JP2002061828A - Waste disposal plant - Google Patents

Waste disposal plant

Info

Publication number
JP2002061828A
JP2002061828A JP2000250930A JP2000250930A JP2002061828A JP 2002061828 A JP2002061828 A JP 2002061828A JP 2000250930 A JP2000250930 A JP 2000250930A JP 2000250930 A JP2000250930 A JP 2000250930A JP 2002061828 A JP2002061828 A JP 2002061828A
Authority
JP
Japan
Prior art keywords
pyrolysis gas
pyrolysis
scraping
gas pipeline
adhering
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.)
Pending
Application number
JP2000250930A
Other languages
Japanese (ja)
Inventor
Daisuke Ayukawa
大祐 鮎川
Akihiro Ito
彰啓 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.)
Takuma Co Ltd
Original Assignee
Takuma Co Ltd
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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP2000250930A priority Critical patent/JP2002061828A/en
Publication of JP2002061828A publication Critical patent/JP2002061828A/en
Pending legal-status Critical Current

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  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a waste disposal plant capable of being reduced in installation space as well as in manufacturing cost. SOLUTION: The plant comprises a pyrolysis drum for pyrolyzing waste into a pyrolysis gas and a pyrolysis residue, a pyrolysis gas channel 8 for guiding the pyrolysis gas from the pyrolysis drum to an incineration melting furnace 13 therethrough, and a deposit scraping mechanism 30 for scraping off a deposit on the inner surface of the pyrolysis gas channel 8. The deposit scraping mechanism 30 is composed of a revolving shaft 31 arranged in the pyrolysis gas channel 8 along the axial direction thereof and a scraper 32 arranged on the revolving shaft 31 for scraping off the deposit with the revolution thereof.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、廃棄物を熱分解ガ
スと熱分解残渣とに熱分解する熱分解ドラムを設け、前
記熱分解ドラムからの熱分解ガスを熱分解ガス管路を通
して燃焼溶融炉に流通案内するよう構成し、前記熱分解
ガス管路の内面に付着した付着物を掻取り除去する付着
物掻取り機構を設けてある廃棄物処理プラントに関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention provides a pyrolysis drum which pyrolyzes waste into a pyrolysis gas and a pyrolysis residue, and burns and melts the pyrolysis gas from the pyrolysis drum through a pyrolysis gas pipe. The present invention relates to a waste treatment plant which is configured to be guided in a furnace and provided with a deposit scraping mechanism for scraping and removing deposits attached to the inner surface of the pyrolysis gas pipeline.

【0002】[0002]

【従来の技術】この種の廃棄物処理プラントでは、熱分
解ガス管路の内面にタール・ダスト等が付着・堆積する
と管路が閉塞することから 、特開平9−196336
号公報に開示されているように、熱分解ガス管路を加熱
する加熱装置を設けた技術が提案されている。
2. Description of the Related Art In a waste treatment plant of this type, if tar or dust adheres or accumulates on the inner surface of a pyrolysis gas pipeline, the pipeline is blocked.
As disclosed in Japanese Unexamined Patent Publication (Kokai) No. H11-264, there has been proposed a technology provided with a heating device for heating a pyrolysis gas pipeline.

【0003】しかしながら、この技術によれば、単に熱
分解ガス管路を加熱するだけであったために付着防止効
果があまり高くはなく、そのために、たびたびプラント
を停止させて熱分解ガス管路から付着物を人力により除
去しなければならなかった。
However, according to this technique, the effect of preventing adhesion is not so high because the pyrolysis gas pipeline is simply heated, and therefore, the plant is frequently stopped and the pyrolysis gas pipeline is disconnected. The kimono had to be removed manually.

【0004】そこで、冒頭に記載したように、熱分解ガ
ス管路の内面に付着した付着物を掻取り除去する付着物
掻取り機構を設けた技術が開発されている。
Therefore, as described at the beginning, a technique has been developed in which an adhering substance scraping mechanism for scraping off and removing adhering substances adhering to the inner surface of the pyrolysis gas pipe has been developed.

