JPH06193842A - Melting incinerator and melting incinerating method - Google Patents

Melting incinerator and melting incinerating method

Info

Publication number
JPH06193842A
JPH06193842A JP4069563A JP6956392A JPH06193842A JP H06193842 A JPH06193842 A JP H06193842A JP 4069563 A JP4069563 A JP 4069563A JP 6956392 A JP6956392 A JP 6956392A JP H06193842 A JPH06193842 A JP H06193842A
Authority
JP
Japan
Prior art keywords
furnace body
flame
drain
air
smoke
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
JP4069563A
Other languages
Japanese (ja)
Other versions
JP2525105B2 (en
Inventor
Tokumitsu Matsumoto
徳光 松元
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP4069563A priority Critical patent/JP2525105B2/en
Publication of JPH06193842A publication Critical patent/JPH06193842A/en
Application granted granted Critical
Publication of JP2525105B2 publication Critical patent/JP2525105B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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

Abstract

PURPOSE:To improve removing efficiency of soot dust in exhaust smoke by feeding the smoke in an incinerator body in zigzag manner along many dust removing baffle plates in a stack for the smoke and injecting atomized water from many fountain units. CONSTITUTION:Many stages of dust removing baffle plates 12 are vertically installed in a stack 11 for exhaust smoke of an incinerator body 10. Many stages of fountain units 13 are vertically installed at a suitable interval in the stack 11. Further, a drain unit 14 for receiving drain flowing down along the plates 12 is arranged. Exhaust smoke in the body 10 is raised in a zigzag manner along the plates 12 in the stack 11, and atomized water is injected from the units 13 on the way of raising. Thus, soot smoke and dust in the exhaust smoke are sucked by atomized water, and recovered as drain to the unit 14. On the other hand, the recovered rain is supplied from a drain tube 15 to a purifying tank 17 to be purified, and purified water is circulated from a feed water tube 15 to the units 13.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、鉄、銅、鉛、亜鉛、ア
ルミニューム等の鉄、非鉄金属の溶解分離、抽出を行う
と共に、発泡スチロール、塩化ビニール、紙、段ボール
等の可燃性または化学性廃棄物を焼却するようにした溶
解焼却炉と溶解焼却方向に関する。
FIELD OF THE INVENTION The present invention relates to the separation and extraction of iron and non-ferrous metals such as iron, copper, lead, zinc and aluminum, and the combustibility or chemical properties of styrofoam, vinyl chloride, paper, cardboard and the like. Smelting incinerator and smelting incineration direction to incinerate radioactive waste.

【0002】[0002]

【従来の技術】溶解焼却炉は、上述のように鉄等の被溶
解物から発泡スチロールのような可燃性または化学性廃
棄物までを同時に処理するため、その排煙用煙突からは
種々の塵埃の含んだ煤煙が排出されることになり、これ
がために炉本体内においては、できるだけ燃焼効率を上
げると共に、炉本体からは可能な限り煤煙の排出されな
い集塵装置を備える必要がある。
2. Description of the Related Art As described above, a melting incinerator simultaneously processes a substance to be melted such as iron and a combustible or chemical waste such as Styrofoam, so that various dusts are emitted from the smoke stack. The soot contained therein will be discharged, and for this reason, it is necessary to increase the combustion efficiency in the furnace body as much as possible and to provide a dust collector that does not emit soot as much as possible from the furnace body.

【0003】従来のこの種溶解焼却炉としては、図3に
示すように、炉本体1の側壁に火炎供給用孔2を設け、
その底部に空気取入孔3を設け、炉本体1に隣接して連
通する排煙管4に濾過式集塵装置5を設け、該濾過式集
塵装置5を介して排煙用煙突6に連通するようになって
いる。なお、溶解焼却炉によって鉄や非鉄金属を溶解抽
出すると共に可燃性廃棄物の焼却する構造については、
周知技術であるので図示は省略する。
As a conventional melting and incinerating furnace of this kind, as shown in FIG. 3, a flame supply hole 2 is provided in a side wall of a furnace body 1,
An air intake hole 3 is provided in the bottom portion thereof, a smoke collecting pipe 4 communicating with the furnace body 1 is provided adjacent to the furnace body 1, and a filter type dust collecting device 5 is provided to the smoke collecting chimney 6 through the filter type dust collecting device 5. It is designed to communicate. Regarding the structure that dissolves and extracts ferrous and non-ferrous metals in a melting incinerator and incinerates combustible waste,
Since this is a well-known technique, illustration is omitted.

