JPS6234117Y2 - - Google Patents
Info
- Publication number
- JPS6234117Y2 JPS6234117Y2 JP8694082U JP8694082U JPS6234117Y2 JP S6234117 Y2 JPS6234117 Y2 JP S6234117Y2 JP 8694082 U JP8694082 U JP 8694082U JP 8694082 U JP8694082 U JP 8694082U JP S6234117 Y2 JPS6234117 Y2 JP S6234117Y2
- Authority
- JP
- Japan
- Prior art keywords
- extraction pipe
- kiln
- fluidized bed
- furnace
- same diameter
- 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
Links
- 239000000463 material Substances 0.000 claims description 26
- 238000000605 extraction Methods 0.000 claims description 15
- 239000002699 waste material Substances 0.000 claims description 11
- 238000001816 cooling Methods 0.000 claims description 5
- 239000004576 sand Substances 0.000 claims description 5
- 239000011521 glass Substances 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 150000002739 metals Chemical class 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 239000004575 stone Substances 0.000 claims description 3
- 239000000498 cooling water Substances 0.000 description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000012530 fluid Substances 0.000 description 5
- 238000007599 discharging Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 238000012805 post-processing Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Description
【考案の詳細な説明】
本考案は、都市ごみや産業廃棄物など(以下、
廃棄物という)を焼却または熱分解処理する流動
床炉における不燃物排出装置に関するものであ
る。[Detailed explanation of the invention] This invention is designed to collect waste materials such as municipal waste and industrial waste (hereinafter referred to as
This invention relates to a device for discharging incombustibles in a fluidized bed furnace that incinerates or thermally decomposes waste (referred to as waste).
従来から、炉内底部に空気分散板を設け、この
空気分散板の上側に珪砂などの流動媒体により流
動床を形成し、この流動床上に投入された廃棄物
を流動床により混合、撹拌、粉砕して燃焼用空気
と接触させるとともに、廃棄物を蓄熱された流動
床により加熱して焼却または熱分解処理するよう
にした流動床炉が用いられている。この場合、廃
棄物中に含まれる金属類、石、ガラスなどの不燃
物は、炉底に開口した不燃物抜出管から流動媒体
を伴つて炉外へ抜き出され、その後不燃物と流動
媒体とが分離され、流動媒体は再び炉に戻される
という一連の後処理工程を経て、流動床炉の運転
が継続されている。 Conventionally, an air distribution plate is installed at the bottom of the furnace, a fluidized bed is formed above the air distribution plate using a fluidized medium such as silica sand, and the waste placed on the fluidized bed is mixed, stirred, and pulverized by the fluidized bed. A fluidized bed furnace is used in which the waste is brought into contact with combustion air, and the waste is heated in a heat-stored fluidized bed for incineration or thermal decomposition treatment. In this case, noncombustible materials such as metals, stones, and glass contained in the waste are extracted from the furnace together with a fluidized medium through a noncombustible material extraction pipe opened at the bottom of the furnace. The operation of the fluidized bed furnace is continued through a series of post-treatment steps in which the fluidized bed furnace is separated and the fluidized medium is returned to the furnace.
不燃物の形状が小さく、少量の場合は、炉底の
不燃物抜出部の口径も小さくでき、抜出管内に高
圧空気を送入して、不燃物と流動媒体との分離お
よび冷却を計ることも可能であるが、不燃物を含
む廃棄物を、前処理工程で不燃物を分離すること
なく簡単な破砕のみで炉に投入する場合は、抜出
管の口径も大きくなり、前記の高圧空気の送入に
よる不燃物と流動媒体との分離および冷却が困難
となり、不燃物は高温の流動媒体とともに、炉外
に抜き出さざるを得なくなる。 If the shape of the incombustible material is small and the amount is small, the diameter of the incombustible material extraction section at the bottom of the furnace can be made smaller, and high-pressure air is introduced into the extraction pipe to separate the noncombustible material from the fluid medium and cool it. However, if waste containing noncombustibles is fed into the furnace after simple crushing without separating the noncombustibles in the pretreatment process, the diameter of the extraction pipe will also be large, and the high pressure It becomes difficult to separate and cool the non-combustibles and the fluidized medium by introducing air, and the non-combustibles have to be extracted out of the furnace together with the high-temperature fluidized medium.
本考案は上記の諸点に鑑みなされたもので、不
燃物を効果的に抜き出し、かつ随伴する高温の流
動媒体をダクトの飛散や高温をもたらすことな
く、周辺の環境を衛生的に保ちながら充分に冷却
し、前記の後処理工程の円滑な操作を行なうこと
ができる流動床炉における不燃物排出装置を提供
せんとするものである。 The present invention was developed in consideration of the above points, and is capable of effectively extracting incombustible materials and discharging the accompanying high-temperature fluid medium without causing duct scattering or high temperatures, while keeping the surrounding environment sanitary. It is an object of the present invention to provide a device for discharging incombustibles in a fluidized bed furnace, which allows cooling and smooth operation of the above-mentioned post-treatment process.
