Although not shown, one air pipe may be provided with an upward air nozzle and a downward air nozzle. The heat of the air pipe 36 is transmitted to the heat transfer pipe (water cooling pipe) 10 via the plate members 12 on both sides, and the air pipe 36 is efficiently cooled.

【0011】[0011]

【考案の効果】本考案は上記のように構成されているの
で、つぎのような効果を奏する。 (1) 空気管、伝熱管(水冷管)、板状部材が同一平
面状に配置された一体構造であり、空気管の両側が板状
部材を介して伝熱管(水冷管)と管の軸方向の広い面積
面接触するように空気管と伝熱管(水冷管)とが規則
的に配置され、伝熱面積が大きくなって、空気管は伝熱
管(水冷管)によって十分に冷却されるので、ステンレ
ス鋼、耐熱鋼などの高価な材料を使用する必要がなくな
る。(2) 空気管を水冷管(伝熱管)と同一平面状に配し
て板状部材で一体構造とするので、ガス分散板がコンパ
クトな構成となる。) 空気管と伝熱管(水冷管)とガスノズルとを一
体構造としてガス分散板を構成することができるので、
構成が簡単であり、経済的な効果が大きい。
[Effects of the Invention] The present invention is configured as described above, and has the following effects. (1) Air pipe, heat transfer pipe (water-cooled pipe), and plate-shaped member are the same
The air tube and the heat transfer tube (water-cooled tube) are integrated so that the air tube and the heat transfer tube (water-cooled tube) are in planar contact with the heat transfer tube (water-cooled tube) through a plate-shaped member. ) And rules
Since the heat transfer area is increased and the air transfer pipe is sufficiently cooled by the heat transfer pipe (water cooling pipe), it is not necessary to use expensive materials such as stainless steel and heat-resistant steel. (2) Arrange the air tube on the same plane as the water cooling tube (heat transfer tube).
The gas dispersion plate is
Configuration. ( 3 ) Since the air pipe, the heat transfer pipe (water cooling pipe), and the gas nozzle can be integrally formed to form a gas dispersion plate,
The structure is simple and the economic effect is great.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本考案の流動層炉の一実施例を示す概略構成図
である。
FIG. 1 is a schematic configuration diagram showing one embodiment of a fluidized bed furnace of the present invention.

【図2】図1における上段ガス分散板まわりを示す斜視
図である。
FIG. 2 is a perspective view showing the periphery of an upper gas dispersion plate in FIG.

【図3】図1における上段ガス分散板の拡大断面図であ
る。
FIG. 3 is an enlarged cross-sectional view of an upper gas dispersion plate in FIG.

【図4】本考案における上段ガス分散板の他の例を示す
断面図である。
FIG. 4 is a cross-sectional view showing another example of the upper gas dispersion plate in the present invention.

【図5】本考案における上段ガス分散板のさらに他の例
を示す断面図である。
FIG. 5 is a cross-sectional view illustrating still another example of the upper gas dispersion plate according to the present invention.

【図6】従来の上段ガス分散板の一例を示す断面図であ
る。
FIG. 6 is a sectional view showing an example of a conventional upper gas dispersion plate.

【符号の説明】[Explanation of symbols]

10 伝熱管(水冷管) 12 鋼板などの板状部材 14 空気管 16 ガスノズル 20 流動層炉 22 下段ガス分散板 24 上段ガス分散板 26 下段流動層 28 上段流動層 36 空気管 38 下段フリーボード 44 上向き空気ノズル 50 下向き空気ノズル DESCRIPTION OF SYMBOLS 10 Heat transfer tube (water-cooled tube) 12 Plate-shaped members, such as a steel plate, 14 Air tube 16 Gas nozzle 20 Fluidized bed furnace 22 Lower gas dispersion plate 24 Upper gas dispersion plate 26 Lower fluidized bed 28 Upper fluidized bed 36 Air tube 38 Lower free board 44 Upward Air nozzle 50 Downward air nozzle

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F23G 5/027 F23G 5/30 F23C 11/02──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) F23G 5/027 F23G 5/30 F23C 11/02

Claims (4)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 ガス分散板を複数段有し、該ガス分散板
上にそれぞれ流動層が形成される流動層炉において、 上段流動層のガス分散板を、伝熱管と空気管とこれらの
管を気密に接続する板状部材とで、空気管の中心軸、伝
熱管の中心軸及び板状部材が同一平面上に配置されるよ
うに一体に構成し、空気管の軸方向の両側が板状部材を
介して伝熱管の軸方向の側面と面接触するように空気管
と伝熱管とを規則的に配置し、この板状部材に下方から
のガスが通過するガスノズルを一体に設け、前記空気管
に空気を噴出する空気ノズルを設けたことを特徴とする
流動層炉。
In a fluidized-bed furnace having a plurality of gas dispersion plates and a fluidized bed formed on each of the gas dispersion plates, the gas dispersion plates of the upper fluidized bed are formed by heat transfer tubes, air tubes, and these tubes. in the plate-shaped member for connecting airtightly the central axis of the air tube, Den
The central axis of the heat tube and the plate-like member are arranged on the same plane.
Uni integrally constructed, the air pipe so that the axis direction of both sides of the air tube is in contact axial sides and surface of the heat transfer tubes through the plate-like member
And a heat transfer tube are regularly arranged , a gas nozzle through which gas from below is integrally provided in the plate-shaped member, and an air nozzle for jetting air to the air tube is provided. .
【請求項2】 前記空気管に上段流動層に向かって空気
を噴出する空気ノズルを設けたことを特徴とする請求項
1記載の流動層炉。
2. The fluidized bed furnace according to claim 1, wherein an air nozzle for jetting air toward the upper fluidized bed is provided in the air pipe.
【請求項3】 前記空気管に下段フリーボードに向かっ
て空気を噴出する空気ノズルを設けたことを特徴とする
請求項1記載の流動層炉。
3. The fluidized bed furnace according to claim 1, wherein an air nozzle for jetting air toward the lower free board is provided in the air pipe.
【請求項4】 前記空気管に上段流動層及び下段フリー
ボードに向かって空気を噴出する空気ノズルを設けたこ
とを特徴とする請求項1記載の流動層炉。
4. The fluidized bed furnace according to claim 1, wherein the air pipe is provided with an air nozzle for blowing air toward the upper fluidized bed and the lower freeboard.
JP1993050437U 1993-08-24 1993-08-24 Fluidized bed furnace Expired - Fee Related JP2572398Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1993050437U JP2572398Y2 (en) 1993-08-24 1993-08-24 Fluidized bed furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1993050437U JP2572398Y2 (en) 1993-08-24 1993-08-24 Fluidized bed furnace

Publications (2)

Publication Number Publication Date
JPH0722206U JPH0722206U (en) 1995-04-21
JP2572398Y2 true JP2572398Y2 (en) 1998-05-20

Family

ID=12858845

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1993050437U Expired - Fee Related JP2572398Y2 (en) 1993-08-24 1993-08-24 Fluidized bed furnace

Country Status (1)

Country Link
JP (1) JP2572398Y2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0335929Y2 (en) * 1987-02-26 1991-07-30
JPH0616280Y2 (en) * 1988-07-08 1994-04-27 宇部興産株式会社 Fluidized bed combustion equipment

Also Published As

Publication number Publication date
JPH0722206U (en) 1995-04-21

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