JPH1089653A - Temperature controlling method for combustion melting furnace and waste treatment apparatus - Google Patents

Temperature controlling method for combustion melting furnace and waste treatment apparatus

Info

Publication number
JPH1089653A
JPH1089653A JP8247490A JP24749096A JPH1089653A JP H1089653 A JPH1089653 A JP H1089653A JP 8247490 A JP8247490 A JP 8247490A JP 24749096 A JP24749096 A JP 24749096A JP H1089653 A JPH1089653 A JP H1089653A
Authority
JP
Japan
Prior art keywords
temperature
combustion
furnace
melting furnace
pyrolysis
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.)
Withdrawn
Application number
JP8247490A
Other languages
Japanese (ja)
Inventor
Yutaka Okubo
豊 大久保
Atsushi Ishikawa
厚史 石川
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 JP8247490A priority Critical patent/JPH1089653A/en
Publication of JPH1089653A publication Critical patent/JPH1089653A/en
Withdrawn legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To simply, easily and stably control a temperature when a temperature in a combustion melting furnace becomes high due to change of quality or amount of waste or other cause by lowering the temperature in the furnace by supplying excess combustion air at the time of exceeding a predetermined value at the temperature in the furnace. SOLUTION: Waste (a) heated by heated air (g) is thermally decomposed to become thermal decomposition gas G and decomposed residue (b) containing nonvolatile components, and separated by an exhaust unit 6. The gas G is supplied to a burner 14 of a combustion melting furnace 13. When the temperature of the furnace 13 becomes high exceeding a predetermined value, it is sensed by a temperature sensor in the furnace, and combustion air (e) burnt, for example at an air ratio of 1.3 is supplied excessively exceeding this air amount. To increase the supply amount of the air (e), a volume of a forced draft fan 18 is previously set to high, and the air is blown from blowing ports 19a to 19d by considering a rising ratio of the temperature in the furnace and a temperature distribution in the furnace and considering a balance between the blowing amount and blowing positions.

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(家庭やオ
フィスなどから出される都市ごみなどの一般廃棄物、廃
プラスチック、カーシュレッダー・ダスト、廃オフィス
機器、電子機器、化成品などの産業廃棄物等可燃物を含
むもの)の熱分解によって生成する熱分解ガスと、同じ
く熱分解によって生成した熱分解残留物中の燃焼性成分
とを供給し燃焼させる廃棄物処理における燃焼溶融炉の
運転方法及びこの燃焼溶融炉の運転方法を用いた廃棄物
処理装置に関するものである。
The present invention relates to industrial waste such as waste (general waste such as municipal waste from homes and offices, waste plastic, car shredder dust, waste office equipment, electronic equipment, and chemical products). Method for operating a combustion-melting furnace in waste treatment in which a pyrolysis gas generated by the pyrolysis of a substance (including a combustible material) and a combustible component in a pyrolysis residue also generated by the pyrolysis are supplied and burned And a waste disposal apparatus using the method for operating a combustion melting furnace.

【0002】[0002]

【従来の技術】従来、廃棄物の熱分解によって熱分解ガ
スと熱分解残留物とを生成し、熱分解残留物からは燃焼
性成分と不燃焼性成分とを分離し、この燃焼性成分と前
記熱分解ガスとを供給する燃焼溶融炉は、この燃焼性成
分と熱分解ガスとを燃焼用空気と共に押し込んで燃焼さ
せ、生じた灰分を溶融してスラグ化するものである(特
公平6−56253号公報等)。
2. Description of the Related Art Conventionally, a pyrolysis gas and a pyrolysis residue are generated by pyrolysis of waste, and a flammable component and a non-flammable component are separated from the pyrolysis residue. The combustion and melting furnace for supplying the pyrolysis gas pushes the combustible component and the pyrolysis gas together with the combustion air and burns, and melts the generated ash to form slag (Japanese Patent Publication No. Hei 6-1994). No. 56253).