【0005】従来、前記付着物掻取り機構は、特開平9
−196333号公報に開示されているように、先端が
熱分解ガス管路の内面に接触可能に小枝状に分岐したワ
イヤを熱分解ガス管路に挿入するとともに、基端側以外
のワイヤ部分を熱分解ガス管路内に挿入した押し入れ状
態と、先端側以外のワイヤ部分を熱分解ガス管路外に引
き出した引き出し状態とにワイヤを回転させながら切り
換え可能に構成して、前記先端部で熱分解ガス管路から
付着物を掻取っていた。
Conventionally, the adhering matter scraping mechanism is disclosed in
As disclosed in Japanese Unexamined Patent Publication (Kokai) No. 196333, a wire branched in a twig shape so that the tip can contact the inner surface of the pyrolysis gas pipeline is inserted into the pyrolysis gas pipeline, and a wire portion other than the proximal end side is connected. It is configured to be switchable while rotating the wire between a pushed-in state inserted into the pyrolysis gas pipeline and a drawn-out state in which a wire portion other than the tip side is drawn out of the pyrolysis gas pipeline, and heat is generated at the tip portion. The deposit was scraped from the cracked gas line.

【0006】[0006]

【発明が解決しようとする課題】上記従来の構成によれ
ば、付着物を熱分解ガス管路から除去することができる
ものの、熱分解ガス管路に挿入したワイヤを押し引きす
るようになっていたために、熱分解ガス管路の外側にワ
イヤのストローク分のスペースを設けなければならなら
ず、広い設置スペースが必要になっていた。
According to the above-mentioned conventional structure, the deposit can be removed from the pyrolysis gas pipeline, but the wire inserted into the pyrolysis gas pipeline is pushed and pulled. For this reason, a space corresponding to the stroke of the wire must be provided outside the pyrolysis gas pipeline, and a large installation space is required.

【0007】また、熱分解ガス管路内でワイヤに付着し
たタールが、ワイヤの引き出しで熱分解ガス管路外に出
てくすぶることから、ワイヤへのタールの付着防止対策
や、引き出したワイヤ周辺の換気対策を取らなければな
らず、付着物掻取り機構以外の装置(換気装置等)にコ
ストがかかるという問題があった。
Further, since the tar adhering to the wire in the pyrolysis gas pipe goes out of the pyrolysis gas pipe when the wire is drawn out and is smoldered, it is possible to prevent tar from adhering to the wire and to prevent the tar from being attached to the wire. Therefore, there is a problem in that a device other than the attached matter scraping mechanism (such as a ventilator) is costly.

【0008】本発明は上記実情に鑑みてなされたもの
で、その目的は、設置スペースの縮小化を図ることがで
きるようにするとともに、製作コストを低廉化すること
ができるようにする点にある。
The present invention has been made in view of the above circumstances, and has as its object to reduce the installation space and to reduce the manufacturing cost. .

【0009】[0009]

【課題を解決するための手段】請求項1による発明の構
成・作用・効果は次の通りである。
The constitution, operation and effect of the invention according to claim 1 are as follows.

【0010】[構成]冒頭に記載した廃棄物処理プラン
トにおいて、前記付着物掻取り機構は、前記熱分解ガス
管路内で管路軸芯方向に沿う回転軸に、前記回転軸の回
転に伴って前記付着物を掻取る掻取り体を設けて構成し
てある。
[0010] [Structure] In the waste treatment plant described at the beginning, the adhering matter scraping mechanism includes a rotating shaft that extends in the pyrolysis gas pipeline in a pipe axis direction and rotates with the rotation of the rotating shaft. And a scraping body for scraping the attached matter.

【0011】[作用]熱分解ガス管路内で管路軸芯方向
に沿う回転軸を回転させ、回転軸に設けた掻取り体を回
転させて熱分解ガス管路からタール・ダスト等の付着物
を掻取る。
[Operation] A rotary shaft is rotated in the pyrolysis gas pipeline along the axis of the pipeline, and a scraping member provided on the rotary shaft is rotated to attach tar and dust from the pyrolysis gas pipeline. Scrape the kimono.

【0012】例えば、押し引き式のワイヤの先端部で熱
分解ガス管路内の付着物を掻取る技術では、引き出し状
態のワイヤの収容スペースを設けなければならず、ま
た、ワイヤへのタールの付着防止対策や、引き出したワ
イヤ周辺の換気装置(ワイヤに付着したタールがくすぶ
るため)を設けなければならないという問題があるが、
請求項1の構成によれば、上記のようにして付着物を掻
取るから、上記の収容スペースや換気装置を設ける必要
がない。
For example, in the technique of scraping off the deposits in the pyrolysis gas pipeline at the tip of the push-pull wire, a space for accommodating the drawn wire must be provided, and tar of the wire must be removed. Although there is a problem that it is necessary to provide an anti-adhesion measure and a ventilation device around the drawn wire (since tar adhering to the wire will smolder),
According to the configuration of the first aspect, since the attached matter is scraped as described above, it is not necessary to provide the accommodation space and the ventilation device.

【0013】[効果]従って、設置スペースの縮小化を
図ることができるとともに、製作コストを低廉化するこ
とができた。
[Effect] Therefore, the installation space can be reduced, and the manufacturing cost can be reduced.

