JPH0799255B2 - Incinerator - Google Patents

Incinerator

Info

Publication number
JPH0799255B2
JPH0799255B2 JP1192401A JP19240189A JPH0799255B2 JP H0799255 B2 JPH0799255 B2 JP H0799255B2 JP 1192401 A JP1192401 A JP 1192401A JP 19240189 A JP19240189 A JP 19240189A JP H0799255 B2 JPH0799255 B2 JP H0799255B2
Authority
JP
Japan
Prior art keywords
side wall
front side
furnace
air
wall
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 - Lifetime
Application number
JP1192401A
Other languages
Japanese (ja)
Other versions
JPH0355414A (en
Inventor
清治 道前
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
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP1192401A priority Critical patent/JPH0799255B2/en
Publication of JPH0355414A publication Critical patent/JPH0355414A/en
Publication of JPH0799255B2 publication Critical patent/JPH0799255B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、ごみ、その他廃棄物の焼却炉に関する。TECHNICAL FIELD The present invention relates to an incinerator for refuse and other waste.

〔従来の技術〕[Conventional technology]

従来、焼却炉は、一般的に、第1図に示すように、炉壁
が全周に亘って垂直であって、上端または上端側部に焼
却物の投入口があった。また、炉壁の下端部には空気吹
込孔を設け、その吹込孔を水平に形成されることが多か
った。
Conventionally, as shown in FIG. 1, in general, incinerators have a furnace wall which is vertical over the entire circumference and has an inlet for incineration at the upper end or the upper end side portion. Further, an air blowing hole is often provided at the lower end of the furnace wall, and the blowing hole is often formed horizontally.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

従来の焼却炉は、上記のように炉壁が全周に亘って垂直
に起立した構造であると、焼却物を炉に投入した場合、
炉の真中の位置において焼却物が量的に密となるのに対
して、炉壁に沿った位置においては粗となり、粗の部分
で空気の流通が良好であるために、焼却物が炉壁に近い
部分で効率的に燃焼し、真中の燃焼が悪く、真中に未燃
焼物が残るために焼却効率が悪かった。
When the conventional incinerator has a structure in which the furnace wall is erected vertically over the entire circumference as described above, when the incinerator is put into the furnace,
The incinerator becomes dense in quantity in the middle position of the furnace, whereas it becomes coarse in the position along the furnace wall, and the air flow is good in the rough part, so Burned efficiently in the area close to, the combustion in the middle was bad, and the incineration efficiency was poor because unburned material remained in the middle.

また、焼却物が非常に燃焼しやすい等の原因で燃焼熱が
高い場合には、高温燃焼のために灰が溶融し、残滓取出
し時にそれが固結している関係で取出し作業が困難とな
り、また、炉壁や炉床が溶けて傷み、炉の補修が多くな
るという問題があった。
Also, if the combustion heat is high due to the fact that the incinerated material is extremely easy to burn, etc., the ash melts due to high temperature combustion, and it becomes difficult to take out due to the fact that it is solidified when removing the residue, Further, there is a problem that the furnace wall and the furnace floor are melted and damaged, and the repair of the furnace increases.

この発明は、上記のような実情に鑑みて、焼却物を平均
して燃焼させることができ、また、炉内が高温となって
も、灰が溶融したり、炉壁が溶けて傷んだりすることの
ない焼却炉を提供することを目的としたものである。
In view of the above situation, the present invention can burn incinerators evenly, and even if the temperature inside the furnace becomes high, the ash melts or the furnace wall melts and is damaged. The purpose is to provide a unique incinerator.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記の目的を達成するために、この発明は、炉の前側壁
を前方へゆくにつれて高くなる前傾斜に形成し、炉の後
側壁を起立した下半壁と前へ傾斜する上半壁で形成し、
且つ、上記前側壁の上端に、前側壁の傾斜に沿って上昇
する燃焼ガスが筒抜け状に排出されることにより、後側
壁に沿って流下する燃焼空気の取込み口ともなる燃焼物
の投入口を斜め横向きに設け、前側壁の下端部には、補
助的に空気を取り入れる吹込孔を下向き吹込み傾斜に設
け、炉床の下に冷却のために冷媒の流通路を設けて焼却
炉を構成した。
In order to achieve the above object, the present invention forms a front side wall of a furnace with a front slope that increases as it goes forward, and forms a rear side wall of the furnace with a standing lower half wall and an upper half wall that slopes forward.
Further, at the upper end of the front side wall, the combustion gas rising along the slope of the front side wall is exhausted in a hollow cylinder shape, so that a combustion material input port that also serves as an intake port for the combustion air flowing down along the rear side wall is provided. It was installed diagonally sideways, and at the lower end of the front side wall, a blow-in hole for auxiliary air intake was provided in a downward blow-inclination, and a cooling medium flow passage was provided under the hearth to construct an incinerator. ..