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記燃
焼溶融炉において、廃棄物の種類、例えば生ごみ、プラ
スチック、紙等その含有水分量や成分等による発熱量の
変動又は供給される廃棄物量の変動或いはその他の要因
により、廃棄物を熱分解して生成される熱分解ガスや燃
焼性成分の性状や生成量が変動し、これら熱分解ガスや
燃焼性成分を供給する燃焼溶融炉の炉内温度が所定の温
度を超えて高くなることがある。
However, in the above-mentioned combustion melting furnace, fluctuations in the amount of heat generated due to the type of waste, for example, garbage, plastics, paper, etc., due to the water content and components, or fluctuations in the amount of waste supplied. Or, due to other factors, the properties and amounts of pyrolysis gas and combustible components generated by pyrolysis of waste fluctuate, and the temperature in the furnace of the combustion melting furnace that supplies these pyrolysis gases and combustible components May rise above a predetermined temperature.

【0004】このような場合、燃焼溶融炉の後流の約2
00℃の排ガスを燃焼溶融炉に戻して炉内温度を下げ制
御している。しかし、排ガスによって炉内温度を制御す
る方法では、排ガスを戻す装置が必要で、装置自体が複
雑になる恐れがあった。
In such a case, about 2 downstream of the combustion melting furnace is required.
The exhaust gas at 00 ° C. is returned to the combustion melting furnace to control the temperature in the furnace by lowering it. However, in the method of controlling the furnace temperature by the exhaust gas, a device for returning the exhaust gas is required, and the device itself may be complicated.

【0005】本発明の目的は、廃棄物処理における燃焼
溶融炉の温度制御方法において、廃棄物の質や量の変動
その他の要因によって炉内温度が高くなった時に、簡便
で容易に安定した温度制御が可能な燃焼溶融炉の温度制
御方法及びこの方法を用いた廃棄物処理装置を提供する
ことである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for controlling the temperature of a combustion melting furnace in the treatment of waste, which is simple and easy to stabilize when the temperature inside the furnace increases due to fluctuations in the quality and quantity of waste and other factors. An object of the present invention is to provide a controllable temperature control method for a combustion melting furnace and a waste disposal apparatus using the method.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
本発明は、投入された廃棄物を熱分解し、熱分解ガスと
主として不揮発性成分からなる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
離した後、燃焼溶融炉によって前記熱分解ガスと前記燃
焼性成分とを燃焼用空気と共に燃焼させ、生じた灰分を
溶融し、該燃焼、溶融の際に生じた燃焼排ガスを冷却し
排出する廃棄物処理における燃焼溶融炉の温度制御方法
において、前記燃焼溶融炉の炉内温度が所定の値を超え
て上昇した時に、前記燃焼用空気を過剰に供給して前記
燃焼溶融炉の炉内温度を下げることである。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention is to thermally decompose a waste that has been introduced, to generate a pyrolysis gas and a pyrolysis residue mainly composed of nonvolatile components, After separating the decomposition residue into a combustible component and a non-combustible component, the pyrolysis gas and the combustible component are burned together with combustion air by a combustion melting furnace, and the resulting ash is melted. In the method for controlling the temperature of a combustion melting furnace in a waste treatment for cooling and discharging the combustion exhaust gas generated during melting, when the temperature in the furnace of the combustion melting furnace rises above a predetermined value, the combustion air is cooled. That is, the temperature in the furnace of the combustion melting furnace is reduced by supplying the excess.

【0007】燃焼溶融炉の炉内温度が廃棄物の質又は量
の変動、その他の要因によって所定の値を超えて上昇し
た時に、温度の低い燃焼用空気を過剰に供給することに
よって燃焼溶融炉の炉内温度を確実、安定に下げること
が出来る。
[0007] When the temperature in the furnace of the combustion and melting furnace rises above a predetermined value due to fluctuations in the quality or quantity of waste and other factors, the combustion and melting furnace is supplied by excessively supplying low-temperature combustion air. Furnace temperature can be reliably and stably reduced.