以下、本考案の構成を図面に示す実施態様に基
づいて説明する。1は流動床炉の炉本体で、この
炉本体1の底部に多数の空気噴出孔2を有する空
気分散板3が設けられ、この空気分散板3の上側
に砂などの流動媒体からなる流動床4が形成さ
れ、この流動床4の上側に燃焼室、いわゆるフリ
ーボード部が形成されている。5は炉底と空気分
散板3との間に形成された風箱である。以上は金
属類、石、ガラスなどの不燃物を含む廃棄物を焼
却する流動床炉であるが、この流動床炉におい
て、炉底および空気分散板に砂などの流動媒体に
よるマテリアルシールが可能な長さの不燃物抜出
管6を接続し、この不燃物抜出管6の下部を、こ
の不燃物抜出管6と同径またはほぼ同径の開口7
を有し、外部とのシール機能と冷却機能を備えた
マントル8に接続する。さらにこのマントル8の
内面に接しながら回転し、不燃物抜出管6の下端
に合致する位置にこの不燃物抜出管6と同径また
はほぼ同径の開口10を有し、かつ冷却機能を備
え、回転数が可変自在のキルン11を設けてい
る。このキルン11は他方に排出口12を有し、
キルン11の静止状態で流動媒体と不燃物が他方
の排出口12から流出しない長さ(キルン直径の
1.5倍以上)を有するように形成されている。1
3は軸受け、14はパツキング、15はキルンの
端部に設けられた冷却器、16は冷却水入口、1
7は冷却水出口、18はキルンの中央部に設けら
れた冷却器、20は冷却水入口、21は冷却水出
口、22は洩れたガスを煙道へ戻す排ガス管であ
る。 Hereinafter, the configuration of the present invention will be explained based on embodiments shown in the drawings. Reference numeral 1 denotes a furnace body of a fluidized bed furnace. At the bottom of the furnace body 1, an air distribution plate 3 having a large number of air ejection holes 2 is provided. On the upper side of this air distribution plate 3, there is a fluidized bed made of a fluidized medium such as sand. 4 is formed, and a combustion chamber, a so-called freeboard section, is formed above this fluidized bed 4. 5 is a wind box formed between the hearth bottom and the air distribution plate 3. The above is a fluidized bed furnace that incinerates waste containing noncombustible materials such as metals, stones, and glass.In this fluidized bed furnace, it is possible to seal the bottom of the furnace and the air distribution plate with a fluid medium such as sand. A length of noncombustible material extraction pipe 6 is connected, and the lower part of this noncombustible material extraction pipe 6 is connected to an opening 7 having the same diameter or approximately the same diameter as this noncombustible material extraction pipe 6.
It is connected to the mantle 8, which has a sealing function with the outside and a cooling function. Furthermore, it rotates while contacting the inner surface of the mantle 8, and has an opening 10 having the same diameter or approximately the same diameter as the incombustible material extraction pipe 6 at a position that matches the lower end of the incombustible material extraction pipe 6, and has a cooling function. A kiln 11 with variable rotation speed is provided. This kiln 11 has an outlet 12 on the other side,
The length (kiln diameter
1.5 times or more). 1
3 is a bearing, 14 is a packing, 15 is a cooler provided at the end of the kiln, 16 is a cooling water inlet, 1
7 is a cooling water outlet, 18 is a cooler provided in the center of the kiln, 20 is a cooling water inlet, 21 is a cooling water outlet, and 22 is an exhaust gas pipe for returning leaked gas to the flue.
上記のように構成された装置において、キルン
11内に落下した不燃物および砂などの流動媒体
は、キルンの回転につれてキルンの他端の排出口
12に達する。この間に不燃物および流動媒体は
キルン外面に噴霧される冷却水によつて冷却され
る。排出口12から排出された不燃物および流動
媒体は、後処理装置へ送られて不燃物と流動媒体
とに分離され、流動媒体は再び炉に戻される。 In the apparatus configured as described above, the incombustible material and the fluid medium such as sand that have fallen into the kiln 11 reach the discharge port 12 at the other end of the kiln as the kiln rotates. During this time, the non-combustible material and the fluid medium are cooled by cooling water sprayed onto the outside of the kiln. The noncombustibles and the fluidized medium discharged from the discharge port 12 are sent to a post-processing device where they are separated into the noncombustibles and the fluidized medium, and the fluidized medium is returned to the furnace again.