〔作用〕[Action]

上記の構成によれば、投入口が斜め横向きであるため、
真上向きである場合に比して空気が吸引されやすく、ま
た、後側壁の上半壁の傾斜面で吸引空気が誘導されるた
め、吸引空気は後側壁に沿って下降する。
According to the above configuration, since the inlet is diagonally sideways,
Air is more easily sucked than when the air is directed straight up, and since the suction air is guided by the inclined surface of the upper half wall of the rear side wall, the suction air descends along the rear side wall.

そして、投入口より焼却物を投入すると、前側壁の傾斜
に沿って落下し、その傾斜に沿って積み上げられ、焼却
物の荷重が前側壁に寄り掛かるために、炉内においては
焼却物が第2図に示すように、前部において密、後部に
おいて粗となり、しかも、前側壁と焼却物との間に少し
の隙間が生じる。
Then, when the incinerated matter is introduced from the charging port, it falls along the slope of the front side wall and is piled up along the slope, and the load of the incinerated matter leans on the front side wall, so that the incinerated matter is the first in the furnace. As shown in FIG. 2, the front part is dense and the rear part is rough, and a small gap is generated between the front side wall and the incinerated material.

そこで、焼却物を燃焼させた場合には、前部における燃
焼の火力によって、燃焼ガスが前側壁の傾斜に沿って上
昇し投入口より排出され、それとは逆に後部において
は、燃焼ガスの排出に伴う吸引作用により、投入口から
空気(酸素)が吸引されて下降しつつ焼却物を燃焼さ
せ、下端に至った空気は、上昇に転じて前側壁の傾斜に
沿って上昇しつつ焼却物を燃焼させる。
Therefore, when the incinerated matter is burned, the combustion gas in the front part raises the combustion gas along the slope of the front side wall and is discharged from the charging port, while the combustion gas is discharged in the rear part. Due to the suction action accompanying with, the air (oxygen) is sucked from the input port and burns the incinerated matter while descending, and the air reaching the lower end turns to rise and rises along the slope of the front side wall to remove the incinerated matter. To burn.

そこで、このような構造の焼却炉においては、強制的な
空気の吹込みの場合とは違って、炉内においては、焼却
物の燃焼に応じた熱に比例的に空気の吸引および対流が
生じ、燃焼に必要な空気のみの反応となる。そこで、加
速度的に非常な高温燃焼となり、このままでは、灰の溶
融が生じるばかりでなく、特に炉床の溶融をも生じる恐
れがあるが、炉床が冷媒の流通によって冷却されるため
に、これらの溶融現象を防止できる。
Therefore, in an incinerator having such a structure, unlike in the case of forced air blowing, air suction and convection occur in proportion to the heat corresponding to the combustion of the incineration product in the furnace. , Only the air required for combustion reacts. Therefore, it becomes an extremely high temperature combustion at an accelerating rate, and if it is left as it is, not only melting of ash but also melting of the hearth may occur, but since the hearth is cooled by the circulation of the refrigerant, these The melting phenomenon can be prevented.

なお、炉床だけの冷却でも、上昇ガスが冷却されるため
に、前側壁の溶融も同時に防止できるが、より安全のた
めには、前側壁にも冷却装置を設けることが望ましい。
Even if only the hearth is cooled, the rising gas is cooled, so melting of the front side wall can be prevented at the same time. However, for safety, it is desirable to provide a cooling device also on the front side wall.

一方、火力による自然流によって、投入口からの空気の
吸引現象が生じることから、空気吹込孔からの空気の吹
込みは、燃焼が自然に行われるようになってからは必ず
しも要しないのであるが、焼却物の質等が原因でその燃
焼が特に悪いというような場合には、自然流を強制流に
切替えることにより、燃焼効率を上昇させることができ
る。
On the other hand, since a natural flow due to thermal power causes a suction phenomenon of air from the charging port, blowing air from the air blowing hole is not always necessary after combustion is naturally performed. When the combustion is particularly bad due to the quality of the incineration material, the combustion efficiency can be increased by switching the natural flow to the forced flow.