【0008】又、投入された廃棄物を加熱空気によって
加熱し、熱分解ガスと主として不揮発性成分からなる熱
分解残留物とに熱分解する熱分解反応器と、該熱分解反
応器で生成される熱分解ガスと熱分解残留物とを分離し
排出する排出装置と、該排出装置から排出される前記熱
分解残留物を燃焼性成分と不燃焼性成分とに分離する分
離装置と、該燃焼性成分と前記熱分解ガスとを燃焼用空
気と共に燃焼し、生じた灰分を溶融する燃焼溶融炉と、
該燃焼溶融炉で生じた燃焼排ガスを冷却するガス冷却装
置とを有する廃棄物処理装置において、前記燃焼溶融炉
は、上記燃焼溶融炉の温度制御方法によって温度制御さ
れることである。
[0008] Further, a pyrolysis reactor which heats the introduced waste with heated air to pyrolyze it into a pyrolysis gas and a pyrolysis residue mainly composed of non-volatile components, and a pyrolysis reactor produced by the pyrolysis reactor. A discharge device for separating and discharging a pyrolysis gas and a pyrolysis residue, a separation device for separating the pyrolysis residue discharged from the discharge device into a combustible component and a non-combustible component, A combustion-melting furnace that burns the toxic component and the pyrolysis gas together with the combustion air and melts the generated ash.
In a waste treatment apparatus having a gas cooling device for cooling combustion exhaust gas generated in the combustion melting furnace, the temperature of the combustion melting furnace is controlled by the temperature control method of the combustion melting furnace.

【0009】[0009]

【発明の実施の形態】以下本発明に係る廃棄物処理にお
ける燃焼溶融炉の温度制御方法及びこれを用いた廃棄物
処理装置の実施の形態を図面に基づいて詳細に説明す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of a method for controlling the temperature of a combustion melting furnace in a waste treatment and a waste treatment apparatus using the same according to the present invention will be described below in detail with reference to the drawings.

【0010】図1は、本発明に係る廃棄物処理装置の一
実施の形態を示す系統図である。本実施の形態の廃棄物
処理装置1は、都市ごみ等の廃棄物aを、例えば二軸剪
断式等の破砕機で、150mm角以下に破砕し、コンベ
ア等により投入部2に投入し、スクリューフィーダ3を
経て熱分解反応器5に供給する。熱分解反応器5に供給
された廃棄物aは、燃焼溶融炉13の後流側に配置され
た図示していない熱交換器により加熱され、加熱空気ラ
インL1によって導入される加熱空気g(熱媒体)によ
り300〜600℃に、通常は450℃程度に加熱され
る。
FIG. 1 is a system diagram showing an embodiment of a waste disposal apparatus according to the present invention. The waste disposal apparatus 1 of the present embodiment crushes waste a such as municipal waste into a 150 mm square or less with a crusher such as a biaxial shearing type, and throws the crushed waste into the loading section 2 by a conveyor or the like. It is supplied to the thermal decomposition reactor 5 via the feeder 3. Waste a fed to the pyrolytic reactor 5 is heated by the heat exchanger (not shown) disposed on the downstream side of the combustion melting furnace 13, heated air is introduced by the heated air lines L 1 g ( The heating medium is used to heat to 300 to 600 ° C, usually to about 450 ° C.

【0011】更に、加熱空気gにより加熱された廃棄物
aは、熱分解して熱分解ガスG1と、主として不揮発性
成分からなる熱分解残留物bとになり、排出装置6に送
られて分離される。排出装置6で分離された熱分解ガス
1は、排出装置6の上部から熱分解ガスラインL2を経
て燃焼溶融炉13のバーナ14に供給される。
Further, the waste a heated by the heated air g is thermally decomposed into a pyrolysis gas G 1 and a pyrolysis residue b mainly composed of a non-volatile component. Separated. The pyrolysis gas G 1 separated by the discharge device 6 is supplied from above the discharge device 6 to the burner 14 of the combustion melting furnace 13 via the pyrolysis gas line L 2 .

