JPH09196333A - Waste pyrolysis drum - Google Patents

Waste pyrolysis drum

Info

Publication number
JPH09196333A
JPH09196333A JP559196A JP559196A JPH09196333A JP H09196333 A JPH09196333 A JP H09196333A JP 559196 A JP559196 A JP 559196A JP 559196 A JP559196 A JP 559196A JP H09196333 A JPH09196333 A JP H09196333A
Authority
JP
Japan
Prior art keywords
gas
waste
pipe
wire
dry distillation
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.)
Granted
Application number
JP559196A
Other languages
Japanese (ja)
Other versions
JP3754478B2 (en
Inventor
Yutaka Okubo
豊 大久保
Takashi Ono
孝 大野
Toshimi Tsukada
俊美 塚田
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP00559196A priority Critical patent/JP3754478B2/en
Publication of JPH09196333A publication Critical patent/JPH09196333A/en
Application granted granted Critical
Publication of JP3754478B2 publication Critical patent/JP3754478B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable adhered substances adhered to the inner surface of a gas pipe for dry distillation gas to be cleaned even during an operation of pyrolysis. SOLUTION: There is provided a waste pyrolysis drum in which some wastes are indirectly heated with heating air, the wastes are thermally decomposed into dry distillation gas G1 and pyrolysis residues, the pyrolysis residues are separated into ignited substances and non-ignited substances, then discharged and concurrently the dry distillation gas G1 is fed out to a burner 11 of a melting furnace 9 through a gas pipe L3, wherein the gas pipe L3 is provided with a cleaning mechanism 60 comprised of a cleaning member 40 for cleaning off the adhered substances such as carbon, tar or the like at the inner surface in such a way that they may be freely inserted thereby and a fixing part 50 of the cleaning member 40.

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、廃棄物の熱分解処
理に係り、特に熱分解ガス(乾留ガス)によりガス配管
内に付着したカーボン等の付着物を清掃するのに好適な
廃棄物熱分解ドラムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a thermal decomposition treatment of waste, and in particular, it is suitable for cleaning a thermal decomposition gas (dry distillation gas) to remove deposits such as carbon deposited in a gas pipe. Regarding the disassembly drum.

【0002】[0002]

【従来の技術】従来より都市ごみ等の一般廃棄物や廃プ
ラスチック等の可燃物を含む産業廃棄物の処理装置の一
つとして、廃棄物を熱分解反応器に入れて低酸素雰囲気
で加熱して熱分解し、乾留ガスと、主として不揮発性成
分よりなる熱分解残留物とを生成し、さらにこの熱分解
残留物を冷却した後に分離装置に導き、この分離装置で
燃焼性成分と、例えば金属や陶器、砂利及びコンクリー
ト片等のがれきよりなる不燃焼性成分とに分離し、燃焼
性成分を粉砕しこの粉砕された燃焼性成分と乾留ガスと
を燃焼器である溶融炉に導き、この溶融炉で燃焼させて
生じた燃焼灰を溶融スラグとなし、この溶融スラグを排
出して冷却固化させるようにした廃棄物処理装置が知ら
れている(例えば、特開平1−49816号参照)。
2. Description of the Related Art Conventionally, as one of apparatuses for treating industrial waste including general waste such as municipal waste and combustible materials such as waste plastic, the waste is put into a pyrolysis reactor and heated in a low oxygen atmosphere. To produce a carbonized gas and a pyrolysis residue mainly composed of non-volatile components. After further cooling the pyrolysis residue, the pyrolysis residue is led to a separator, where the combustible component and, for example, metal And separated into non-combustible components consisting of debris such as porcelain, porcelain, gravel, concrete fragments, etc. There is known a waste treatment apparatus in which combustion ash generated by burning in a furnace is converted into molten slag, and the molten slag is discharged and solidified by cooling (for example, see JP-A-1-49816).