【0014】請求項2による発明の構成・作用・効果は
次の通りである。
The configuration, operation and effect of the invention according to claim 2 are as follows.

【0015】[構成]請求項1による発明の構成におい
て、前記熱分解ガス管路に複数の流体吹き込み口を管路
軸芯方向で所定の間隔を置いて形成し、前記熱分解ガス
管路から煤や灰が排出されるように、前記流体吹き込み
口から前記熱分解ガス管路内に流体を吹き込む流体吹き
込み手段を設けてある。
[Configuration] In the configuration according to the first aspect of the present invention, a plurality of fluid injection ports are formed in the pyrolysis gas pipeline at predetermined intervals in the axial direction of the pipeline. Fluid blowing means is provided for blowing fluid from the fluid blowing port into the pyrolysis gas pipe so that soot and ash are discharged.

【0016】[作用]請求項1の構成による作用と同様
の作用を奏することができるのに加え、前記複数の流体
吹き込み口から熱分解ガス管路内に流体を吹き込むこと
で、熱分解ガス管路内の煤や灰を管路外に排出すること
ができ、しかも、熱分解ガス中のタール・ダスト等を前
記流体で熱分解ガス管路外に排出して、タール・ダスト
等が回転軸及び掻取り体に付着するのを防止することが
できる。
[Function] In addition to providing the same function as the function of the first aspect, a fluid can be blown into the pyrolysis gas pipe from the plurality of fluid inlets to form a pyrolysis gas pipe. The soot and ash in the passage can be discharged to the outside of the pipe, and the tar and dust in the pyrolysis gas are discharged to the outside of the pyrolysis gas pipe by the fluid, so that the tar and dust are removed from the rotary shaft. In addition, it can be prevented from adhering to the scraping body.

【0017】前記複数の流体吹き込み口は熱分解ガス管
路に管路軸芯方向で所定の間隔を置いて形成してあるか
ら、例えば、熱分解ガスの流れ方向で上手側の流体吹き
込み口から順に開放して流体を供給していくように制御
することで、全ての流体吹き込み口を同時に開放したと
きのような熱分解ガス管路内及び溶融燃焼炉内の急激な
圧力の変動を防止することができる。
Since the plurality of fluid injection ports are formed in the pyrolysis gas pipe at predetermined intervals in the axial direction of the pipe, for example, the fluid injection ports from the fluid injection port on the upstream side in the flow direction of the pyrolysis gas are used. By controlling the fluid to be opened in order and to supply the fluid, it is possible to prevent a rapid pressure fluctuation in the pyrolysis gas pipeline and the molten combustion furnace as when all the fluid injection ports are simultaneously opened. be able to.

【0018】例えば、回転軸を中空に形成するととも
に、複数の流体吹き込み口を回転軸にその長手方向に所
定の間隔をおいて形成して、回転軸内を通した流体を流
体吹き込み口から熱分解ガス管路内に供給する技術で
は、上記のように熱分解ガス管路内及び溶融燃焼炉内の
圧力が急激に変動するという問題や、回転軸の一端側の
流体吹き込み口ほど流体の圧力が低下して、煤吹き効果
が弱まりやすいという問題があるが、請求項1の構成に
よれば、複数の流体吹き込み口を熱分解ガス管路に形成
してあるから、上記の問題を解消することができる。
For example, the rotary shaft is formed hollow, and a plurality of fluid inlets are formed at predetermined intervals in the longitudinal direction of the rotary shaft so that the fluid passing through the rotary shaft is heated by the fluid inlet through the fluid inlet. In the technique of supplying the gas into the cracked gas pipe, the problem that the pressure in the pyrolyzed gas pipe and the inside of the melting combustion furnace fluctuates rapidly as described above, However, according to the configuration of claim 1, since the plurality of fluid injection ports are formed in the pyrolysis gas pipeline, the above problem is solved. be able to.

【0019】[効果]従って、請求項1の構成による効
果と同様の効果を奏することができるのに加え、付着物
を熱分解ガス管路外により確実に排出することができ
て、より高いクリーニング効果を得ることができ、さら
に燃焼溶融炉内で安定的に燃焼させることができるよう
になった。
[Effect] Therefore, in addition to the same effect as the effect of the first aspect, it is possible to more reliably discharge the deposits to the outside of the pyrolysis gas pipe, thereby achieving higher cleaning. The effect can be obtained, and furthermore, it is possible to stably burn in the combustion melting furnace.