【0004】[0004]

【発明が解決しようとする課題】上述のように従来のこ
の種溶解焼却炉は、該炉本体1に隣接して濾過式集塵装
置5を設置するようになっているため、装置全体が大型
になり、それだけ設置面積を多く必要とし、トータルコ
ストが高くなるという難点があった。
As described above, in the conventional melting and incinerating furnace of this kind, since the filter-type dust collecting apparatus 5 is installed adjacent to the furnace body 1, the entire apparatus is large in size. Therefore, there is a problem that the installation cost is increased and the total cost is increased.

【0005】また従来のこの種溶解焼却炉は、上述のよ
うに燃焼効率を上げるために単に火炎供給用孔2より多
くの燃料を供給することのみ配慮していたので、鉄等の
被溶解物や発泡合成樹脂等の可燃性または化学性物質等
の産業廃棄物を溶解焼却炉によって溶解焼却するために
は多くの燃料を必要とし、特に燃焼時に化学性廃棄物か
ら発生するガスの圧縮爆発により炉本体1が破損するな
どの問題があった。
Further, in the conventional melting and incinerating furnace of this kind, in order to improve the combustion efficiency as described above, it is considered only to supply a larger amount of fuel than the flame supply hole 2, so that the material to be melted such as iron is melted. A large amount of fuel is required to smelt and incinerate industrial waste such as flammable or foamed synthetic resin with a smelting incinerator, especially due to compression and explosion of gas generated from chemical waste during combustion. There was a problem that the furnace body 1 was damaged.

【0006】従って本発明は可能な限り上述の集塵装置
を小型し尚かつ集塵効率を向上させると共に、できるだ
け燃焼効率を上げ、且つ化学性廃棄物から発生するガス
による炉本体1内の圧力上昇を防ぎ、安全な溶解焼却炉
とその溶解焼却方向を提案することを目的とする。
Therefore, according to the present invention, the above dust collector is made as small as possible and the dust collection efficiency is improved, the combustion efficiency is increased as much as possible, and the pressure in the furnace body 1 due to the gas generated from the chemical waste is increased. The purpose is to prevent rising and propose a safe smelting incinerator and its smelting incineration direction.

【0007】[0007]

【課題を解決するための手段】上記問題点を解決するた
めに、本発明の請求項1にあっては、実施例に示す参照
符号を付して示すと、炉本体10内の排煙を排出する排
煙用煙突11内に除塵用邪魔板12を上下方向に多数段
に設けると共に、上記煙突11内にその上下方向適当間
隔に圧力水を噴出する噴水装置13を取り付け、且つ上
記邪魔板12に伝って流下する排水を受けるドレン14
を配設し、上記噴水装置13に連通する給水管15と上
記ドレン14に連通する排水管16とを浄化槽17を介
して連通連結してなる構成を採用するものである。
In order to solve the above-mentioned problems, in claim 1 of the present invention, when the reference numerals shown in the embodiment are attached, the exhaust gas in the furnace body 10 A plurality of baffle plates 12 for dust removal are provided in the vertical direction in the exhaust chimney 11 for discharging, a fountain device 13 for ejecting pressure water is vertically installed in the chimney 11 at appropriate vertical intervals, and the baffle plate is Drain 14 that receives the drainage that flows down to 12
And a drainage pipe 16 communicating with the drain 14 and a drainage pipe 16 communicating with the drain 14 are connected via a septic tank 17.

【0008】また請求項2にあっては、炉本体10の周
方向適当間隔に火炎供給用兼空気供給用孔18を設ける
と共に、炉本体10の蓋体19に呼吸用孔20を設けて
なる構成を採用するものである。
According to the second aspect of the present invention, the flame supply and air supply holes 18 are provided at appropriate intervals in the circumferential direction of the furnace body 10, and the breathing holes 20 are provided in the lid 19 of the furnace body 10. The configuration is adopted.

【0009】また請求項3にあっては、前記呼吸用孔2
0は調整手段21によってその開度が調整可能となって
いる請求項2記載の構成を採用するものである。
In the third aspect, the breathing hole 2
No. 0 adopts the configuration according to claim 2 whose opening can be adjusted by the adjusting means 21.

