JPH0245620Y2 - - Google Patents

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Publication number
JPH0245620Y2
JPH0245620Y2 JP1986015199U JP1519986U JPH0245620Y2 JP H0245620 Y2 JPH0245620 Y2 JP H0245620Y2 JP 1986015199 U JP1986015199 U JP 1986015199U JP 1519986 U JP1519986 U JP 1519986U JP H0245620 Y2 JPH0245620 Y2 JP H0245620Y2
Authority
JP
Japan
Prior art keywords
combustion
wind box
waste
supply pipe
air supply
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1986015199U
Other languages
Japanese (ja)
Other versions
JPS62131237U (en
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
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Priority to JP1986015199U priority Critical patent/JPH0245620Y2/ja
Publication of JPS62131237U publication Critical patent/JPS62131237U/ja
Application granted granted Critical
Publication of JPH0245620Y2 publication Critical patent/JPH0245620Y2/ja
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 〔考案の技術分野〕 本考案は産業廃棄物を乾留塔にて不完全燃焼さ
せ熱分解により高発熱量を有する乾留ガスに変換
し、該乾留ガスを完全燃焼させ熱交換器にて熱回
収を図る廃棄物の熱回収設備について、その燃焼
筒の空気供給装置の改良に関する。
[Detailed description of the invention] [Technical field of the invention] This invention involves incompletely burning industrial waste in a carbonization tower, converting it into carbonization gas with a high calorific value through thermal decomposition, and then completely burning the carbonization gas to generate heat. This paper relates to improvements to the air supply device for the combustion tube of waste heat recovery equipment that uses an exchanger to recover heat.

〔考案の技術的背景とその問題点〕[Technical background of the invention and its problems]

近時、産業廃棄物は増加の一途をたどつてお
り、この廃棄物を有効に利用及び処理することが
急務となつている。
In recent years, industrial waste has been increasing steadily, and it has become an urgent need to effectively utilize and dispose of this waste.

産業廃棄物、ことに廃タイヤ、廃ゴム、ラミネ
ート紙屑、ラベル印刷屑、クラフト紙、紙接着テ
ープ屑等の廃棄物処理としては、該廃棄物を燃焼
処理するとともに、燃焼熱を廃熱ボイラーで回収
する方法が採用されており、設備としては一般に
産業廃棄物の乾留装置、乾留ガスの燃焼装置及び
燃焼ガスの熱回収装置(例えば廃熱ボイラー)か
ら 構成されている。上記のような廃棄物焼却熱回
収設備における乾留ガスの燃焼装置としては第4
図、第5図に示すような構造が採用されている。
第4図は従来の燃焼筒の断面図、第5図は第4図
の−線矢視図である。燃焼筒1の燃焼室7は
燃焼室上流側の水冷壁8、燃焼室下流側の耐火断
熱壁19で包囲して形成されている。9は耐火壁
を貫通して設けられるガンタイプ式加熱バーナで
あつてその開口部は燃焼室下流側に向つて傾斜し
て設けられている。2は燃焼用空気供給管であつ
て、外部より水冷壁を貫通して挿入し、その先端
が燃焼室中心部に位置し、下流側に向つて開口部
が設けられている。10は燃焼室部分の燃焼用空
気供給管2を包囲して設けられる水冷管である。
11は燃焼用空気供給管先端開口位置にあたる水
冷壁内に環状に設けられるウインドボツクスであ
る。12はウインドボツクスより燃焼用空気供給
管開口部に向つて同一旋回方向に多数設けられる
円弧状のノズルである。13は燃焼用ブロワーで
あつて燃焼用空気供給管とウインドボツクスに連
通している。以上のような構成であつて、まず、
加熱バーナで燃焼筒を加熱しておき、乾留ガス導
入と同時に燃焼用ブロワーを稼動して空気を供給
し、乾留ガスを完全燃焼する。
Industrial waste, especially waste tires, waste rubber, laminated paper waste, label printing waste, kraft paper, paper adhesive tape waste, etc., can be treated by burning the waste and using the combustion heat in a waste heat boiler. The equipment generally consists of a carbonization device for industrial waste, a combustion device for the carbonization gas, and a heat recovery device for the combustion gas (e.g., a waste heat boiler). The fourth type of carbonization gas combustion equipment in the waste incineration heat recovery equipment mentioned above is
A structure as shown in FIG. 5 is adopted.
FIG. 4 is a sectional view of a conventional combustion tube, and FIG. 5 is a view taken along the - line in FIG. 4. The combustion chamber 7 of the combustion tube 1 is surrounded by a water-cooled wall 8 on the upstream side of the combustion chamber and a fireproof and heat-insulating wall 19 on the downstream side of the combustion chamber. Reference numeral 9 denotes a gun-type heating burner that is installed through the fireproof wall, and its opening is inclined toward the downstream side of the combustion chamber. Reference numeral 2 denotes a combustion air supply pipe, which is inserted from the outside through the water-cooled wall, and has its tip located at the center of the combustion chamber and an opening facing downstream. Reference numeral 10 denotes a water-cooled pipe provided surrounding the combustion air supply pipe 2 in the combustion chamber portion.
Reference numeral 11 denotes a wind box provided in an annular shape within the water-cooled wall at the opening position of the tip of the combustion air supply pipe. Reference numeral 12 designates a large number of arc-shaped nozzles that are provided in the same rotation direction from the wind box toward the opening of the combustion air supply pipe. Reference numeral 13 denotes a combustion blower, which communicates with the combustion air supply pipe and the wind box. With the above configuration, first,
The combustion tube is heated with a heating burner, and at the same time as the carbonization gas is introduced, a combustion blower is operated to supply air to completely burn the carbonization gas.