【0020】請求項3による発明の構成・作用・効果は
次の通りである。
The construction, operation and effect of the invention according to claim 3 are as follows.

【0021】[構成]請求項1又は2による発明の構成
において、前記掻取り体をスクリュー羽根で形成してあ
る。
[Structure] In the structure of the invention according to claim 1 or 2, the scraping body is formed by a screw blade.

【0022】[作用]請求項1又は2の構成による作用
と同様の作用を奏することができるのに加え、掻取り体
をスクリュー羽根で形成してあるから掻取り体の構造を
簡素化でき、掻取った付着物をスクリュー羽根で燃焼溶
融炉側に搬送することができる。
[Operation] In addition to providing the same operation as the operation according to the configuration of claim 1 or 2, the structure of the scraping body can be simplified since the scraping body is formed by the screw blades. The scraped deposits can be conveyed to the combustion melting furnace side by the screw blade.

【0023】[効果]従って、請求項1又は2の構成に
よる効果と同様の効果をより得やすくなった。
[Effect] Therefore, the same effect as the effect of the first or second aspect can be more easily obtained.

【0024】請求項4による発明の構成・作用・効果は
次の通りである。
The structure, operation and effect of the invention according to claim 4 are as follows.

【0025】[構成]請求項1,2,3のいずれか一つ
による発明の構成において、前記回転軸の両端部のうち
回転駆動部とは反対側の端部を、前記熱分解ガス管路に
回転自在に支持させてある。
[Configuration] In the configuration of the invention according to any one of claims 1, 2 and 3, of the two ends of the rotary shaft, the end opposite to the rotary drive unit is connected to the pyrolysis gas pipeline. Is rotatably supported.

【0026】[作用]請求項1,2,3のいずれか一つ
の構成による作用と同様の作用を奏することができるの
に加え、回転軸の両端部のうち回転駆動部とは反対側の
端部を、熱分解ガス管路に回転自在に支持させてあるか
ら、回転軸の撓みを抑制できて、回転軸の撓みに起因す
る掻取り体と熱分解ガス管路の内面との摺接による両者
の磨耗を抑制することができる。
[Operation] In addition to the same operation as the operation according to any one of the first, second, and third aspects, the other end of the rotating shaft on the opposite side to the rotation drive unit can be obtained. The part is rotatably supported by the pyrolysis gas pipeline, so that the bending of the rotating shaft can be suppressed, and the scraping member caused by the bending of the rotating shaft and the inner surface of the pyrolysis gas pipeline slide. Wear of both can be suppressed.

【0027】[効果]従って、請求項1,2,3のいず
れか一つの構成による効果と同様の効果を奏することが
できるのに加え、掻取り体及び熱分解ガス管路の耐久性
を向上させることができた。
[Effect] Therefore, in addition to the same effects as the effects of any one of the first, second, and third aspects, the durability of the scraping body and the pyrolysis gas pipe can be improved. I was able to.

【0028】[0028]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0029】図1に廃棄物処理プラントとしての熱分解
ガス化溶融プラントを示してある。この熱分解ガス化溶
融プラントは受入供給設備1・熱分解反応設備2・熱分
解残渣選別設備3・高温燃焼溶融設備4・ボイラ発電設
備5・排ガス処理設備6から成る。次に各設備について
説明する。
FIG. 1 shows a pyrolysis gasification and melting plant as a waste treatment plant. This pyrolysis gasification and melting plant is composed of a receiving and supplying facility 1, a pyrolysis reaction facility 2, a pyrolysis residue sorting facility 3, a high-temperature combustion and melting facility 4, a boiler power generation facility 5, and an exhaust gas treatment facility 6. Next, each facility will be described.

【0030】[受入供給設備1]廃棄物ピット7に貯留
された廃棄物を破砕機(図示せず)で150mm角以下
に破砕し、破砕廃棄物を搬送装置9で熱分解ドラム設備
2に送る。
[Receiving and Supplying Equipment 1] The waste stored in the waste pit 7 is crushed by a crusher (not shown) to 150 mm square or less, and the crushed waste is sent to the pyrolysis drum equipment 2 by the transfer device 9. .

【0031】[熱分解反応設備2]廃棄物ピット7から
の廃棄物をスクリューコンベア10が熱分解ドラム12
内に搬送供給し、熱分解ドラム12により廃棄物を無酸
素あるいは低酸素雰囲気で約450°Cの熱分解ガスと
熱分解残渣とに熱分解する。
[Thermal Decomposition Reaction Facility 2] The screw conveyer 10 removes the waste from the waste pit 7 by the pyrolysis drum 12
The waste is thermally decomposed by the pyrolysis drum 12 into a pyrolysis gas at about 450 ° C. and a pyrolysis residue in an oxygen-free or low-oxygen atmosphere.