【0010】また請求項4にあっては、炉本体10の周
方向適当間隔に設けられた火炎供給用兼空気供給孔18
から炉本体10内に火炎を噴射させて炉本体10内の被
燃焼物に着火させ、その着火後に火炎から圧縮空気に切
り換えて火炎供給用兼空気供給孔18から圧縮空気を噴
射して炉本体10内に燃焼気流を発生させ、且つ炉本体
10内の圧力を炉本体10に設けた呼吸用孔20によっ
て自調整させるようにしてなる構成を採用するものであ
る。
Further, according to the present invention, the flame supply and air supply holes 18 are provided at appropriate intervals in the circumferential direction of the furnace body 10.
To inject a flame into the furnace body 10 to ignite the burned material in the furnace body 10, and after the ignition, switch the flame to compressed air and inject compressed air from the flame supply / air supply hole 18 A configuration is adopted in which a combustion airflow is generated in the furnace 10, and the pressure in the furnace body 10 is automatically adjusted by a breathing hole 20 provided in the furnace body 10.

【0011】[0011]

【作用】本発明の請求項1によれば、炉本体10内の排
煙が排煙用煙突11を通過する途上で除塵用邪魔板12
に当接することによって蛇行状に上昇し、その蛇行状の
上昇途上で噴水装置13から噴出する圧力水がシャワー
状ないしカーテン状となって煙突11内に均一に分散し
た噴霧水によって排煙の粒子が吸着され、これが除塵用
邪魔板12などをつたって流下する排水となってドレン
14に集められ、これに連通する排水管16から浄化槽
17に煤煙や塵埃の含有した排水が還流され、ここで浄
化槽17の高性能フイルター等で煤煙や塵埃と水分とが
分離され、清澄水となった排水は給水管15によって圧
力水として噴水装置13に再供給されることになる。こ
の噴水装置13は煙突11内を上下に幾重にも設けされ
ているため、煙突11内を蛇行状に上昇する煤煙や塵埃
はその殆どが噴水装置13の噴霧水に接触してその粒子
が捕獲されることになる。
According to the first aspect of the present invention, the dust removing baffle plate 12 is provided while the smoke exhaust in the furnace body 10 passes through the smoke exhaust stack 11.
The pressure water that rises in a meandering shape by coming into contact with the meandering shape, and the pressure water ejected from the fountain device 13 in the meandering ascending shape becomes a shower shape or a curtain shape and is uniformly dispersed in the chimney 11. Is adsorbed, and this is collected as drainage flowing down through the dust removal baffle 12 and the like in the drain 14, and the drainage pipe 16 communicating with this is returned to the septic tank 17 in the drainage containing soot and dust. Soot and dust are separated from water by a high-performance filter or the like in the septic tank 17, and the clarified water is re-supplied to the fountain device 13 as pressurized water by the water supply pipe 15. Since the fountain device 13 is vertically stacked in the chimney 11, most of the soot and dust rising in a meandering manner inside the chimney 11 come into contact with the spray water of the fountain device 13 to capture particles. Will be done.

【0012】また請求項2によれば、炉本体10の周方
向適当間隔に火炎供給用兼空気供給用孔18を設けてな
るため、これより火炎を炉本体10内に噴射させること
によって炉本体10内の産業廃棄物を均一に溶解焼却す
ることができ、且つ周方向適当間隔に設けた火炎供給用
兼空気供給用孔18より圧縮空気を炉本体10内に噴出
することによって燃焼中のガスを炉本体10内に均一に
流通させると共に、酸素の供給により一層の燃焼効率を
上げることができる。
According to the second aspect, since the flame supply and air supply holes 18 are provided at appropriate intervals in the circumferential direction of the furnace main body 10, the flame is injected into the furnace main body 10 from this, and thereby the furnace main body 10 is injected. The industrial waste in 10 can be uniformly melted and incinerated, and the gas being burned by injecting compressed air into the furnace main body 10 through the flame supply and air supply holes 18 provided at appropriate intervals in the circumferential direction. Is uniformly distributed in the furnace body 10, and the combustion efficiency can be further improved by supplying oxygen.