従来の燃焼筒における空気供給装置は以上のよ
うに構成されているので、構造が複雑で製造コス
トが高くまた、空気量の調節に限界があり廃棄物
の種類による対応の範囲が狭い上に、ノズルが焼
損した場合の取替え補修作業が困難で長期間を要
するといつた問題がある。
Conventional air supply devices for combustion cylinders are constructed as described above, and are complex in structure and expensive to manufacture.Also, there are limits to the adjustment of air volume, and the scope of adaptation to different types of waste is narrow. There is a problem in that when a nozzle burns out, replacement and repair work is difficult and takes a long time.

〔考案の目的〕[Purpose of invention]

本考案は上記事項に鑑みてなされたものであつ
て、その目的は製造コストが低廉であつて、かつ
廃棄物の種類による対応範囲が広く、しかも取替
え補修が簡単容易な燃焼筒の空気供給装置を提供
することにある。
The present invention was developed in view of the above-mentioned matters, and its purpose is to provide an air supply device for combustion tubes that is inexpensive to manufacture, has a wide range of applications depending on the type of waste, and is easy to replace and repair. Our goal is to provide the following.

〔考案の概要〕[Summary of the idea]

本考案は上記目的を達成するために、廃棄物か
ら得た乾留ガスを燃焼する燃焼筒1において、先
端が燃焼筒中心部にあつて、乾留ガス流れ方向下
流側に開口する燃焼用空気供給管を設け、この供
給管先端に、供給管より大径の有底筒状部材から
なるウインドボツクスを、その底部を、その底部
が乾留ガス流れ方向下流側に位置するように、接
続手段を介して脱着自在に設け、上記ウインドボ
ツクス底部に、空気分散用の孔を多数個化穿設す
るとともに、ウインドボツクス周囲に、ウインド
ボツクスより小径のノズル部材を同一旋回方向に
多数配設したことを特徴とする。
In order to achieve the above object, the present invention provides a combustion air supply pipe in a combustion tube 1 for burning carbonized gas obtained from waste, whose tip is located at the center of the combustion tube and opens downstream in the flow direction of the carbonized gas. A wind box made of a bottomed cylindrical member having a diameter larger than that of the supply pipe is installed at the tip of the supply pipe, and the bottom of the wind box is connected via a connecting means so that the bottom is located on the downstream side in the flow direction of the carbonized gas. The wind box is removably provided, and the bottom of the wind box is provided with a large number of holes for air dispersion, and a large number of nozzle members having a smaller diameter than the wind box are arranged around the wind box in the same rotation direction. do.