【0032】熱分解ガスは熱分解ガスダクト8(熱分解
ガス管路に相当)を通して高温燃焼溶融炉13に送り、
熱分解残渣は熱分解残渣選別設備3に送る。熱分解ガス
ダクト8、及び熱分解ガスダクト8の周りの詳細な構造
については後で説明する。
The pyrolysis gas is sent to a high temperature combustion melting furnace 13 through a pyrolysis gas duct 8 (corresponding to a pyrolysis gas pipeline).
The pyrolysis residue is sent to the pyrolysis residue sorting equipment 3. The pyrolysis gas duct 8 and the detailed structure around the pyrolysis gas duct 8 will be described later.

【0033】[熱分解残渣選別設備3]熱分解反応設備
2からの熱分解残渣を冷却コンベア14で冷却しながら
搬送し、スクリーン15・選別機16(磁選機やアルミ
選別機)により、鉄・アルミ等の有価物を選別回収し、
有価物以外のカーボン残渣を高温燃焼溶融炉13に送
る。
[Pyrolysis Residue Separation Equipment 3] The pyrolysis residue from the pyrolysis reaction equipment 2 is conveyed while being cooled by a cooling conveyor 14, and is subjected to iron / iron separation by a screen 15 and a sorter 16 (a magnetic sorter or an aluminum sorter). Sorting and collecting valuables such as aluminum,
The carbon residue other than valuables is sent to the high temperature combustion melting furnace 13.

【0034】[高温燃焼溶融設備4]熱分解ガス・カー
ボン残渣・集塵ダスト(ボイラや集塵器22からのダス
ト)を高温燃焼溶融炉13に炉頂側から吹き込み、これ
らを旋回燃焼する。灰分は溶融し、炉底から連続排出さ
れる。
[High-Temperature Combustion Melting Facility 4] Pyrolysis gas, carbon residue, and dust (dust from the boiler and dust collector 22) are blown into the high-temperature combustion and melting furnace 13 from the furnace top side, and they are swirled and burned. The ash melts and is continuously discharged from the furnace bottom.

【0035】[ボイラ発電設備5]排ガスはボイラ輻射
ゾーンで冷却し、蒸発管群で均一な温度にした後、約6
00°Cで過熱蒸気管群に送る。ボイラ18で41at
a・400°Cの蒸気を熱回収し、タービン19・発電
機20で電気として回収する。
[Boiler power generation equipment 5] Exhaust gas is cooled in a boiler radiation zone and brought to a uniform temperature in an evaporating tube group.
Send to superheated steam tube group at 00 ° C. 41 at boiler 18
a. Steam at 400 ° C. is recovered by heat and is recovered as electricity by the turbine 19 and the generator 20.

【0036】[排ガス処理設備6]減温塔21・集塵器
22等で処理して煙突25から排気する。
[Exhaust gas treatment equipment 6] The exhaust gas is treated in the cooling tower 21, the dust collector 22, and the like, and exhausted from the chimney 25.

【0037】次に、前記熱分解反応設備2の熱分解ガス
ダクト8、及びこの熱分解ガスダクト8の周りの構造に
ついて説明する。
Next, the pyrolysis gas duct 8 of the pyrolysis reaction facility 2 and the structure around the pyrolysis gas duct 8 will be described.

【0038】図1,図2に示すように、前記熱分解ガス
ダクト8は熱分解ドラム12側の熱分解ガス・熱分解残
渣排出ケース45に連通接続した煙突型ダクト26と、
この煙突型ダクト26に連通接続した水平ダクト27
と、一端側が水平ダクト27に他端側が高温燃焼溶融炉
13の炉頂側に連通接続した垂直ダクト29とから成
り、各ダクトを電気ヒータ等(図示せず)により450
℃〜480℃に加熱して、タール等がダクト内面に付着
するのを防止してある。
As shown in FIGS. 1 and 2, the pyrolysis gas duct 8 includes a chimney type duct 26 connected to a pyrolysis gas / pyrolysis residue discharge case 45 on the pyrolysis drum 12 side,
Horizontal duct 27 connected to this chimney type duct 26
And a vertical duct 29 having one end connected to the horizontal duct 27 and the other end connected to the furnace top side of the high-temperature combustion melting furnace 13, and each duct is connected by an electric heater or the like (not shown).
The temperature is raised to 480 ° C to prevent tar and the like from adhering to the inner surface of the duct.