【0013】また炉本体10内の圧力が設定圧力よりも
上昇したときには呼吸用孔20から異常圧力を放出する
ことになり、炉本体10内の圧力が設定圧より低下した
場合には呼吸用孔20から炉本体10内に外気を導入し
て炉本体10内を常に所定を設定圧力に維持することが
できる。
When the pressure in the furnace body 10 rises above the set pressure, an abnormal pressure is released from the breathing hole 20. When the pressure in the furnace body 10 falls below the set pressure, the breathing hole 20 is released. External air can be introduced into the furnace body 10 from 20 to maintain a predetermined set pressure inside the furnace body 10 at all times.

【0014】また請求項3によれば、前記呼吸用孔20
は調整手段21によってその開度が調整可能となってい
るため、炉本体10内の被燃焼物の種類や量あるいは火
力に応じて炉本体10内の設定圧力が変化する場合ある
いは経時的に変化する場合にこれに合わせて呼吸用孔2
0の開度を調整することができる。
According to a third aspect, the breathing hole 20.
Since its opening degree can be adjusted by the adjusting means 21, the set pressure in the furnace body 10 changes depending on the type and amount of burned material in the furnace body 10 or the thermal power, or changes with time. Breathing hole 2 according to this
The opening degree of 0 can be adjusted.

【0015】また請求項4によれば、炉本体10の周方
向適当間隔に設けられた火炎供給用兼空気供給孔19か
ら炉本体10内に火炎を噴射させて炉本体10内の被燃
焼物に着火させ、その着火後に火炎から圧縮空気に切り
換えて火炎供給用兼空気供給孔19から圧縮空気を噴射
して炉本体10内に燃焼気流を発生させることによって
炉本体10内の燃焼効率を向上させることができ、また
炉本体10内の圧力が設定圧力よりも異常に高くなった
場合や反対に低くなった場合には呼吸用孔20が自調整
して炉本体10内の圧力を外部に放出したり、外気を炉
本体10内に吸引して炉本体10内の圧力を一定に保持
し、特に化学性廃棄物から発生するガスによる異常の高
圧現象を防止し、ガスの炉本体10内での異常圧による
爆発の生起を有効に阻止することができる。
According to a fourth aspect of the present invention, the flame-injection / air-supply holes 19 provided at appropriate intervals in the circumferential direction of the furnace body 10 are used to inject flame into the furnace body 10 to burn the burned material in the furnace body 10. After the ignition, the flame is switched to compressed air after the ignition, and the compressed air is injected from the flame supply / air supply hole 19 to generate a combustion air flow in the furnace body 10 to improve the combustion efficiency in the furnace body 10. If the pressure in the furnace body 10 becomes abnormally higher than the set pressure or becomes lower than the set pressure, the breathing hole 20 adjusts itself to bring the pressure in the furnace body 10 to the outside. The pressure inside the furnace body 10 is maintained constant by releasing or sucking the outside air into the furnace body 10 to prevent the abnormal high pressure phenomenon due to the gas generated from the chemical waste in particular. Effective occurrence of explosion due to abnormal pressure at It can be prevented.

【0016】[0016]

【実施例】図1は、本発明の一実施例を示すもので、炉
本体10の側壁にその周方向適当間隔に火炎供給用兼空
気供給用孔18が開設されており、その底部には従来ど
うりに燃焼に必要な空気取入孔22が開設されており、
炉本体10の上部の蓋体19には呼吸用孔20が開設さ
れ、これに呼吸用孔20の開度を調整する調整手段21
が設けられている。この調整手段21は、例えば図示の
ように蓋体19に沿って矢印方向にスライドするスライ
ド板21aに呼吸用孔20に重合可能な孔21bを設け
て呼吸用孔20と孔21bとの重合度を変えることによ
って開度を調整するようにしたものである。呼吸用孔2
0の内径は、実験の結果によれば炉本体10の内径の大
略100分の1が好ましい。これより内径が大きいと火
炎が呼吸用孔20から放出されることになり、これより
内径が小さければ充分な呼吸作用を発揮することができ
ない。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows an embodiment of the present invention, in which side walls of a furnace main body 10 are provided with flame supply / air supply holes 18 at appropriate intervals in the circumferential direction thereof, and at the bottom thereof. Conventionally, the air intake hole 22 required for combustion is opened,
A breathing hole 20 is opened in the lid 19 on the upper part of the furnace body 10, and an adjusting means 21 for adjusting the opening degree of the breathing hole 20 is provided therein.
Is provided. In this adjusting means 21, for example, as shown in the figure, a slide plate 21a that slides in the direction of the arrow along the lid 19 is provided with a hole 21b that can overlap with the breathing hole 20 and the degree of polymerization between the breathing hole 20 and the hole 21b. The opening degree is adjusted by changing. Breathing hole 2
According to the result of the experiment, the inner diameter of 0 is preferably about 1/100 of the inner diameter of the furnace body 10. If the inner diameter is larger than this, flame will be discharged from the breathing hole 20, and if the inner diameter is smaller than this, sufficient breathing action cannot be exhibited.