〔考案の実施例〕[Example of idea]

以下、本考案を図面に示した実施例に基づいて
説明する。第1図は廃棄物焼却熱回収設備の構成
図であつて、図面中の符号14は下部において前
述の産業廃棄物を不完全燃焼し、その燃焼熱で廃
棄物の熱分解を行わしめ、可燃性の揮発分を回収
する乾留塔である。1は乾留塔の後流側に設けら
れ、不足空気を供給して乾留ガスを完全燃焼せし
めて高温の燃焼ガスを得るための燃焼筒である。
15は高温燃焼ガス保有熱を回収するための熱交
換器としての廃熱ボイラー、16は軸流サイクロ
ン、17は誘引フアン、18は煙突である。
Hereinafter, the present invention will be explained based on embodiments shown in the drawings. Fig. 1 is a block diagram of a waste incineration heat recovery facility, and reference numeral 14 in the drawing indicates that the aforementioned industrial waste is incompletely combusted in the lower part, and the waste is thermally decomposed with the combustion heat, resulting in combustible This is a carbonization tower that recovers volatile volatile matter. Reference numeral 1 denotes a combustion cylinder provided on the downstream side of the carbonization tower to completely burn the carbonization gas by supplying insufficient air to obtain high-temperature combustion gas.
15 is a waste heat boiler as a heat exchanger for recovering heat retained in high-temperature combustion gas, 16 is an axial flow cyclone, 17 is an induction fan, and 18 is a chimney.

第2図は本考案における燃焼筒の断面図、第3
図は第2図の−矢視図である。図面中の符号
7は燃焼筒の燃焼室であつて、上流側の水冷壁8
と下流側の耐火断熱壁19で包囲して円筒状に形
成される。燃焼室下流側を耐火断熱壁とするのは
燃焼炎の冷却を防止し、完全燃焼させるためであ
る。2は燃焼筒外部より水冷壁を貫通して挿入さ
れる燃焼用空気供給管であつて、その先端は燃焼
室中心部にあつて乾留ガス流れ方向Aの下流側に
向つて開口している。3は燃焼用空気供給管先端
に設けられる有底筒状部材からなるウインドボツ
クスであつて底部Sが乾留ガス流れ方向下流側に
配されている。このウインドボツクス3は、燃焼
用空気供給管2より大径としてあり、この実施例
においては、後述する水冷壁10と略同一外径に
設定してある。4はウインドボツクス底部Sに所
要寸法の大きさで多数設けられる空気分散用の孔
である。5は円弧状のノズルであつて、ウインド
ボツクス周壁に同一旋回方向に多数設けられる。
該ノズルの径は、上記ウインドボツクス3より小
径としてあり、開口部はウインドボツクスと水冷
壁のほぼ中心部に位置し、ウインドボツクスの底
部と同一方向に開口している。なお、前記ウイン
ドボツクスは適宜の接続手段、即ち、フランジ構
造6あるいはネジ構造にて脱着自在に燃焼用空気
供給管2に取付けられている。10は水冷壁であ
つて、燃焼室に位置する燃焼用供給管を包囲し、
水冷壁に連通した状態で設けられている。13は
燃焼用ブロワーであつて、ダンパーを介して燃焼
用空気供給管と連通して設けられている。9は燃
焼筒加熱バーナであつて、耐火壁を貫通して先端
が乾留ガス流れ下流側に向かつて開口するごとく
傾斜して設けられる。
Figure 2 is a sectional view of the combustion tube in the present invention;
The figure is a view taken along the - arrow in FIG. Reference numeral 7 in the drawing is the combustion chamber of the combustion tube, and the water cooling wall 8 on the upstream side
It is surrounded by a fireproof heat insulating wall 19 on the downstream side and formed into a cylindrical shape. The purpose of using a fireproof and insulating wall on the downstream side of the combustion chamber is to prevent the combustion flame from cooling and to ensure complete combustion. A combustion air supply pipe 2 is inserted from the outside of the combustion cylinder through the water-cooled wall, and its tip is located at the center of the combustion chamber and opens toward the downstream side in the flow direction A of the carbonized gas. Reference numeral 3 denotes a wind box made of a bottomed cylindrical member provided at the tip of the combustion air supply pipe, and the bottom portion S is disposed on the downstream side in the flow direction of the carbonized gas. This wind box 3 has a larger diameter than the combustion air supply pipe 2, and in this embodiment, it is set to have approximately the same outer diameter as a water cooling wall 10, which will be described later. Reference numeral 4 denotes a large number of air dispersion holes provided in the bottom S of the wind box with required dimensions. Reference numeral 5 denotes arc-shaped nozzles, which are provided in large numbers on the peripheral wall of the wind box in the same rotating direction.
The diameter of the nozzle is smaller than that of the wind box 3, and the opening is located approximately at the center of the wind box and the water cooling wall, opening in the same direction as the bottom of the wind box. The wind box is removably attached to the combustion air supply pipe 2 by a suitable connecting means, ie, a flange structure 6 or a screw structure. 10 is a water-cooled wall surrounding the combustion supply pipe located in the combustion chamber;
It is installed in communication with the water cooling wall. Reference numeral 13 denotes a combustion blower, which is provided in communication with the combustion air supply pipe via a damper. Reference numeral 9 denotes a combustion tube heating burner, which is provided so as to penetrate through the fireproof wall and be inclined so that its tip opens toward the downstream side of the flow of the carbonized gas.