次に、吹込孔と前側壁との関係を第3図において説明す
ると、吹込孔が下向き傾斜であるため、吹込孔より空気
が勢い良く吹き込まれると、その空気が炉床や反対側の
側壁に当たって反転気流が生じ、その反転気流が焼却物
の密な前部(〔I〕ゾーン)において前側壁の傾斜に沿
って焼却物内を上昇し、特に、焼却物と前側壁との間の
隙間を上昇することによって、焼却物は急速に燃焼され
るので、粗である〔II〕ゾーンと同じ状態が望める。
Next, the relationship between the blow hole and the front side wall will be described with reference to FIG. 3. Since the blow hole is inclined downward, when the air is blown from the blow hole with force, the air hits the hearth and the side wall on the opposite side and is inverted. An airflow is generated, and the reversal airflow rises in the incineration product along the slope of the front side wall in the dense front part ([I] zone) of the incineration product, and particularly in the gap between the incineration product and the front side wall. By doing so, the incineration is burned rapidly, and the same condition as in the coarse [II] zone can be expected.

これによれば、燃焼し難い部分より空気を吹込むことに
より、平均的に燃焼を行うことができる。これを仮に反
対より吹き込むと、〔I〕ゾーンが残り〔II〕ゾーンが
空になって空気の未利用が発生し、燃焼効率が低下す
る。
According to this, the air can be blown from the portion that is difficult to burn, so that the burning can be performed on average. If this is blown in from the opposite side, the [I] zone remains and the [II] zone is emptied, resulting in unused air and lowering combustion efficiency.

なお、空気は焼却物に均等に及ぶことが望ましいから、
空気吹込孔は、炉の左右巾の真中に設けることによっ
て、燃焼効率に最大効果を発揮する。また、炉の左右巾
が特に広い場合には間隔おきに複数の吹込孔を設ける。
In addition, since it is desirable that the air spreads over the incineration evenly,
The air injection hole is provided in the center of the width of the furnace to maximize the combustion efficiency. If the width of the furnace is wide, a plurality of blow holes are provided at intervals.

前側壁の傾斜角度αは、(第4図に示すように)水平線
に対して30°までが望ましく、それ以下の緩い傾斜であ
ると対流現象が生じ難い。
The inclination angle α of the front wall is preferably up to 30 ° with respect to the horizontal line (as shown in FIG. 4), and if the inclination is less than 30 °, the convection phenomenon hardly occurs.

また、吹込孔の下向き傾斜角度βについては、水平線か
ら80°までが望ましく、それよりも急傾斜にすると、空
気の反転現象が生じ難い。
Further, the downward inclination angle β of the blow hole is preferably 80 ° from the horizontal line, and if the inclination angle is steeper than that, the inversion phenomenon of air is unlikely to occur.

また、前側壁の反対側の後側壁も傾斜させるが、その角
度は垂直線に対して前後それぞれ最大限30°程度が望ま
しい。
Further, the rear side wall opposite to the front side wall is also inclined, but the angle is preferably about 30 ° at the front and the rear with respect to the vertical line.

また、この発明の焼却炉の構造の利点は、第5図に示す
ように、炉内が幾つもの機能に分担されることである。
Further, an advantage of the structure of the incinerator according to the present invention is that the inside of the furnace is divided into several functions as shown in FIG.

〔実施例〕〔Example〕

次に、この発明の実施例を説明する。 Next, an embodiment of the present invention will be described.

第6図は一実施例を示したもので、その焼却炉は、前側
壁1、後側壁2、左右側壁3、3および炉床4とから構
成され、上端に焼却物の投入口5を有する。
FIG. 6 shows an embodiment, and the incinerator is composed of a front side wall 1, a rear side wall 2, left and right side walls 3, 3 and a hearth 4, and has an incinerator inlet 5 at the upper end. .

前側壁1は、前へ傾斜しその下端部に空気吹込孔6が炉
床4に向かって斜めに形成してある。
The front side wall 1 is inclined forward and an air blowing hole 6 is formed obliquely toward the hearth 4 at a lower end portion thereof.

後側壁2は、起立した下半壁2aと前へ傾斜する上半壁2b
とからなり、上半壁2bは、前側壁1よりも少し多い傾斜
角度に形成される。
The rear side wall 2 includes a standing lower half wall 2a and an upper half wall 2b inclined forward.
And the upper half wall 2b is formed with an inclination angle slightly larger than that of the front side wall 1.

前側壁1と後側壁2の上端には前方へ水平に突出する鍔
部10、11を形成し、両鍔部10、11の先端が投入口5の蓋
が当たりやすいように同一角度の斜面に形成してある。
Collar portions 10 and 11 that horizontally project forward are formed at the upper ends of the front side wall 1 and the rear side wall 2, and the tip ends of both the flange portions 10 and 11 are formed into slopes of the same angle so that the lid of the inlet 5 can easily hit. Has been formed.