【0012】又、排出装置6から排出された熱分解残留
物bは、450℃程度の比較的高温であるため、冷却装
置8により80℃程度に冷却され、例えば磁選式、うず
電流式、遠心式又は風力選別式等の公知の単独又は組み
合わされた分離装置9に供給され、燃焼性成分cと不燃
焼性成分dとに分離され、不燃焼性成分dはコンテナ1
0に回収され再利用される。燃焼性成分cは、粉砕機1
1により、例えば1mm以下に微粉砕され、燃焼性成分
ラインL3を経て燃焼溶融炉13に供給される。
Further, since the pyrolysis residue b discharged from the discharge device 6 has a relatively high temperature of approximately 450 ° C., it is cooled to approximately 80 ° C. by the cooling device 8 and is, for example, a magnetic separation type, an eddy current type, or a centrifugal type. Is supplied to a known single or combined separation device 9 such as an incineration type or a wind separation type, and is separated into a combustible component c and a non-combustible component d.
Collected to 0 and reused. The combustible component c is supplied to the pulverizer 1
The 1, for example, 1mm milled below, supplied to the combustion melting furnace 13 through the combustible component line L 3.

【0013】一方、押込送風機18により供給される燃
焼用空気eの一部は燃焼溶融炉のバーナ14から吹き込
まれると共に、バーナ14の近傍に設けられた矢印19
aで示された吹込口からも吹き込まれ、熱分解ガスライ
ンL2から供給される熱分解ガスG1及び前記燃焼性成分
cと共に、燃焼溶融炉13で1,300℃程度の高温域
で燃焼される。更に、燃焼用空気eは、炉上部の矢印1
9bで示された吹込口、二次空気として矢印19cで示
された吹込口、三次空気として矢印19dで示された吹
込口の各々から吹き込まれる。
On the other hand, a part of the combustion air e supplied by the forced air blower 18 is blown from the burner 14 of the combustion melting furnace, and an arrow 19 provided near the burner 14.
a, and is burned in the combustion melting furnace 13 at a high temperature of about 1,300 ° C. together with the pyrolysis gas G 1 supplied from the pyrolysis gas line L 2 and the combustible component c. Is done. Further, the combustion air e is indicated by arrow 1 at the top of the furnace.
Air is blown from each of the blowout port shown by 9b, the blowout port shown by arrow 19c as secondary air, and the blowout port shown by arrow 19d as tertiary air.

【0014】燃焼性成分cの燃焼の結果生じた灰分は溶
融スラグfとなって、燃焼溶融炉13の内壁に付着し、
更に、内壁を流下して底部排出口15から水槽16に落
下し冷却固化される。
The ash generated as a result of the combustion of the combustible component c becomes molten slag f and adheres to the inner wall of the combustion melting furnace 13,
Furthermore, it flows down the inner wall, falls from the bottom outlet 15 into the water tank 16, and is cooled and solidified.

【0015】次に、燃焼溶融炉13で生じた燃焼排ガス
2は、高温空気加熱器17を経て煙道ガスラインL5
介してガス冷却装置、例えば水をスプレーして燃焼排ガ
スG2を冷却するガス冷却塔20で冷却され、煙道ガス
ラインL6を介して集塵器21で除塵され、更に排ガス
浄化器22で有害成分が除去された後、低温のクリーン
な排ガスG3となって誘引送風機23を介して煙突24
から大気へ放出される。クリーンな排ガスG3の一部は
ファン25を介して排ガス循環ラインL7により冷却装
置8に戻される。
Next, the flue gas G 2 generated in the combustion melting furnace 13 passes through a high-temperature air heater 17 and is passed through a flue gas line L 5 through a gas cooling device, for example, water to spray the flue gas G 2 . is cooled in a gas cooling tower 20 for cooling, is dust in the dust collector 21 through the flue gas line L 6, after removing the harmful components further exhaust converter 22, a low-temperature clean gas G 3 of Chimney 24 via the draft fan 23
Emitted from the atmosphere. Some of the clean exhaust gas G 3 are returned to the cooling unit 8 by the exhaust gas circulation line L 7 via a fan 25.

【0016】以上のような構成の廃棄物処理装置1にお
いて、燃焼溶融炉13は、先に説明したように、廃棄物
aの種類、例えば生ごみ、プラスチック、紙等その含有
水分量や成分等による発熱量の変動又は供給する廃棄物
量の変動或いはその他の要因により、廃棄物aを熱分解
して生成される熱分解ガスG1や燃焼性成分cの性状や
生成量が変動し、これらを供給する燃焼溶融炉13の炉
内温度が所定の値、例えば1300℃を超えて高くなる
ことがある。
In the waste treatment apparatus 1 having the above-described configuration, as described above, the combustion and melting furnace 13 includes the type of the waste a, for example, garbage, plastic, paper, etc. fluctuations or other factors change or supplying waste of calorific value by waste a and fluctuates properties and yield of the pyrolysis gases G 1 and combustible components c produced by thermal decomposition, these In some cases, the temperature in the furnace 13 of the supplied combustion melting furnace 13 becomes higher than a predetermined value, for example, 1300 ° C.