次に上記構成の作用について説明する。まず、
乾留塔上部より被焼却物を所定量投入しておく。
又、乾留塔の水冷却壁や配熱ボイラーに水を所定
量供給しておく。次に予熱運転に入り、誘引フア
ンを稼働し、設定時間燃焼筒及び廃熱ボイラーの
プリパージを行つた後、燃焼筒に設けた加熱バー
ナを点火して燃焼筒の予熱を言う。燃焼温度が約
700℃に達した点で、乾留運転に移行する。乾留
運転においては誘引フアン・加熱バーナ稼動の状
態で燃焼用送風機を稼動し燃焼筒に乾留ガス燃焼
用の空気を供給するとともに除塵用送風機(図示
せず)を稼動して軸流サイクロンの抽気を開始し
たのち乾留塔下部点火口(図示せず)より、廃棄
物に点火する。ついで乾留用ブロワー(図示せ
ず)を稼動し、乾留用ノズルより空気を噴出して
乾留塔炉床部において燃焼を開始する。該燃焼熱
にて廃棄物は高温に加熱され熱分解を起して可燃
性の揮発分を発生する。この乾留ガスは燃焼筒に
入ると、燃焼用送風機からの二次空気と混合し、
完全燃焼を行い高温の燃焼ガスとなつて廃熱ボイ
ラーに至る。廃熱ボイラーで熱交換を行い低温と
なつた排ガスは軸流サイイクロンで除塵され煙突
より系外に排出される。燃焼筒の燃焼温度が約
900℃に達すれば加熱用のバーナを停止して定常
状態に移行する。廃棄物の乾留化が完了し炭燃焼
用送風機(図示せず)を稼動しても燃焼筒温度が
200℃以下に低下すると乾留運転を終了し廃棄物
の炭燃焼運転に移行する。即ち、炭燃焼用送風機
と乾留ブロワーを同時に稼動して炭燃焼を開始す
る。炭燃焼が完了すれば灰出部より残灰をかき出
す。以上の操作を例えば1日1回のサイクルで繰
返して行い、産業廃棄物を処理する。このとき、
ウインドボツクスの底部孔4の開口面積とノズル
部材5の開口面積が適度の比率に構成されてお
り、又ノズルによる空気旋回効果により乾留ガス
と空気が良好に混合し、低空気比で完全燃焼す
る。
Next, the operation of the above configuration will be explained. first,
A predetermined amount of material to be incinerated is introduced from the top of the carbonization tower.
Also, a predetermined amount of water is supplied to the water cooling wall of the carbonization tower and the heat distribution boiler. Next, preheating operation is started, the induction fan is operated, and the combustion tube and waste heat boiler are pre-purged for a set period of time, and then the heating burner installed in the combustion tube is ignited to preheat the combustion tube. The combustion temperature is approx.
When the temperature reaches 700℃, carbonization operation begins. During carbonization operation, a combustion blower is operated with the induction fan and heating burner in operation to supply air for carbonization gas combustion to the combustion tube, and a dust removal blower (not shown) is operated to extract air from the axial flow cyclone. After starting, the waste is ignited from the ignition port at the bottom of the carbonization tower (not shown). Next, a carbonization blower (not shown) is operated to blow out air from the carbonization nozzle to start combustion in the carbonization tower hearth. The waste is heated to a high temperature by the combustion heat, causing thermal decomposition and generating flammable volatile matter. When this carbonized gas enters the combustion tube, it mixes with secondary air from the combustion blower,
It undergoes complete combustion and becomes high-temperature combustion gas that reaches the waste heat boiler. The exhaust gas, which is cooled by heat exchange in the waste heat boiler, is removed by an axial cyclone and discharged out of the system through the chimney. The combustion temperature of the combustion tube is approximately
When the temperature reaches 900℃, the heating burner is stopped and the process returns to a steady state. Even after the carbonization of waste is completed and the charcoal combustion blower (not shown) is operated, the temperature of the combustion tube remains low.
When the temperature drops below 200℃, carbonization operation ends and waste charcoal combustion operation begins. That is, the charcoal combustion blower and carbonization blower are operated at the same time to start charcoal combustion. When charcoal combustion is completed, the remaining ash is scraped out from the ash outlet. The above operations are repeated, for example, once a day to treat industrial waste. At this time,
The opening area of the bottom hole 4 of the wind box and the opening area of the nozzle member 5 are configured at an appropriate ratio, and the carbonized gas and air are mixed well due to the air swirling effect of the nozzle, resulting in complete combustion at a low air ratio. .