【0003】そして廃棄物熱分解ドラムにおいては、通
常、間接加熱の伝熱面である伝熱管を内装した回転ドラ
ムが用いられているが、廃棄物熱分解ドラムに供給され
た廃棄物を、加熱空気により低酸素雰囲気で300℃〜
600℃、通常は450℃程度で加熱分解し、乾留ガス
と熱分解残留物とを生成し、この乾留ガスと熱分解残留
物とを排出装置において分解し、乾留ガスをガス配管を
経由して溶融炉のバーナへ導出する構成である。
In the waste pyrolysis drum, a rotary drum having a heat transfer tube as a heat transfer surface for indirect heating is usually used. However, the waste supplied to the waste pyrolysis drum is heated. 300 ° C in a low oxygen atmosphere with air
It is decomposed by heating at 600 ° C., usually about 450 ° C. to generate a dry distillation gas and a thermal decomposition residue, and the dry distillation gas and the thermal decomposition residue are decomposed in an exhaust device, and the dry distillation gas is passed through a gas pipe. This is a configuration that leads to the burner of the melting furnace.

【0004】[0004]

【発明が解決しようとする課題】ところで、前記したよ
うな従来の廃棄物熱分解ドラムにあっては、熱分解残留
物の一部、具体的には微細なカーボンや灰分の一部が乾
留ガスに同伴して、ガス配管を経て溶融炉のバーナへ導
かれるため、このうちの一部や乾留ガス中に含まれるタ
ール分等がガス配管中に付着し、乾留ガスの流れに悪影
響を与える恐れがあった。
By the way, in the conventional waste thermal decomposition drum as described above, a part of the thermal decomposition residue, specifically, a part of fine carbon and ash is carbonized gas. It is introduced into the burner of the melting furnace through the gas pipes, and part of this or tar contained in the carbonization gas may adhere to the gas pipes, adversely affecting the flow of carbonization gas. was there.

【0005】本発明の目的は、乾留ガスのガス配管の内
面に付着した付着物を運転中でも清掃することのできる
廃棄物熱分解ドラムを提供することにある。
An object of the present invention is to provide a waste pyrolysis drum capable of cleaning deposits adhering to the inner surface of a gas pipe for dry distillation gas even during operation.

【0006】[0006]

【課題を解決するための手段】前記の目的を達成するた
め、本発明に係る廃棄物熱分解ドラムは、加熱空気によ
り廃棄物を間接加熱し、廃棄物を熱分解して乾留ガスと
熱分解残留物とを生成し、熱分解残留物を燃焼性成分と
不燃焼性成分とに分離して排出するとともに、乾留ガス
をガス配管を経由して溶融炉のバーナへ導出する廃棄物
熱分解ドラムにおいて、ガス配管に、内面の付着物を挿
通自在に清掃する清掃具と、清掃具の取付部とよりなる
清掃機構を具備した構成とする。
In order to achieve the above-mentioned object, the waste pyrolysis drum according to the present invention indirectly heats the waste with heated air to pyrolyze the waste to pyrolyze it with pyrolysis gas. Waste pyrolysis drum that produces a residue, separates the pyrolysis residue into combustible components and non-combustible components and discharges it, and also discharges the dry distillation gas to the burner of the melting furnace via a gas pipe. In the above, the gas pipe is provided with a cleaning mechanism including a cleaning tool for cleaning the adhered matter on the inner surface so as to be inserted therethrough, and a cleaning mechanism.

【0007】そして清掃具は、所定長さを有しかつ先端
がガス配管の内面に接触可能に形成されたワイヤと、ワ
イヤを長さ方向に移動させる駆動部と、駆動部とワイヤ
とを着脱自在に接続する接続部とよりなる構成でもよ
い。
The cleaning tool has a wire having a predetermined length and a tip formed so as to be in contact with the inner surface of the gas pipe, a drive unit for moving the wire in the length direction, and a drive unit and the wire are attached and detached. It may be configured with a connecting portion that is freely connected.

【0008】また取付部は、ガス配管の端部に短管を介
して突設されたフランジと、フランジに取付けられ清掃
具のワイヤを挿通したのち端部をシール可能な取付管
と、取付管に設けられワイヤを挿通可能な少なくとも一
つの弁と、それぞれの弁の間又は一方の弁とフランジと
の間に接続された不活性ガス注入管とよりなる構成でも
よい。
The mounting portion includes a flange projecting from the end of the gas pipe via a short pipe, a mounting pipe mounted on the flange and capable of sealing the end after inserting the wire of the cleaning tool, and the mounting pipe. It may be configured to include at least one valve provided in the above and through which a wire can be inserted, and an inert gas injection pipe connected between the respective valves or between one valve and the flange.