【0039】前記水平ダクト27に、その内面に付着し
たタール・ダスト等の付着物を掻取り除去する付着物掻
取り機構30を設けてある。
The horizontal duct 27 is provided with a deposit scraping mechanism 30 for scraping and removing deposits such as tar and dust attached to the inner surface thereof.

【0040】この付着物掻取り機構30は、図3
(a),図3(b)にも示すように、付着物掻取り用の
スクリュー羽根32(掻取り体に相当)を複数の支持材
40を介して回転軸31に支持させて成る回転体を、そ
の一端側から水平ダクト27に挿入するとともに、煙突
型ダクト26側で前記水平ダクト27から突出している
回転軸の他端側に、回転駆動部としての電動モータMを
連動連結して構成してある。つまり前記付着物掻取り機
構30は、水平ダクト27内で水平ダクト27の軸芯方
向(管路軸芯方向に相当)に沿う回転軸31に、この回
転軸31の回転に伴って付着物を掻取るスクリュー羽根
32を設けた構造になっている。
This adhering matter scraping mechanism 30 is shown in FIG.
As shown in FIGS. 3 (a) and 3 (b), a rotating body formed by supporting a screw blade 32 (corresponding to a scraping body) for scraping off attached matter on a rotating shaft 31 via a plurality of supporting members 40. Is inserted into the horizontal duct 27 from one end thereof, and an electric motor M as a rotation drive unit is interlockedly connected to the other end of the rotating shaft projecting from the horizontal duct 27 on the chimney type duct 26 side. I have. That is, the adhering matter scraping mechanism 30 applies the adhering matter to the rotating shaft 31 in the horizontal duct 27 along the axis of the horizontal duct 27 (corresponding to the direction of the pipe axis) with the rotation of the rotating shaft 31. The structure is provided with a screw blade 32 for scraping.

【0041】前記スクリュー羽根32はリボン状の耐磨
耗性に優れた金属材から成り(セラミック材で形成して
あってもよい)、水平ダクト27の内面側に寄せて、回
転軸31周りにガス流通空間Sを形成してある。
The screw blade 32 is made of a ribbon-shaped metal material having excellent abrasion resistance (may be formed of a ceramic material). A gas circulation space S is formed.

【0042】前記回転軸31の一端側(電動モーターM
とは反対側の端部)は、水平ダクト27の終端部に、十
字型の支持材33を介して回転自在に支持させてある。
これにより回転軸31の撓みを抑制することができる。
また、回転軸31及びスクリュー羽根32が垂直ダクト
29に干渉することがないことから、垂直ダクト29の
上部に燃焼溶融炉13のバーナを昇降自在に配設してあ
る。
One end of the rotating shaft 31 (the electric motor M
The other end of the horizontal duct 27 is rotatably supported at the end of the horizontal duct 27 via a cross-shaped support member 33.
Thereby, the bending of the rotating shaft 31 can be suppressed.
Further, since the rotating shaft 31 and the screw blade 32 do not interfere with the vertical duct 29, the burner of the combustion melting furnace 13 is disposed above and below the vertical duct 29 so as to be movable up and down.

【0043】上記の構造により、水平ダクト27内で回
転軸31を回転させ、スクリュー羽根32を回転させて
水平ダクト27から付着物を掻取る。そして掻取った付
着物をスクリュー羽根32で垂直ダクト29側に搬送
し、燃焼溶融炉13に供給して燃焼させる。回転軸31
は本プラントを作動させているときは連続して回転させ
る。
With the above structure, the rotating shaft 31 is rotated in the horizontal duct 27 and the screw blades 32 are rotated to scrape off the deposits from the horizontal duct 27. Then, the scraped deposit is conveyed to the vertical duct 29 side by the screw blade 32 and supplied to the combustion melting furnace 13 for combustion. Rotating shaft 31
Is continuously rotated when the plant is operating.

【0044】図2に示すように、前記水平ダクト27に
複数の蒸気吹き込み口34(流体吹き込み口に相当)を
水平ダクト27の軸芯方向で所定の間隔を置いて形成す
るとともに、水平ダクト27内から煤や灰が排出される
ように、蒸気を蒸気吹き込み口34から水平ダクト27
内に定期的に吹き込む蒸気吹き込み手段35(流体吹き
込み手段に相当)を設けてある。
As shown in FIG. 2, a plurality of steam inlets 34 (corresponding to fluid inlets) are formed in the horizontal duct 27 at predetermined intervals in the axial direction of the horizontal duct 27. Steam is injected from the steam inlet 34 into the horizontal duct 27 so that soot and ash are discharged from the inside.
A steam blowing means 35 (corresponding to a fluid blowing means) for periodically blowing into the inside is provided.