【0017】本実施の形態の燃焼溶融炉の温度制御方法
は、上記のように燃焼溶融炉13の炉内温度が所定の値
を超えて高くなった場合、それを炉内温度センサーで検
知し、通常例えば燃焼用空気eを空気比1.3で燃焼さ
せているものを、この空気量を超えて過剰に供給する。
燃焼用空気eの供給量を増やすには、図1に示すよう
に、押込送風機18の容量を予め高く設定しておき、燃
焼用空気eの過剰供給に備える。燃焼用空気eの過剰吹
込供給量は、炉内温度の上昇割合、炉内温度分布、その
他の条件を考慮し、吹込量とその吹き込み個所のバラン
スを考慮して吹込口19a〜19dから吹き込む。
In the method for controlling the temperature of the combustion and melting furnace according to the present embodiment, when the furnace temperature of the combustion and melting furnace 13 exceeds a predetermined value as described above, it is detected by a furnace temperature sensor. Usually, for example, combustion air e burned at an air ratio of 1.3 is supplied in excess of this air amount.
In order to increase the supply amount of the combustion air e, as shown in FIG. 1, the capacity of the push-in blower 18 is set high in advance to prepare for an excessive supply of the combustion air e. The excess air supply amount of the combustion air e is blown from the inlets 19a to 19d in consideration of the rate of increase in the furnace temperature, the furnace temperature distribution, and other conditions, and the balance of the blown amount and the location of the blow.

【0018】燃焼溶融炉13に吹き込む燃焼用空気e
は、常温の空気を使用するので温度が低く、従来の排ガ
スを吹き込む場合に比べ、少ない空気量で炉内温度を冷
却出来る。その上、従来使用されている排ガス循環装置
を省くことが出来、設備が簡便で経済的である。
Combustion air e blown into the combustion melting furnace 13
Since air at room temperature is used, the temperature is low, and the furnace temperature can be cooled with a smaller amount of air than in the case where conventional exhaust gas is blown. In addition, the exhaust gas circulation device conventionally used can be omitted, and the equipment is simple and economical.

【0019】[0019]

【発明の効果】本発明の廃棄物処理における燃焼溶融炉
の温度制御方法によれば、廃棄物の質や量の変動その他
の要因によって炉内温度が高くなった時に、簡便で容易
に安定して炉内温度を下げることが出来る。
According to the method for controlling the temperature of a combustion melting furnace in the waste treatment of the present invention, when the temperature inside the furnace is increased due to fluctuations in the quality and quantity of waste and other factors, it is simple and easy to stabilize. To lower the furnace temperature.

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

【図1】本発明に係る廃棄物処理装置の一実施の形態を
示す系統図である。
FIG. 1 is a system diagram showing one embodiment of a waste disposal apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 廃棄物処理装置 5 熱分解反応器 6 排出装置 9 分離装置 13 燃焼溶融炉 20 ガス冷却塔(ガス冷却装置) G1 熱分解ガス G2 燃焼排ガス a 廃棄物 b 熱分解残留物 c 燃焼性成分 d 不燃焼性成分 e 燃焼用空気 g 加熱空気(熱媒体)1 waste disposal device 5 the pyrolysis reactor 6 discharge device 9 separator 13 combustion melting furnace 20 the gas cooling tower (gas cooler) G 1 pyrolysis gas G 2 combustion exhaust a waste b pyrolysis residue c combustible components d Non-combustible component e Combustion air g Heated air (heat medium)

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F23G 5/027 ZAB F23G 5/027 ZABZ 5/16 ZAB 5/16 ZABE F23J 15/06 ZAB F23J 15/00 ZABK ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI F23G 5/027 ZAB F23G 5/027 ZABZ 5/16 ZAB 5/16 ZABE F23J 15/06 ZAB F23J 15/00 ZABK