本考案の不燃物排出装置は、上記のようにキル
ンの回転数を可変速としているので、炉底からの
抜出量を簡単に調節することができ、かつ不燃物
および流動媒体がキルン内に落下してから排出さ
れるまでの間に冷却されるので、排出時における
ダストの飛散が防止され、周辺の環境を衛生的に
保つことができ、また後処理工程での操作を円滑
に行なうことができるなどの効果を有している。 The incombustible material discharging device of the present invention has a variable kiln rotation speed as described above, so the amount of removal from the bottom of the furnace can be easily adjusted, and the incombustible material and fluidized medium are kept inside the kiln. Since it is cooled from the time it falls until it is discharged, dust is prevented from scattering during discharge, the surrounding environment can be kept sanitary, and operations in the post-processing process can be performed smoothly. It has the following effects:
第1図は本考案の装置の一実施態様を示す断面
説明図、第2図は第1図におけるA−A線拡大断
面図(ただし要部のみを示す)、第3図は第2図
の状態からさらにキルンが回転した状態を示す断
面説明図である。
1……炉本体、2……空気噴出孔、3……空気
分散板、4……流動床、5……風箱、6……不燃
物抜出管、7……開口、8……マントル、10…
…開口、11……キルン、12……排出口、13
……軸受け、14……パツキング、15……冷却
器、16……冷却水入口、17……冷却水出口、
18……冷却器、20……冷却水入口、21……
冷却水出口、22……排ガス管。
Fig. 1 is an explanatory sectional view showing one embodiment of the device of the present invention, Fig. 2 is an enlarged sectional view taken along the line A-A in Fig. 1 (however, only the main parts are shown), and Fig. 3 is the same as Fig. 2. It is a cross-sectional explanatory view showing a state where the kiln is further rotated from the state. DESCRIPTION OF SYMBOLS 1...Furnace body, 2...Air outlet, 3...Air distribution plate, 4...Fluidized bed, 5...Wind box, 6...Incombustible material extraction pipe, 7...Opening, 8...Mantle , 10...
...Opening, 11...Kiln, 12...Discharge port, 13
... bearing, 14 ... packing, 15 ... cooler, 16 ... cooling water inlet, 17 ... cooling water outlet,
18...Cooler, 20...Cooling water inlet, 21...
Cooling water outlet, 22...Exhaust gas pipe.
Claims (1)
を焼却する流動床炉において、流動床炉の炉底に
砂などの流動媒体によるマテリアルシールが可能
な長さの不燃物抜出管を接続し、この不燃物抜出
管の下部を、この不燃物抜出管と同径またはほぼ
同径の開口を有し外部とのシール機能と冷却機能
を備えたマントルに接続し、さらにこのマントル
の内面に接しながら回転し、不燃物抜出管の下端
に合致する位置にこの不燃物抜出管と同径または
ほぼ同径の開口を有し、かつ冷却機能を備え、回
転数が可変自在のキルンを設け、このキルンは他
方に排出口を有し、キルンの静止状態で流動媒体
と不燃物が他方の排出口から流出しない長さを有
するように形成されてなることを特徴とする流動
床炉における不燃物排出装置。 In a fluidized bed furnace that incinerates waste containing noncombustible materials such as metals, stones, and glass, a noncombustible material extraction pipe of a length that allows material sealing with a fluidized medium such as sand is connected to the bottom of the fluidized bed furnace. The lower part of this incombustible material extraction pipe is connected to a mantle that has an opening with the same diameter or approximately the same diameter as this incombustible material extraction pipe and has a sealing function with the outside and a cooling function, and furthermore, It rotates while touching the inner surface, has an opening with the same diameter or almost the same diameter as the noncombustible material extraction pipe at a position that matches the lower end of the noncombustible material extraction pipe, has a cooling function, and has a variable rotation speed. A fluidized bed comprising a kiln, the kiln having a discharge port on the other side, and having a length such that the fluidized medium and the non-combustible material do not flow out from the other discharge port when the kiln is stationary. Non-combustible material discharge device in furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8694082U JPS58189444U (en) | 1982-06-10 | 1982-06-10 | Non-combustible material discharge device in fluidized bed furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8694082U JPS58189444U (en) | 1982-06-10 | 1982-06-10 | Non-combustible material discharge device in fluidized bed furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58189444U JPS58189444U (en) | 1983-12-16 |
JPS6234117Y2 true JPS6234117Y2 (en) | 1987-08-31 |
Family
ID=30095701
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8694082U Granted JPS58189444U (en) | 1982-06-10 | 1982-06-10 | Non-combustible material discharge device in fluidized bed furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58189444U (en) |
-
1982
- 1982-06-10 JP JP8694082U patent/JPS58189444U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS58189444U (en) | 1983-12-16 |
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