【0017】炉本体10の側壁から延びる排煙用煙突1
1の内部には傾斜状に配列された多数の除塵用邪魔板1
2がユニットとなって上下に複数段に設けられ、各ユニ
ット毎に噴水装置13とドレン14とが配設されてい
る。噴水装置13は、例えば図2に示すように排煙用煙
突11の内壁に沿って環状に管23を取り付け、この管
23の環状内周に適当間隔に噴出孔23aを貫設してな
るものである。
A smoke stack 1 extending from the side wall of the furnace body 10.
In the inside of 1, a large number of baffles for dust removal 1 arranged in an inclined shape
The unit 2 is provided in a plurality of upper and lower stages, and a fountain device 13 and a drain 14 are provided for each unit. As shown in FIG. 2, for example, the water spouting device 13 has a pipe 23 attached in an annular shape along the inner wall of the smoke exhaust chimney 11, and the ejection holes 23a are formed in the annular inner periphery of the pipe 23 at appropriate intervals. Is.

【0018】噴水装置13は給水管15によって給水ポ
ンプ24を介して浄化槽17に繋がれ、ドレン14は排
水管16によって同じく浄化槽17に繋がれている。ま
た給水管15の途中にはバルブ付きの補給管25に繋が
れ、水分の蒸発に応じて補給管25より水を補給するよ
うになっている。また排煙用煙突11には適宜送風管2
6をその上部側に合流連結し、該送風管26からの風を
矢印で示すように排煙用煙突11内に上方に向かって噴
出することによって排煙用煙突11内の排ガスの外部へ
の排気を助けるようになっている。
The fountain device 13 is connected by a water supply pipe 15 to a septic tank 17 via a water supply pump 24, and the drain 14 is also connected by a drain pipe 16 to the septic tank 17. A water supply pipe 15 is connected to a supply pipe 25 with a valve in the middle of the water supply pipe 15, and water is supplied from the supply pipe 25 in accordance with evaporation of water. In addition, the flue pipe 2 is appropriately installed in the smoke stack
6 is joined to the upper side of the exhaust pipe, and the wind from the blower pipe 26 is ejected upward into the smoke exhaust chimney 11 as shown by an arrow so that the exhaust gas in the smoke exhaust chimney 11 is discharged to the outside. It is designed to help exhaust.

【0019】本発明の実施例は以上の構成からなり、こ
れを使用するには、炉本体10内に鉄、非鉄金属、合成
樹脂、紙等の産業廃棄物を投入し、火炎供給用兼空気供
給用孔18から火炎を炉本体10内に噴出させて、空気
取入孔22から燃焼用空気を取り入れながら産業廃棄物
を着火させ、充分に着火分布が行き渡った時点で火炎の
供給を停止して圧縮空気の供給に切り換え、該圧縮空気
を炉本体10に噴出させることによって炉本体10内に
燃焼気流を発生させて燃焼効率を上げ、炉本体10内で
の燃焼途上で化学性廃棄物等からのガスの発生により炉
本体10内が設定圧力よりも高くなった場合には呼吸用
孔20から炉本体10内の圧力が自動的に放出されて高
圧ガスによる炉本体10内での爆発現象を未然に防ぎ、
これによって炉本体10内で安全に且つ効率良く燃焼す
ることができる。
The embodiment of the present invention has the above-described structure. To use this, industrial waste such as iron, non-ferrous metal, synthetic resin, and paper is put into the furnace body 10 to supply flame and also as air. A flame is ejected from the supply hole 18 into the furnace body 10 to ignite the industrial waste while taking in the combustion air from the air intake hole 22, and the supply of the flame is stopped when the ignition distribution is sufficiently distributed. To supply compressed air, and by injecting the compressed air into the furnace body 10 to generate a combustion airflow in the furnace body 10 to increase combustion efficiency, and to generate chemical waste during combustion in the furnace body 10. When the inside of the furnace body 10 becomes higher than the set pressure due to the generation of gas from the inside, the pressure inside the furnace body 10 is automatically released from the breathing hole 20 and the explosion phenomenon inside the furnace body 10 due to the high pressure gas. To prevent
This allows safe and efficient combustion in the furnace body 10.