【0009】本実施例によれば、清掃機構がガス配管に
取付けられたため、清掃能率が向上されるとともに、運
転中でも不活性ガスを注入しながら清掃できるため、運
転効率が向上される。
According to the present embodiment, since the cleaning mechanism is attached to the gas pipe, the cleaning efficiency is improved, and the cleaning can be performed while injecting the inert gas even during the operation, so that the operation efficiency is improved.

【0010】[0010]

【発明の実施の形態】本発明の一実施例を図1〜図3を
参照しながら説明する。図1〜図3に示すように、加熱
空気により廃棄物aを間接加熱し、廃棄物aを熱分解し
て乾留ガスG1と熱分解残留物bとを生成し、熱分解残
留物bを燃焼性成分dと不燃焼性成分とに分離して排出
するとともに、乾留ガスG1をガス配管L3を経由して
溶融炉9のバーナ11へ導出する廃棄物熱分解ドラム6
であって、ガス配管L3に、内面のカーボン又はタール
等の付着物を挿通自在に清掃する清掃具40と、清掃具
40の取付部50とよりなる清掃機構60を具備した構
成とする。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described with reference to FIGS. As shown in FIGS. 1 to 3, the waste a is indirectly heated by heated air to thermally decompose the waste a to generate a dry distillation gas G1 and a thermal decomposition residue b, and burn the thermal decomposition residue b. Waste pyrolysis drum 6 that separates and discharges the organic component d and the non-combustible component, and also leads the dry distillation gas G1 to the burner 11 of the melting furnace 9 via the gas pipe L3.
In addition, the gas pipe L3 is provided with a cleaning mechanism 60 including a cleaning tool 40 for cleaning deposits such as carbon or tar on the inner surface so that the gas pipe L3 can be freely inserted, and a mounting portion 50 of the cleaning tool 40.

【0011】そして図4及び図5に示すように、清掃具
40は、所定長さを有しかつ先端がガス配管L3の内面
に接触可能に形成されたワイヤ42と、ワイヤ42を長
さ方向に自在に移動又は回転させる駆動部43と、駆動
部43とワイヤ42とを着脱自在に接続する接続部44
とよりなるものとし、取付部50は、ガス配管L3の端
部に短管51を介して突設されたフランジ52と、フラ
ンジ52に取付けられ清掃具40のワイヤ42を挿通し
たのち端部をシール可能な取付管53と、取付管53に
設けられワイヤ42を挿通可能な少なくとも一つの弁5
4,55と、それぞれの弁54,55の間又は一方の弁
54とフランジ52との間に接続された不活性ガス注入
管56とよりなるものとする。
As shown in FIGS. 4 and 5, the cleaning tool 40 has a wire 42 having a predetermined length and a tip formed in contact with the inner surface of the gas pipe L3, and the wire 42 in the longitudinal direction. Drive unit 43 that moves or rotates freely, and connection unit 44 that detachably connects the drive unit 43 and the wire 42
The mounting portion 50 has a flange 52 projecting from the end portion of the gas pipe L3 via the short pipe 51, and the wire 42 of the cleaning tool 40 attached to the flange 52 and then the end portion. A sealable mounting tube 53 and at least one valve 5 provided on the mounting tube 53 and through which the wire 42 can be inserted.
4, 55, and an inert gas injection pipe 56 connected between the respective valves 54, 55 or between one valve 54 and the flange 52.

【0012】ワイヤ42の先端は図示のように、小枝状
に分岐した形状又は他の内面清掃に適した形状を有する
ものとし、接続部44を介して駆動部43と接続し長さ
方向に前後進及び回転が可能になっている。したがって
接続部44より先端側のワイヤ42を常時、ガス配管L
3内に挿着しておくことが可能であり、その際は弁54
に、弁体にワイヤ42の貫通穴を穿孔したボール弁等を
用い、取付管53の端部にシール構造57を設け、廃棄
物熱分解ドラムの内圧約−10mmAqの負圧に対し、
ガス配管L3内への空気の漏れ込みを防止しなければな
らない。駆動部43は、例えば電動式又は手動式があ
り、ワイヤ42の巻取り部を備え、電動式を用いて信号
により自動的にワイヤ42を駆動するとともに、弁57
を開して不活性ガスを注入することができる。
As shown in the figure, the tip of the wire 42 has a branching shape or another shape suitable for cleaning the inner surface, and is connected to the drive section 43 through a connecting section 44 to move back and forth in the longitudinal direction. It is possible to advance and rotate. Therefore, the wire 42 on the tip side of the connection portion 44 is always connected to the gas pipe L
It is possible to insert it in the inside of the valve 3, and in that case, the valve 54
In addition, a ball valve or the like having a through hole for the wire 42 bored in the valve body is used, and a seal structure 57 is provided at the end of the mounting pipe 53. The internal pressure of the waste pyrolysis drum is about −10 mmAq, and
Air must be prevented from leaking into the gas pipe L3. The drive unit 43 is, for example, of an electric type or a manual type, includes a winding unit for the wire 42, and automatically drives the wire 42 by a signal using the electric type, and the valve 57.
Can be opened and inert gas can be injected.