投入口5は、前側壁1の傾斜面上方に位置し、斜め横向
きの投入角度に形成されている。そこで、投入口5より
焼却物を投入すると、焼却物が前側壁1の斜面に沿って
滑り落ち、前側壁1に寄り掛かって積み上げられる結
果、前部が密、後部が粗となる。
The charging port 5 is located above the inclined surface of the front side wall 1 and is formed at an obliquely horizontal charging angle. Then, when the incinerated matter is thrown in through the charging port 5, the incinerated matter slides down along the slope of the front side wall 1 and leans on the front side wall 1 to be piled up. As a result, the front part becomes dense and the rear part becomes rough.

また、投入口5が斜め横向きであるため、真上向きであ
る場合に比して空気が吸引されやすく、また、後側壁2
の上半壁2bの傾斜面で吸引空気が誘導されるため、吸引
空気は後側壁2に沿って下降する。
Further, since the charging port 5 is obliquely laterally oriented, air is more easily sucked in than when the charging port 5 is directly upward, and the rear side wall 2 is also provided.
Since the suction air is guided by the inclined surface of the upper half wall 2b, the suction air descends along the rear side wall 2.

炉床4は、鉄板によって中空に形成され、内部に冷水の
流通路12がその中空によって設けられている。
The hearth 4 is formed in a hollow shape by an iron plate, and a cold water flow passage 12 is provided in the inside thereof.

第7図は、炉床4の他の例を示したもので、コンクリー
トの基礎床13に突条14、14、…を等間隔に設け、突条1
4、14…の上に鉄板15を載せることによって、突条14、1
4間に空気の流通路12を設けてある。
FIG. 7 shows another example of the hearth floor 4, in which the ridges 14, 14, ...
By placing the iron plate 15 on 4, 14, ...
An air passage 12 is provided between the four.

〔発明の効果〕〔The invention's effect〕

以上説明したように、この発明によれば、炉の前側壁を
前方へゆくにつれて高くなる前傾斜に形成し、炉の後側
壁を起立した下半壁と前へ傾斜する上半壁で形成し、且
つ、上記前側壁の上端に、前側壁の傾斜に沿って上昇す
る燃焼ガスが筒抜け状に排出されることにより、後側壁
に沿って流下する燃焼空気の取込み口ともなる燃焼物の
投入口を斜め横向きに設けたこの構造では、前部に焼却
物が密に堆積し、後部が粗となることから、投入口から
空気が後部に吸引され前部で上昇して投入口から排出さ
れる対流現象が生じると、その自然対流によって焼却物
が均等に燃焼し、その効率が非常に良好であるという優
れた効果がある。
As described above, according to the present invention, the front side wall of the furnace is formed to have a forward slope that becomes higher as it goes forward, and the rear side wall of the furnace is formed by the standing lower half wall and the upper half wall that slopes forward, and At the upper end of the front side wall, the combustion gas that rises along the slope of the front side wall is discharged like a cylinder so that the combustion material inlet, which also serves as an inlet for the combustion air flowing down along the rear side wall, is slanted. With this structure installed horizontally, the incinerated matter is densely accumulated in the front part and the rear part becomes rough, so that air is sucked from the inlet to the rear and rises in the front and is discharged from the convection phenomenon. When this occurs, there is an excellent effect that the incineration material burns uniformly due to the natural convection and the efficiency is very good.

また、投入口が斜め横向きであるため、真上向きである
場合に比して空気が吸引されやすく、また、後側壁の上
半壁の傾斜面で吸引空気が誘導されるため、吸引空気は
後側壁に沿って下降する。
In addition, since the inlet is diagonally sideways, air is more easily sucked in than when it is right above, and because the suction air is guided by the inclined surface of the upper half wall of the rear wall, the suction air is Descend along.

さらに、燃焼効率が良好なことによって、高温となって
も炉床が冷却されるために、灰が溶融して残滓の取出し
が困難になったり、炉が溶けて傷むという不都合を防止
できる。
Further, since the combustion efficiency is good, the hearth is cooled even when the temperature becomes high, so that it is possible to prevent inconveniences that the ash is melted and it is difficult to take out the residue, and the furnace is melted and damaged.

なお、場合によっては、燃焼をより確実に行なうため
に、あえて燃焼物の溶融を伴なわせる場合もあるが、そ
のときも、本発明焼却炉にあっては、その炉の構造から
して、溶融が発生する条件を充分に備えており、かえっ
て、残滓を溶融しスラグ化することは、従来の他の焼却
炉よりは非常に簡単になし得るのである。
In some cases, in order to perform the combustion more reliably, it may be intentionally accompanied by melting of the combusted material, but even then, in the incinerator of the present invention, from the structure of the furnace, It is equipped with sufficient conditions for melting, and rather, melting and slagging the residue can be made much easier than other conventional incinerators.