【0020】燃焼により発生する排気ガスは、排煙用煙
突11内に多段状に設けた除塵用邪魔板12に当接して
蛇行状に上昇し、その上昇途上で噴水装置13から噴出
する噴霧水に接触して排気ガス中に含まれる煤煙や塵埃
の粒子が吸着され、この粒子の吸着した排水は除塵用邪
魔板12などをつたって流下し、ドレン14に集められ
る。このドレン14にあつめられた排水は排水管16に
よって浄化槽17に回収される。上述の噴水装置13と
除塵用邪魔板12とは排煙用煙突11内に多段状に多数
配設され且つこれがシャワー状ないしカーテン状に噴出
されるため、尚かつ排気ガスが排煙用煙突11内を蛇行
状に上昇するために、排気ガスに含まれる煤煙や塵埃は
その殆どが排水に含まれて回収されることになり、その
除塵効率を格段に上げることができ、排煙用煙突11か
らは煤煙が放出されることが殆どない。
Exhaust gas generated by combustion comes into contact with a dust removing baffle plate 12 provided in a stack in a smoke exhaust chimney 11 and ascends in a meandering manner. The particles of soot and dust contained in the exhaust gas are adsorbed upon contact with the exhaust gas, and the wastewater adsorbed by the particles flows down through the dust removing baffle plate 12 and the like, and is collected in the drain 14. The drainage collected in the drain 14 is collected in the septic tank 17 by the drainage pipe 16. Since the above-described fountain device 13 and the dust removing baffle plate 12 are arranged in multiple stages in the smoke exhaust chimney 11 and are ejected in a shower shape or a curtain shape, the exhaust gas is still exhaust gas chimney 11 Since the inside of the exhaust gas rises in a meandering manner, most of the soot and dust contained in the exhaust gas are contained in the waste water and collected, so that the dust removal efficiency can be markedly increased, and the smoke exhaust chimney 11 Soot is rarely emitted from the.

【0021】そして浄化槽17に回収された排水は浄化
された後、再び清澄圧力水として給水ポンプ24によっ
て噴水装置13に供給される。このように排水を再利用
することによって水の消費量も軽減することができる。
The waste water collected in the septic tank 17 is purified and then supplied again to the fountain device 13 by the water supply pump 24 as refining pressure water. By reusing the waste water in this way, the water consumption can also be reduced.

【0022】[0022]

【発明の効果】本発明の請求孔1によれば、炉本体内の
排煙が排煙用煙突を通過する途上でそれに含まれる煤煙
や塵埃の粒子が噴水装置によって噴出される噴霧水に効
率的に吸着され、これが排水として回収されることにな
り、除塵効率を格段に向上することができる。
EFFECTS OF THE INVENTION According to claim 1 of the present invention, the soot and dust particles contained in the flue gas in the furnace body passing through the flue gas stack are efficiently used for the spray water ejected by the fountain device. Is adsorbed as a wastewater, and this is collected as wastewater, so that the dust removal efficiency can be remarkably improved.

【0023】しかも除塵機構は排煙用煙突の空間を利用
してこの内部に設けられるため、炉本体の外部には浄化
槽を設けるだけでよく、従って溶解焼却炉全体の設置面
積が格段に少なくなり、このためトータルコストを大幅
に低減することができる。
Moreover, since the dust removal mechanism is provided inside the smoke exhaust chimney, it is only necessary to provide a septic tank outside the furnace main body, and therefore the installation area of the entire smelting incinerator is significantly reduced. Therefore, the total cost can be significantly reduced.