【0013】運転中にガス配管L3内を清掃する際は、
接続部44及びワイヤ42を介して駆動部43を接続
し、不活性ガス注入管56の弁57を経て窒素ガス等の
不活性ガスを供給し、シール構造58からの空気の漏れ
込みを防止しながら清掃するものとする。除去された付
着物は乾留ガスG1により運ばれ、乾留ガスG1ととも
に溶融炉9のバーナ11で燃焼される。
When cleaning the inside of the gas pipe L3 during operation,
The drive unit 43 is connected through the connection unit 44 and the wire 42, and an inert gas such as nitrogen gas is supplied through the valve 57 of the inert gas injection pipe 56 to prevent air from leaking from the seal structure 58. While cleaning. The removed deposits are carried by the dry distillation gas G1 and burned in the burner 11 of the melting furnace 9 together with the dry distillation gas G1.

【0014】また図5に示すように、弁54,55を設
け、弁54,55間に不活性ガス注入管56を接続する
ことにより、空気の漏れ込みがさらに抑制される。さら
に不活性ガスを注入して弁54を開放した後に、弁55
を開放して取付管53に清掃具40を取付け、前記のよ
うに運転中にガス配管L3の管内を清掃することも可能
である。なお各弁を制御弁で形成することにより、清掃
作業が自動化される。
Further, as shown in FIG. 5, valves 54 and 55 are provided, and an inert gas injection pipe 56 is connected between the valves 54 and 55, whereby air leakage is further suppressed. After further injecting an inert gas and opening the valve 54, the valve 55
It is also possible to open the valve and attach the cleaning tool 40 to the attachment pipe 53 to clean the inside of the gas pipe L3 during operation as described above. The cleaning work is automated by forming each valve with a control valve.

【0015】清掃機構60を運転停止中に取付け、定期
的にガス配管L3の管内を清掃する場合は、弁54の弁
体にワイヤ42の貫通穴を穿孔しておく必要がなく、例
えば仕切弁等を用いてこの仕切弁を全開し、取付管53
に清掃具40を取付けて清掃すればよい。不活性ガスの
注入も不要である。
When the cleaning mechanism 60 is attached while the operation is stopped and the inside of the gas pipe L3 is regularly cleaned, it is not necessary to perforate the through hole of the wire 42 in the valve body of the valve 54. Fully open this sluice valve using
The cleaning tool 40 may be attached to and cleaned. Injecting an inert gas is also unnecessary.

【0016】本実施例によれば、清掃機構により運転中
でもガス配管内の付着物が清掃されるため、定期的に運
転を停止する必要がなくなり、運転効率が向上される。
According to this embodiment, since the cleaning mechanism cleans the deposits in the gas pipe even during operation, it is not necessary to stop the operation periodically, and the operation efficiency is improved.