更に、ウインドボツクス3は大径としてあるた
め、ウインドボツクス下流側での保炎が良好であ
り、更に、上記の空気旋回効果により、乾留ガス
の燃焼を短時間で、しかも安定して行うことがで
きる。
Furthermore, since the wind box 3 has a large diameter, flame holding on the downstream side of the wind box is good, and furthermore, due to the above-mentioned air swirling effect, carbonization gas can be combusted in a short time and stably. can.

〔考案の効果〕[Effect of idea]

本考案は上述のように構成されているので、下
記のような効果がある。
Since the present invention is configured as described above, it has the following effects.

(1) 燃焼室中心部へ空気を供給するウインドボツ
クスと燃焼室周壁部へ空気を供給するノズルと
を一体構造としたので、従来のように水冷壁内
にウインドボツクスを設けた構造に比べコンパ
クトで低コストで製造できる。
(1) The wind box that supplies air to the center of the combustion chamber and the nozzle that supplies air to the peripheral wall of the combustion chamber are integrated, making it more compact than the conventional structure in which the wind box is installed inside the water-cooled wall. can be manufactured at low cost.

(2) 燃焼用空気供給管とウインドボツクスとをフ
ランジあるいはネジ構造等の接続手段で脱着自
在に締結する構成とすることが可能となり、 a 不測の事態によりノズルが焼損した場合 b 廃棄物の構成が変動して乾留ガスの成分が
変つたため、供給空気量を変更する等、ウイ
ンドボツクスの底部孔とノズル孔の開口面積
や開口面積比の変更を要する場合 等に際しても非常に簡単に取替え変更すること
ができ、設備の休止期間を大幅に低減すること
ができる。
(2) It is now possible to connect the combustion air supply pipe and the wind box in a removable manner using a connecting means such as a flange or screw structure. It is very easy to replace and change when it is necessary to change the opening area or opening area ratio between the bottom hole of the wind box and the nozzle hole, such as changing the amount of air supplied due to fluctuations in the composition of the carbonized gas. This makes it possible to significantly reduce equipment downtime.

(3) 空気供給管の先端に設けるウインドボツクス
を、空気供給管より大径としたことにより、こ
のウインドボツクス下流側での保炎が良好とな
り、上記ノズルによる空気の旋回効果と相俟つ
て乾留ガスの燃焼を短時間で、しかも安定して
行える。
(3) By making the wind box installed at the tip of the air supply pipe larger in diameter than the air supply pipe, flame stability on the downstream side of the wind box is improved, and together with the air swirling effect from the nozzle mentioned above, carbonization is achieved. Gas can be burned in a short time and stably.

(4) 乾留ガスの燃焼を短時間で行えるため、燃焼
筒の長さをコンパクトにできるため、設備全体
としても小型化、省スペース化が図れる。
(4) Since the carbonized gas can be combusted in a short time, the length of the combustion tube can be made compact, making it possible to downsize and save space as a whole.