【0045】前記蒸気吹き込み手段35は、ボイラ18
の主蒸気管路から分岐した分岐蒸気管36を、複数の電
磁弁Vを介して各蒸気吹き込み口34に連通接続し、電
磁弁Vを開閉切り換え制御する制御装置37を設けて構
成してある。
The steam blowing means 35 is connected to the boiler 18
The branch steam pipe 36 branched from the main steam pipe is connected to each steam blow-in port 34 through a plurality of solenoid valves V, and a control device 37 for controlling the opening and closing of the solenoid valve V is provided. .

【0046】前記制御装置37は、熱分解ガスの流れ方
向で上手側の蒸気吹き込み口34から順に開放して蒸気
を供給していくように各電磁弁Vを制御する。これによ
り、例えば、全ての電磁弁Vを同時に開放したときのよ
うな水平ダクト27内及び高温溶融燃焼炉13内の急激
な圧力の変動を防止することができる。
The control device 37 controls each of the solenoid valves V so as to sequentially open and supply steam from the steam blowing port 34 on the upper side in the flow direction of the pyrolysis gas. Thereby, for example, it is possible to prevent a sudden change in pressure in the horizontal duct 27 and the high-temperature melting and burning furnace 13 such as when all the solenoid valves V are simultaneously opened.

【0047】上記の構造により、複数の蒸気吹き込み口
34から水平ダクト27内に蒸気を吹き込むことで、水
平ダクト27の煤や灰を吹き飛ばすことができ、しか
も、熱分解ガス中のタール・ダストを蒸気で水平ダクト
27外に排出して、タール・ダスト等が回転軸31及び
スクリュー羽根32に付着するのを防止することができ
る。
With the above structure, soot and ash in the horizontal duct 27 can be blown off by blowing steam into the horizontal duct 27 from the plurality of steam blowing ports 34, and furthermore, tar dust in the pyrolysis gas is removed. The steam is discharged to the outside of the horizontal duct 27 to prevent tar and dust from adhering to the rotating shaft 31 and the screw blade 32.

【0048】[別実施形態]上記の実施形態では、前記
回転軸31は本プラントを作動させているときは連続し
て回転させたが、定期的に駆動回転させてもよい。
[Alternative Embodiment] In the above embodiment, the rotary shaft 31 is continuously rotated when the present plant is operating, but may be periodically driven and rotated.

【0049】前記スクリュー羽根32に換えて、別の構
造の掻取り体を回転軸31に設けてあってもよい。
Instead of the screw blade 32, a scraping body having another structure may be provided on the rotating shaft 31.

【0050】前記熱分解ガスダクト8は上記の構造に限
られるものではなく、例えば水平ダクト27に換えて、
高温燃焼溶融炉13側ほど低くなる傾斜ダクトを設けて
あってもよい。
The pyrolysis gas duct 8 is not limited to the above structure. For example, instead of the horizontal duct 27,
An inclined duct that becomes lower toward the high-temperature combustion melting furnace 13 may be provided.

【0051】前記蒸気に換えて不活性ガスを熱分解ガス
ダクト8に供給するよう構成してあってもよい。
In place of the steam, an inert gas may be supplied to the pyrolysis gas duct 8.

【0052】前記回転軸31の回転駆動部は油圧式又は
空気圧式の駆動部で構成してあってもよい。
The rotary drive of the rotary shaft 31 may be constituted by a hydraulic or pneumatic drive.

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

【図1】熱分解ガス化溶融プラントの概略図FIG. 1 is a schematic diagram of a pyrolysis gasification and melting plant.

【図2】付着物掻取り機構を示す縦断正面図FIG. 2 is a longitudinal sectional front view showing an attached matter scraping mechanism.

【図3】回転軸の支持構造を示す図FIG. 3 is a view showing a support structure of a rotating shaft.

【符号の説明】[Explanation of symbols]

8 熱分解ガス管路 12 熱分解ドラム 30 付着物掻取り機構 31 回転軸 32 掻取り体 34 流体吹き込み口 35 流体吹き込み手段 M 回転駆動部 Reference Signs List 8 pyrolysis gas pipeline 12 pyrolysis drum 30 adhering matter scraping mechanism 31 rotating shaft 32 scraping body 34 fluid blowing port 35 fluid blowing means M rotation drive unit