また、必要があれば空気吹込孔からの空気の吹込みによ
り、自然流を強制流に切替えて燃焼速度の向上を図るこ
とができる。
Further, if necessary, by blowing air from the air blowing hole, the natural flow can be switched to the forced flow to improve the combustion speed.

また、本発明の焼却炉を、例えば産業廃棄物用の一連の
焼却システムの末端に設備すれば、未燃物の発生を完全
に防止することができ、加えて、それを溶融されること
も可能であり、この溶融により残滓の無害化を図ること
ができるとともに、残滓の量的減少にも役立つという、
優れた効果も有する。
Also, if the incinerator of the present invention is installed at the end of a series of incinerator systems for industrial waste, for example, it is possible to completely prevent the generation of unburned substances, and in addition, it is possible to melt it. It is possible, and by melting this residue, it is possible to make the residue harmless, and it also helps to reduce the amount of the residue.
It also has excellent effects.

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

第1図は従来例の説明図である。 第2図ないし第5図はこの発明の説明図であって、その
うち第2図、第3図、第5図は炉の機能の説明図、第4
図は炉前側壁および吹込孔の説明図である。 第6図は本発明実施例炉を側面から見た縦断面図、第7
図は炉床の別の実施例の断面図である。 1……前側壁、2……後側壁、4……炉床、5……投入
口、6……吹込孔、12……冷媒の流通路
FIG. 1 is an explanatory diagram of a conventional example. 2 to 5 are explanatory views of the present invention, of which FIG. 2, FIG. 3 and FIG. 5 are explanatory views of the function of the furnace, and FIG.
The figure is an explanatory view of the front wall of the furnace and the blowing hole. FIG. 6 is a vertical cross-sectional view of the furnace of the present invention as seen from the side,
The figure is a cross-sectional view of another embodiment of the hearth. 1 ... Front side wall, 2 ... Rear side wall, 4 ... Hearth, 5 ... Input port, 6 ... Injection hole, 12 ... Refrigerant flow passage

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】炉の前側壁を前方へゆくにつれて高くなる
前傾斜に形成し、炉の後側壁を起立した下半壁と前へ傾
斜する上半壁で形成し、且つ、上記前側壁の上端に、前
側壁の傾斜に沿って上昇する燃焼ガスが筒抜け状に排出
されることにより、後側壁に沿って流下する燃焼空気の
取込み口ともなる燃焼物の投入口を斜め横向きに設け、
前側壁の下端部には、補助的に空気を取り入れる吹込孔
を下向き吹込み傾斜に設け、炉床の下に冷却のために冷
媒の流通路を設けたことを特徴とする焼却炉。
1. A front side wall of the furnace is formed to have a front slope that becomes higher as it goes forward, and a rear side wall of the furnace is formed by a standing lower half wall and an upper half wall that slopes forward, and at the upper end of the front side wall. , The combustion gas rising along the slope of the front side wall is discharged in a tubular shape, so that a combustion material inlet, which also serves as an inlet for the combustion air flowing down along the rear side wall, is provided obliquely sideways,
An incinerator characterized in that a blow hole for supplementarily taking in air is provided at a lower end of the front side wall at a downward blow slope, and a refrigerant flow passage is provided under the furnace floor for cooling.
JP1192401A 1989-07-25 1989-07-25 Incinerator Expired - Lifetime JPH0799255B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1192401A JPH0799255B2 (en) 1989-07-25 1989-07-25 Incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1192401A JPH0799255B2 (en) 1989-07-25 1989-07-25 Incinerator

Publications (2)

Publication Number Publication Date
JPH0355414A JPH0355414A (en) 1991-03-11
JPH0799255B2 true JPH0799255B2 (en) 1995-10-25

Family

ID=16290701

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1192401A Expired - Lifetime JPH0799255B2 (en) 1989-07-25 1989-07-25 Incinerator

Country Status (1)

Country Link
JP (1) JPH0799255B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5233912B2 (en) * 2009-08-28 2013-07-10 株式会社Ihi Fine powder combustion test equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55110928U (en) * 1979-01-27 1980-08-04
JPS6134045A (en) * 1984-07-27 1986-02-18 Japan Synthetic Rubber Co Ltd Thermoplastic resin composition

Also Published As

Publication number Publication date
JPH0355414A (en) 1991-03-11

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