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

第1図は廃棄物焼却熱回収設備の構成図、第2
図は本考案における乾留塔下部の断面図、第3図
は第2図の−矢視図、第4図は従来の燃焼筒
の断面図、第5図は第4図の−矢視図であ
る。 1……燃焼筒、2……燃焼用空気供給管、3…
…ウインドボツクス、4……孔、5……円弧状の
ノズル、6……フランジ構造(接続手段)7……
燃焼室、8……水冷壁、9……加熱バーナ、10
……水冷管、11……ウインドボツクス、12…
…ノズル、13……燃焼用ブロワー、14……乾
留塔、15……廃熱ボイラー、16……軸流サイ
クロン、17……誘引フアン、18……煙突、1
9……耐火断熱壁。
Figure 1 is a configuration diagram of waste incineration heat recovery equipment, Figure 2
The figure is a cross-sectional view of the lower part of the carbonization tower in the present invention, FIG. 3 is a view taken in the direction of the − arrow in FIG. 2, FIG. 4 is a cross-sectional view of a conventional combustion tube, and FIG. be. 1... Combustion tube, 2... Combustion air supply pipe, 3...
... Wind box, 4 ... Hole, 5 ... Arc-shaped nozzle, 6 ... Flange structure (connection means) 7 ...
Combustion chamber, 8...Water cooling wall, 9...Heating burner, 10
...Water cooling pipe, 11...Wind box, 12...
... Nozzle, 13 ... Combustion blower, 14 ... Carbonization tower, 15 ... Waste heat boiler, 16 ... Axial flow cyclone, 17 ... Induction fan, 18 ... Chimney, 1
9... Fireproof insulation wall.

Claims (1)

【実用新案登録請求の範囲】 (1) 廃棄物から得た乾留ガスを燃焼する燃焼筒1
において、 先端が燃焼筒1中心部にあつて、乾留ガス流
れ方向A下流側に開口する燃焼用空気供給管2
を設け、 この供給管2先端に、供給管2より大径の有
底筒状部材からなるウインドボツクス3を、そ
の底部Sが乾留ガス流れ方向A下流側に位置す
るように、接続手段6を介して脱着自在に設
け、 上記ウインドボツクス底部Sに、空気分散用
の孔4を多数個穿設すると共に、ウインドボツ
クス周囲に、ウインドボツクス3より小径のノ
ズル部材5を同一旋回方向に多数配設したこと
を特徴とする廃棄物焼却熱回収設備における燃
焼筒の空気供給装置。 (2) 前記円弧状のノズル5の開口部がウインドボ
ツクスの底部Sと同一方向に設けられることを
特徴とする実用新案登録請求の範囲第1項記載
の廃棄物焼却熱回収設備における燃焼筒の空気
供給装置。
[Scope of claim for utility model registration] (1) Combustion tube 1 for burning carbonized gas obtained from waste
, a combustion air supply pipe 2 whose tip is located at the center of the combustion tube 1 and opens downstream in the carbonization gas flow direction A;
A wind box 3 made of a bottomed cylindrical member having a diameter larger than that of the supply pipe 2 is installed at the tip of the supply pipe 2, and a connecting means 6 is connected so that the bottom S of the wind box 3 is located on the downstream side in the carbonization gas flow direction A. A large number of air dispersion holes 4 are bored in the bottom S of the wind box, and a large number of nozzle members 5 having a smaller diameter than the wind box 3 are arranged around the wind box in the same rotation direction. An air supply device for a combustion cylinder in a waste incineration heat recovery facility, characterized by: (2) The combustion tube in the waste incineration heat recovery equipment according to claim 1 of the registered utility model, characterized in that the opening of the arc-shaped nozzle 5 is provided in the same direction as the bottom S of the wind box. Air supply device.
JP1986015199U 1986-02-03 1986-02-03 Expired JPH0245620Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1986015199U JPH0245620Y2 (en) 1986-02-03 1986-02-03

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1986015199U JPH0245620Y2 (en) 1986-02-03 1986-02-03

Publications (2)

Publication Number Publication Date
JPS62131237U JPS62131237U (en) 1987-08-19
JPH0245620Y2 true JPH0245620Y2 (en) 1990-12-03

Family

ID=30805909

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1986015199U Expired JPH0245620Y2 (en) 1986-02-03 1986-02-03

Country Status (1)

Country Link
JP (1) JPH0245620Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2678162B2 (en) * 1990-12-22 1997-11-17 前田建材工業株式会社 Pyrolysis gasification combustion device
JP2660643B2 (en) * 1992-08-20 1997-10-08 有限会社鳥島製作所 Air supply nozzle for incinerator

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5517054A (en) * 1978-07-20 1980-02-06 Toei Shoko Kk Burning waste product and incinerator
JPS5652132B2 (en) * 1979-05-24 1981-12-10

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5652132U (en) * 1979-09-22 1981-05-08

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5517054A (en) * 1978-07-20 1980-02-06 Toei Shoko Kk Burning waste product and incinerator
JPS5652132B2 (en) * 1979-05-24 1981-12-10

Also Published As

Publication number Publication date
JPS62131237U (en) 1987-08-19

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