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 投入された廃棄物を熱分解し、熱分解ガ
スと主として不揮発性成分からなる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
分離した後、燃焼溶融炉によって前記熱分解ガスと前記
燃焼性成分とを燃焼用空気と共に燃焼させ、生じた灰分
を溶融し、該燃焼、溶融の際に生じた燃焼排ガスを冷却
し排出する廃棄物処理における燃焼溶融炉の温度制御方
法において、前記燃焼溶融炉の炉内温度が所定の値を超
えて上昇した時に、前記燃焼用空気を過剰に供給して前
記燃焼溶融炉の炉内温度を下げることを特徴とする燃焼
溶融炉の温度制御方法。
Claims: 1. A thermal decomposition of an input waste to generate a pyrolysis gas and a pyrolysis residue mainly composed of a non-volatile component, and convert the pyrolysis residue into a combustible component and a non-combustible component. After separation, the pyrolysis gas and the combustible component are burned together with combustion air by a combustion melting furnace to melt the generated ash, and to cool and discharge the flue gas generated during the combustion and melting. In the method for controlling the temperature of the combustion melting furnace in the material treatment, when the furnace temperature of the combustion melting furnace rises above a predetermined value, the combustion air is excessively supplied to increase the furnace temperature of the combustion melting furnace. A method for controlling the temperature of a combustion melting furnace, characterized by lowering the temperature.
【請求項2】 投入された廃棄物を加熱空気によって加
熱し、熱分解ガスと主として不揮発性成分からなる熱分
解残留物とに熱分解する熱分解反応器と、該熱分解反応
器で生成される熱分解ガスと熱分解残留物とを分離し排
出する排出装置と、該排出装置から排出される前記熱分
解残留物を燃焼性成分と不燃焼性成分とに分離する分離
装置と、該燃焼性成分と前記熱分解ガスとを燃焼用空気
と共に燃焼し、生じた灰分を溶融する燃焼溶融炉と、該
燃焼溶融炉で生じた燃焼排ガスを冷却するガス冷却装置
とを有する廃棄物処理装置において、前記燃焼溶融炉
は、請求項1に記載の燃焼溶融炉の温度制御方法によっ
て温度制御されることを特徴とする廃棄物処理装置。
2. A pyrolysis reactor which heats the introduced waste with heated air and pyrolyzes into a pyrolysis gas and a pyrolysis residue mainly composed of non-volatile components, and a pyrolysis reactor produced by the pyrolysis reactor. An exhaust device for separating and discharging a pyrolysis gas and a pyrolysis residue, a separation device for separating the pyrolysis residue discharged from the exhaust device into a combustible component and a non-combustible component, And a pyrolysis gas, which burns the pyrolytic gas together with the combustion air, and melts the generated ash, and a gas cooling device that cools the combustion exhaust gas generated in the combustion melting furnace. A waste treatment apparatus, wherein the temperature of the combustion melting furnace is controlled by the temperature control method of the combustion melting furnace according to claim 1.
JP8247490A 1996-09-19 1996-09-19 Temperature controlling method for combustion melting furnace and waste treatment apparatus Withdrawn JPH1089653A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8247490A JPH1089653A (en) 1996-09-19 1996-09-19 Temperature controlling method for combustion melting furnace and waste treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8247490A JPH1089653A (en) 1996-09-19 1996-09-19 Temperature controlling method for combustion melting furnace and waste treatment apparatus

Publications (1)

Publication Number Publication Date
JPH1089653A true JPH1089653A (en) 1998-04-10

Family

ID=17164249

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8247490A Withdrawn JPH1089653A (en) 1996-09-19 1996-09-19 Temperature controlling method for combustion melting furnace and waste treatment apparatus

Country Status (1)

Country Link
JP (1) JPH1089653A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1301384C (en) * 2005-05-24 2007-02-21 顾子全 Technique for burning domestic garbage and garbage incinerator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1301384C (en) * 2005-05-24 2007-02-21 顾子全 Technique for burning domestic garbage and garbage incinerator

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