【0017】廃棄物熱分解ドラム6の詳細を図2により
補足説明する。中空円筒のドラム本体(回転ドラム)7
は、図示しない駆動源により回転される複数のローラ3
1に搭載されて約2rpmで回転し、一方の端面にスク
リューフィーダ32を内管33bに挿着した加熱空気出
口ヘッダ33がシールを介して摺動自在に接続され、ス
クリューフィーダ32の一方の端面に廃棄物aの投入口
4が接続可能になっている。そしてドラム本体7の他方
の端面に加熱空気入口ヘッダ34がシールを介して摺動
可能に接続され、ドラム本体7の内部に、加熱空気出口
側ヘッダ33の管板33aと加熱空気入口側ヘッダ34
の管板34aとに両端を固定された複数の伝熱管8がド
ラム本体7の内周に配設されている。伝熱管8は、耐
熱、耐食材料の例えば、オーステナイト系ステンレス
(SUS316、SUS310SS、SUS321又は
SUS347)、50Cr−50Ni、インコロイ又は
インコネル等で形成されている。加熱空気入口側ヘッダ
34の他端に、加熱空気入口チャンネル35と、排出装
置10とが直結され、排出装置10の上部に乾留ガスG
1の出口10aと、下部に熱分解残留物bを分離した燃
焼性成分d及び不燃焼性成分e1,e2の排出口10b
とが設けられている。そして加熱空気入口側ヘッダ34
の管板34aに穿設された排出穴34bより、排出管3
6が加熱空気入口チャンネル35を挿通して排出装置1
0に連結され、排出管36を通してドラム本体7内の熱
分解残留物b等を排出装置10に排出するようになって
いる。
Details of the waste thermal decomposition drum 6 will be supplementarily described with reference to FIG. Hollow cylinder drum body (rotary drum) 7
Is a plurality of rollers 3 rotated by a drive source (not shown).
1 is rotated at about 2 rpm, and one end surface of the screw feeder 32 is slidably connected to a heated air outlet header 33 having a screw feeder 32 inserted in an inner tube 33b. The input port 4 for the waste a can be connected to. A heated air inlet header 34 is slidably connected to the other end surface of the drum body 7 through a seal, and the tube plate 33a of the heated air outlet side header 33 and the heated air inlet side header 34 are provided inside the drum body 7.
A plurality of heat transfer tubes 8 whose both ends are fixed to the tube sheet 34 a of the drum body 7 are arranged on the inner circumference of the drum body 7. The heat transfer tube 8 is formed of a heat-resistant or corrosion-resistant material such as austenitic stainless steel (SUS316, SUS310SS, SUS321 or SUS347), 50Cr-50Ni, Incoloy or Inconel. The other end of the heated air inlet side header 34 is directly connected to the heated air inlet channel 35 and the discharge device 10.
1 and an outlet 10b for the combustible component d and the non-combustible components e1 and e2 from which the thermal decomposition residue b is separated in the lower part.
Are provided. And the heated air inlet side header 34
Through the discharge hole 34b formed in the tube plate 34a of the discharge pipe 3a.
6 is inserted through the heated air inlet channel 35 and the discharge device 1
The thermal decomposition residue b and the like in the drum body 7 is discharged to the discharge device 10 through the discharge pipe 36.

【0018】ここで図1に示す廃棄物処理装置を詳細に
説明する。受入れヤードAに配置された例えば二軸剪断
式の破砕機1に、都市ごみ等の廃棄物aが第1のコンベ
ア2により供給され、ここで例えば150mm以下に粉
砕される。この粉砕された廃棄物aは第2のコンベア3
により投入口4よりスクリューフィーダ5を経て熱交換
部6aに供給される。この熱交換部6aは回転するドラ
ム本体7の内周壁に沿って複数の伝熱管8を配置して形
成され、図示しないシール機構によりその内部の圧力が
−10mmAq程度の大気圧以下の雰囲気に保持され
る。溶融炉9の後流側に内蔵された高温空気加熱器40
により加熱された加熱空気が、ラインL1より伝熱管8
内に供給され、この加熱空気により廃棄物aは300℃
〜600℃に、通常は450℃程度に間接加熱される。
そのため、この熱交換部6a内に供給された廃棄物aは
熱分解され、乾留ガスG1と、主として不揮発性の熱分
解残留物bとが生成される。
Here, the waste treatment apparatus shown in FIG. 1 will be described in detail. Waste a such as municipal waste is supplied to a crusher 1 of, for example, a twin-screw shear type disposed in a receiving yard A by a first conveyor 2, where it is crushed to, for example, 150 mm or less. This crushed waste a is transferred to the second conveyor 3
Thus, the heat is supplied from the charging port 4 to the heat exchange section 6a through the screw feeder 5. The heat exchanging portion 6a is formed by arranging a plurality of heat transfer tubes 8 along the inner peripheral wall of the rotating drum body 7, and the inside pressure thereof is maintained at an atmospheric pressure of about -10 mmAq or less by an unillustrated sealing mechanism. To be done. High-temperature air heater 40 built in the downstream side of melting furnace 9
The heating air heated by the heat transfer pipe 8
The waste a is heated to 300 ℃ by this heated air.
It is indirectly heated to about 600 ° C., usually about 450 ° C.
Therefore, the waste a supplied into the heat exchange section 6a is thermally decomposed, and the carbonization gas G1 and mainly the non-volatile pyrolysis residue b are generated.