【0024】また排煙用煙突内の煤煙や塵埃を含む排水
を浄化槽に回収すると共に、これを清澄水として再び噴
水装置に供給するようになっているため、水の消費量も
少なくこの面からも除塵のための費用をも低減すること
ができる。
Further, since the wastewater containing soot and dust in the smoke exhaust chimney is collected in the septic tank and is supplied again to the fountain device as clear water, the water consumption is small and from this aspect. Also, the cost for dust removal can be reduced.

【0025】また請求項2によれば、炉本体内の産業廃
棄物を均一に且つ効率的に溶解焼却することができ、且
つ燃焼油の消費量が少ないため、燃費の軽減に貢献する
ことができる。
According to the second aspect, the industrial waste in the furnace body can be uniformly and efficiently melted and incinerated, and the consumption of combustion oil is small, which contributes to the reduction of fuel consumption. it can.

【0026】また炉本体内の設定圧力を、単に炉本体の
蓋体に呼吸用孔を設けるだけで行うようになっているた
め、構成が簡単で故障が少なく実用的である。
Further, since the set pressure in the furnace body is set by simply providing the breathing hole in the lid body of the furnace body, the structure is simple and there are few failures and it is practical.

【0027】また請求項3によれば、前記呼吸用孔は調
整手段によってその開度が調整可能となっているため、
炉本体内の被燃焼物の種類や量あるいは火力に応じて炉
本体内の設定圧力が変化する場合あるいは経時的に変化
する場合にこれに合わせて呼吸用孔の開度を調整するこ
とができ、それだけ汎用性に優れている。
Further, according to claim 3, since the opening of the breathing hole can be adjusted by the adjusting means,
When the set pressure in the furnace body changes or changes over time depending on the type and amount of burned material in the furnace body or the thermal power, the opening of the breathing hole can be adjusted accordingly. , It is so versatile.

【0028】また請求項4によれば、炉本体内に燃焼気
流を発生させることによって炉本体内の燃焼効率を向上
させ燃費の軽減に貢献すると共に、炉本体内の圧力を一
定に保持し、特に化学性廃棄物から発生するガスによる
異常の高圧現象を防止し、ガスの炉本体内での異常圧に
よる爆発の生起を有効に阻止することができ、炉本体の
寿命を格段に長くのばすことができる。
Further, according to claim 4, by generating a combustion air flow in the furnace body, the combustion efficiency in the furnace body is improved to contribute to the reduction of fuel consumption, and the pressure in the furnace body is kept constant. Especially, it is possible to prevent abnormal high pressure phenomenon due to gas generated from chemical waste, effectively prevent the occurrence of explosion due to abnormal pressure of gas in the furnace body, and extend the life of the furnace body significantly. You can

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

【図1】本発明の一実施例の縦断正面図である。FIG. 1 is a vertical sectional front view of an embodiment of the present invention.

【図2】同要部の横断平面図である。FIG. 2 is a cross-sectional plan view of the main part.

【図3】従来技術の縦断正面図である。FIG. 3 is a vertical sectional front view of a conventional technique.

【符号の説明】[Explanation of symbols]

10 炉本体 11 排煙用煙突 12 除塵用邪魔板 13 噴水装置 14 ドレン 15 給水管 16 排水管 17 浄化槽 18 火炎供給用兼空気供給用孔 19 蓋体 20 呼吸用孔 21 調整手段 10 furnace body 11 smoke exhaust chimney 12 dust removing baffle plate 13 fountain device 14 drain 15 water supply pipe 16 drainage pipe 17 septic tank 18 flame supply and air supply hole 19 lid 20 breathing hole 21 adjusting means