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23G 5/14 ZAB F23G 5/14 ZABF Fターム(参考) 3K061 AA07 AA23 AB02 AB03 AC01 DA01 DA13 DA18 DA19 FA10 FA21 QC06 QC38 RA04 3K078 BA03 BA22 CA02 CA21 CA24 4D004 AA46 CA27 CA29 CB41 CB50──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) F23G 5/14 ZAB F23G 5/14 ZABF F-term (Reference) 3K061 AA07 AA23 AB02 AB03 AC01 DA01 DA13 DA18 DA19 FA10 FA21 QC06 QC38 RA04 3K078 BA03 BA22 CA02 CA21 CA24 4D004 AA46 CA27 CA29 CB41 CB50

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物を熱分解ガスと熱分解残渣とに熱
分解する熱分解ドラムを設け、前記熱分解ドラムからの
熱分解ガスを熱分解ガス管路を通して燃焼溶融炉に流通
案内するよう構成し、前記熱分解ガス管路の内面に付着
した付着物を掻取り除去する付着物掻取り機構を設けて
ある廃棄物処理プラントであって、 前記付着物掻取り機構は、前記熱分解ガス管路内で管路
軸芯方向に沿う回転軸に、前記回転軸の回転に伴って前
記付着物を掻取る掻取り体を設けて構成してある廃棄物
処理プラント。
A pyrolysis drum for pyrolyzing waste into a pyrolysis gas and a pyrolysis residue is provided, and the pyrolysis gas from the pyrolysis drum is guided through a pyrolysis gas line to a combustion melting furnace. A waste treatment plant, comprising: an adhering substance scraping mechanism that scrapes and removes adhering substances adhering to an inner surface of the pyrolysis gas pipeline, wherein the adhering substance scraping mechanism includes the pyrolysis gas. A waste treatment plant comprising a rotary shaft extending in a pipe axis direction in a pipe, and a scraper for scraping off the adhering matter with the rotation of the rotary shaft.
【請求項2】 前記熱分解ガス管路に複数の流体吹き込
み口を管路軸芯方向で所定の間隔を置いて形成し、前記
熱分解ガス管路から煤や灰が排出されるように、前記流
体吹き込み口から前記熱分解ガス管路内に流体を吹き込
む流体吹き込み手段を設けてある請求項1記載の廃棄物
処理プラント。
2. A plurality of fluid injection ports are formed in the pyrolysis gas pipeline at predetermined intervals in the axial direction of the pipeline so that soot and ash are discharged from the pyrolysis gas pipeline. The waste treatment plant according to claim 1, further comprising a fluid blowing unit configured to blow fluid from the fluid blowing port into the pyrolysis gas pipeline.
【請求項3】 前記掻取り体をスクリュー羽根で形成し
てある請求項1又は2記載の廃棄物処理プラント。
3. The waste treatment plant according to claim 1, wherein the scraping body is formed by a screw blade.
【請求項4】 前記回転軸の両端部のうち回転駆動部と
は反対側の端部を、前記熱分解ガス管路に回転自在に支
持させてある請求項1,2,3のいずれか一つに記載の
廃棄物処理プラント。
4. The pyrolysis gas pipe according to claim 1, wherein an end of the rotating shaft opposite to the rotation driving section is rotatably supported by the pyrolysis gas pipeline. Waste treatment plant according to one of the above.
JP2000250930A 2000-08-22 2000-08-22 Waste disposal plant Pending JP2002061828A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000250930A JP2002061828A (en) 2000-08-22 2000-08-22 Waste disposal plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000250930A JP2002061828A (en) 2000-08-22 2000-08-22 Waste disposal plant

Publications (1)

Publication Number Publication Date
JP2002061828A true JP2002061828A (en) 2002-02-28

Family

ID=18740422

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000250930A Pending JP2002061828A (en) 2000-08-22 2000-08-22 Waste disposal plant

Country Status (1)

Country Link
JP (1) JP2002061828A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009133527A (en) * 2007-11-29 2009-06-18 Toshiba Corp Apparatus for converting sludge into fuel
CN108278609A (en) * 2018-02-11 2018-07-13 湖南尚威新能源环保有限公司 A kind of horizontal refuse pyrolysis gasification installation
CN111878842A (en) * 2020-08-07 2020-11-03 东营市正能石油科技有限公司 Crude oil heating device with anti-blocking structure

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009133527A (en) * 2007-11-29 2009-06-18 Toshiba Corp Apparatus for converting sludge into fuel
CN108278609A (en) * 2018-02-11 2018-07-13 湖南尚威新能源环保有限公司 A kind of horizontal refuse pyrolysis gasification installation
CN108278609B (en) * 2018-02-11 2023-12-19 湖南尚威新能源环保有限公司 Horizontal garbage pyrolysis gasification device
CN111878842A (en) * 2020-08-07 2020-11-03 东营市正能石油科技有限公司 Crude oil heating device with anti-blocking structure

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