【0019】熱交換部6a内で生成した乾留ガスG1
と、熱分解残留物bは排出装置10で分離され、乾留ガ
スG1はライン(ガス配管)L3を経て溶融炉9のバー
ナ11に供給され、一方、熱分解残留物bは冷却装置1
2で発火防止のため80℃程度にまで冷却され、その
後、例えば篩、磁選式、うず電流式、遠心式又は風力選
別式等の公知の分離装置13に供給され、ここで細粒灰
分を含む燃焼性成分dと、不燃焼性成分である金属成分
e1及び非金属成分e2とに分離される。
Dry distillation gas G1 generated in the heat exchange section 6a
The pyrolysis residue b is separated by the discharge device 10, the dry distillation gas G1 is supplied to the burner 11 of the melting furnace 9 through the line (gas pipe) L3, while the pyrolysis residue b is cooled by the cooling device 1.
It is cooled to about 80 ° C. in order to prevent ignition in 2 and then supplied to a known separation device 13 such as a sieve, a magnetic separation type, an eddy current type, a centrifugal type or a wind type selection type, in which fine ash content is contained. The combustible component d is separated into a metal component e1 and a non-metal component e2 which are non-combustible components.

【0020】そして燃焼性成分dは粉砕機14により例
えば1mm以下に微粉砕され、ラインL4を経て溶融炉
9のバーナ11に供給され、ラインL3より供給された
乾留ガスG1と、送風機15によりラインL5より供給
された燃焼用空気Fとが、1300℃程度の高温域で燃
焼され、このとき発生した燃焼灰は溶融スラグとなって
溶融炉9の内壁に付着流下し、排出口16より水槽17
内に流下し、冷却固化する。この固化したスラグは舗装
材等建材として利用される。
The combustible component d is finely pulverized by the pulverizer 14 to, for example, 1 mm or less, supplied to the burner 11 of the melting furnace 9 through the line L4, and the dry distillation gas G1 supplied from the line L3 and the line by the blower 15. The combustion air F supplied from L5 is combusted in a high temperature region of about 1300 ° C., and the combustion ash generated at this time becomes molten slag that adheres to the inner wall of the melting furnace 9 and flows down, and from the discharge port 16 to the water tank 17
It flows down and cools and solidifies. The solidified slag is used as a building material such as a pavement material.

【0021】溶融炉9で発生した高温排ガスG2は高温
空気加熱器30を経てラインL7より廃熱ボイラ21で
熱回収され、集塵機22a,22bで除塵され、低温の
クリーンな排ガスG3となって煙突23へ大気へ放出さ
れる。このクリーンな排ガスG3の一部はラインL8を
経て冷却装置12へ供給される。廃熱ボイラ21で発生
した蒸気は発電機に連結した蒸気タービン24を回転す
る。
The high-temperature exhaust gas G2 generated in the melting furnace 9 is recovered by the waste heat boiler 21 from the line L7 through the high-temperature air heater 30, and dust is removed by the dust collectors 22a and 22b to become a low-temperature clean exhaust gas G3 and a chimney. 23 is released to the atmosphere. Part of the clean exhaust gas G3 is supplied to the cooling device 12 via the line L8. The steam generated in the waste heat boiler 21 rotates a steam turbine 24 connected to a generator.

【0022】廃棄物が熱交換部に供給されると、廃棄物
は低酸素雰囲気で加熱空気により間接加熱されて熱分解
し、乾留ガスと主として不揮発性成分よりなる熱分解残
留物が生成する。この熱分解工程で廃棄物は常温より3
00℃〜600℃、通常は450℃程度まで加熱空気に
より間接的に加熱昇温される。
When the waste is supplied to the heat exchange section, the waste is indirectly heated by heated air in a low oxygen atmosphere and thermally decomposed to produce a pyrolysis residue consisting of dry distillation gas and mainly non-volatile components. In this thermal decomposition process, the waste is 3
The temperature is indirectly increased by heating with heated air to 00 ° C to 600 ° C, usually about 450 ° C.