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 炉本体内の排煙を排出する排煙用煙突内
に除塵用邪魔板を上下方向に多数段に設けると共に、上
記煙突内にその上下方向適当間隔に圧力水を噴出する噴
水装置を取り付け、且つ上記邪魔板に伝って流下する排
水を受けるドレンを配設し、上記噴水装置に連通する給
水管と上記ドレンに連通する排水管とを浄化槽を介して
連通連結してなる溶解焼却炉。
1. A fountain for ejecting pressure water at an appropriate vertical interval in the chimney while a plurality of baffles for dust removal are provided in a vertical direction in a chimney for exhausting the smoke emitted from the furnace body. Dissolution by attaching a device and arranging a drain for receiving drainage that flows down to the baffle plate and connecting a water supply pipe communicating with the fountain device and a drain pipe communicating with the drain through a septic tank Incinerator.
【請求項2】 炉本体の周方向適当間隔に火炎供給用兼
空気供給用孔を設けると共に、炉本体の蓋体に呼吸用孔
を設けてなる溶解焼却炉。
2. A smelting incinerator in which a flame-supplying and air-supplying hole is provided at appropriate intervals in the circumferential direction of the furnace body, and a breathing hole is provided in the lid of the furnace body.
【請求項3】 前記呼吸用孔は調整手段によってその開
度が調整可能となっている請求項2記載の溶解焼却炉。
3. The melting incinerator according to claim 2, wherein the opening of the breathing hole can be adjusted by an adjusting means.
【請求項4】 炉本体の周方向適当間隔に設けられた火
炎供給用兼空気供給孔から炉本体内に火炎を噴射させて
炉本体内の被燃焼物に着火させ、その着火後に火炎から
圧縮空気に切り換えて火炎供給用兼空気供給孔から圧縮
空気を噴射して炉本体内に燃焼気流を発生させ、且つ炉
本体内の圧力を炉本体に設けた呼吸孔によって自調整さ
せるようにしてなる溶解焼却方法。
4. A flame-injecting and air-supplying hole provided at appropriate intervals in the circumferential direction of the furnace body to inject a flame into the furnace body to ignite a burned material in the furnace body, and after the ignition, compress from the flame. By switching to air and injecting compressed air from the flame-supplying / air-supplying hole to generate a combustion air flow in the furnace body, and adjusting the pressure in the furnace body by a breathing hole provided in the furnace body. Melting and incineration method.
JP4069563A 1992-02-18 1992-02-18 Melting incinerator Expired - Lifetime JP2525105B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4069563A JP2525105B2 (en) 1992-02-18 1992-02-18 Melting incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4069563A JP2525105B2 (en) 1992-02-18 1992-02-18 Melting incinerator

Publications (2)

Publication Number Publication Date
JPH06193842A true JPH06193842A (en) 1994-07-15
JP2525105B2 JP2525105B2 (en) 1996-08-14

Family

ID=13406359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4069563A Expired - Lifetime JP2525105B2 (en) 1992-02-18 1992-02-18 Melting incinerator

Country Status (1)

Country Link
JP (1) JP2525105B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019124420A (en) * 2018-01-18 2019-07-25 株式会社環健スーパーテクノ chimney

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102052687A (en) * 2011-02-17 2011-05-11 大连瑞希特木业制品有限公司 Spray dust removal type environment-friendly chimney

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4947254A (en) * 1971-04-27 1974-05-07
JPS4996544U (en) * 1972-12-12 1974-08-20
JPS5038371A (en) * 1973-08-07 1975-04-09
JPS5173874U (en) * 1974-12-07 1976-06-10
JPS51105665U (en) * 1975-02-22 1976-08-24
JPS551092A (en) * 1978-05-22 1980-01-07 Gen Electric Contact switch
JPS57207723A (en) * 1981-06-15 1982-12-20 Shogo Fujimori Boiler utilizing waste tire
JPS59122813A (en) * 1982-12-28 1984-07-16 Mitsubishi Paper Mills Ltd Method for drying and incinerating sludge of waste water treatment
JPS63164929U (en) * 1987-04-15 1988-10-27

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4947254A (en) * 1971-04-27 1974-05-07
JPS4996544U (en) * 1972-12-12 1974-08-20
JPS5038371A (en) * 1973-08-07 1975-04-09
JPS5173874U (en) * 1974-12-07 1976-06-10
JPS51105665U (en) * 1975-02-22 1976-08-24
JPS551092A (en) * 1978-05-22 1980-01-07 Gen Electric Contact switch
JPS57207723A (en) * 1981-06-15 1982-12-20 Shogo Fujimori Boiler utilizing waste tire
JPS59122813A (en) * 1982-12-28 1984-07-16 Mitsubishi Paper Mills Ltd Method for drying and incinerating sludge of waste water treatment
JPS63164929U (en) * 1987-04-15 1988-10-27

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019124420A (en) * 2018-01-18 2019-07-25 株式会社環健スーパーテクノ chimney

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