【0023】そして、この熱分解反応器で生成した乾留
ガスと熱分解残留物とは、排出装置で分離され、乾留ガ
スは燃焼機である溶融炉へ供給され、一方、熱分解残留
物は冷却されかつ分離装置で燃焼性成分及び細粒の灰分
と、鉄又はアルミニウム等の金属よりなる粗粒不燃焼性
成分とに分離され、その内の燃焼性成分及び細粒の灰分
は溶融炉へ供給され燃焼される。この場合、溶融炉内は
約1300℃程度の高温に保持されているため、細粒の
灰分より生じた燃焼灰は溶融し溶融スラグとなって溶融
炉の内壁に付着流下する。不燃焼性成分は鉄等の金属成
分と陶器等の非金属成分とに分離され、金属成分は再利
用に供せられ、非金属成分は埋め立てに、または必要に
応じて溶融スラグに混合され舗装材等として再利用され
る。
Then, the dry distillation gas produced in the pyrolysis reactor and the pyrolysis residue are separated by an exhaust device, and the dry distillation gas is supplied to a melting furnace which is a combustor, while the pyrolysis residue is cooled. And separated by a separator into combustible components and fine-grained ash, and coarse-grained non-combustible components made of metal such as iron or aluminum, and the combustible components and fine-grained ash contained therein are supplied to the melting furnace. And burned. In this case, since the inside of the melting furnace is maintained at a high temperature of about 1300 ° C., the combustion ash generated from the fine ash is melted to form a molten slag and adheres down to the inner wall of the melting furnace. The non-combustible components are separated into metal components such as iron and non-metal components such as pottery, the metal components are reused, and the non-metal components are mixed in landfill or, if necessary, mixed with molten slag and paved. Reused as materials.

【0024】[0024]

【発明の効果】本発明によれば、乾留ガスのガス配管に
清掃機構を具備したため、運転中でもガス配管内の付着
物が清掃可能となり、清掃作業工数が低減するとともに
稼働率が向上する効果がある。
According to the present invention, since the gas pipe for dry distillation gas is equipped with the cleaning mechanism, it is possible to clean the deposits in the gas pipe even during operation, which reduces the cleaning man-hours and improves the operation rate. is there.

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

【図1】本発明の一実施例の廃棄物熱分解ドラムを備え
た廃棄物処理装置を示す系統図である。
FIG. 1 is a system diagram showing a waste treatment apparatus provided with a waste pyrolysis drum according to one embodiment of the present invention.

【図2】図1の廃棄物熱分解ドラムを示す縦断面図であ
る。
FIG. 2 is a longitudinal sectional view showing the waste pyrolysis drum of FIG. 1;

【図3】図1のガス配管を示す構成図である。3 is a configuration diagram showing a gas pipe of FIG. 1. FIG.

【図4】図3の一部を拡大した断面図である。FIG. 4 is an enlarged sectional view of a part of FIG. 3;

【図5】本発明の他の実施例を示す図である。FIG. 5 is a diagram showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 破砕機 2 第1のコンベア 3 第2のコンベア 4 投入口 5 スクリューフィーダ 6 廃棄物熱分解ドラム 6a 熱交換部 7 ドラム本体 8 伝熱管 9 溶融炉 10 排出装置 11 バーナ 12 冷却装置 13 分離装置 14 粉砕機 15 送風機 16 排出口 17 水槽 18 コンテナ 19 粉砕機 21 廃熱ボイラ 22a,22b 集塵機 23 煙突 24 発電機 40 清掃具 42 ワイヤ 43 駆動部 44 接続部 50 取付部 51 短管 53 取付管 54,55 弁 56 不活性ガス注入管 1 Crusher 2 1st conveyor 3 2nd conveyor 4 Input port 5 Screw feeder 6 Waste pyrolysis drum 6a Heat exchange part 7 Drum body 8 Heat transfer tube 9 Melting furnace 10 Exhaust device 11 Burner 12 Cooling device 13 Separation device 14 Crusher 15 Blower 16 Discharge port 17 Water tank 18 Container 19 Crusher 21 Waste heat boiler 22a, 22b Dust collector 23 Chimney 24 Generator 40 Cleaning tool 42 Wire 43 Drive part 44 Connection part 50 Mounting part 51 Short pipe 53 Mounting pipe 54, 55 Valve 56 Inert gas injection pipe

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 加熱空気により廃棄物を間接加熱し、該
廃棄物を熱分解して乾留ガスと熱分解残留物とを生成
し、該熱分解残留物を燃焼性成分と不燃焼性成分とに分
離して排出するとともに、前記乾留ガスをガス配管を経
由して溶融炉のバーナへ導出する廃棄物熱分解ドラムに
おいて、前記ガス配管に、内面の付着物を挿通自在に清
掃する清掃具と、該清掃具の取付部とよりなる清掃機構
を具備したことを特徴とする廃棄物熱分解ドラム。
1. A waste product is indirectly heated by heated air to thermally decompose the waste product to produce a dry distillation gas and a pyrolysis residue, and the pyrolysis residue is separated into combustible components and non-combustible components. In a waste pyrolysis drum that separates and discharges the dry distillation gas into a burner of a melting furnace through a gas pipe, a cleaning tool that cleans the gas pipe so that deposits on the inner surface can be inserted. A waste pyrolysis drum comprising a cleaning mechanism including an attachment portion of the cleaning tool.
【請求項2】 清掃具は、所定長さを有しかつ先端がガ
ス配管の内面に接触可能に形成されたワイヤと、該ワイ
ヤを長さ方向に移動させる駆動部と、該駆動部と前記ワ
イヤとを着脱自在に接続する接続部とよりなることを特
徴とする請求項1記載の廃棄物熱分解ドラム。
2. The cleaning tool has a wire having a predetermined length and a tip formed so as to be in contact with the inner surface of the gas pipe, a drive section for moving the wire in the length direction, the drive section and the drive section. The waste pyrolysis drum according to claim 1, further comprising a connecting portion for detachably connecting the wire.
【請求項3】 取付部は、ガス配管の端部に短管を介し
て突設されたフランジと、該フランジに取付けられ清掃
具のワイヤを挿通したのち端部をシール可能な取付管
と、該取付管に設けられ前記ワイヤを挿通可能な少なく
とも一つの弁と、それぞれの弁の間又は一方の弁と前記
フランジとの間に接続された不活性ガス注入管とよりな
ることを特徴とする請求項1又は2記載の廃棄物熱分解
ドラム。
3. The mounting part comprises a flange projecting from the end of the gas pipe via a short pipe, and a mounting pipe mounted on the flange and capable of sealing the end after inserting the wire of the cleaning tool. It is characterized in that it comprises at least one valve provided in the attachment pipe through which the wire can be inserted, and an inert gas injection pipe connected between the respective valves or between one valve and the flange. The waste pyrolysis drum according to claim 1 or 2.
JP00559196A 1996-01-17 1996-01-17 Waste pyrolysis drum Expired - Fee Related JP3754478B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP00559196A JP3754478B2 (en) 1996-01-17 1996-01-17 Waste pyrolysis drum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP00559196A JP3754478B2 (en) 1996-01-17 1996-01-17 Waste pyrolysis drum

Publications (2)

Publication Number Publication Date
JPH09196333A true JPH09196333A (en) 1997-07-29
JP3754478B2 JP3754478B2 (en) 2006-03-15

Family

ID=11615489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP00559196A Expired - Fee Related JP3754478B2 (en) 1996-01-17 1996-01-17 Waste pyrolysis drum

Country Status (1)

Country Link
JP (1) JP3754478B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005207279A (en) * 2004-01-21 2005-08-04 Ishikawajima Harima Heavy Ind Co Ltd Impeller blow device for pyrolytic gas fan
JP2007327689A (en) * 2006-06-07 2007-12-20 Chugoku Electric Power Co Inc:The Cleaning device for pressure detecting pipe
KR102613920B1 (en) * 2023-04-13 2023-12-18 유한회사 호원 A continuous pyrolysis system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005207279A (en) * 2004-01-21 2005-08-04 Ishikawajima Harima Heavy Ind Co Ltd Impeller blow device for pyrolytic gas fan
JP4530131B2 (en) * 2004-01-21 2010-08-25 株式会社Ihi Impeller blower for pyrolysis gas fan
JP2007327689A (en) * 2006-06-07 2007-12-20 Chugoku Electric Power Co Inc:The Cleaning device for pressure detecting pipe
KR102613920B1 (en) * 2023-04-13 2023-12-18 유한회사 호원 A continuous pyrolysis system

Also Published As

Publication number Publication date
JP3754478B2 (en) 2006-03-15

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