JPH0619944Y2 - Wet solid continuous incinerator - Google Patents
Wet solid continuous incineratorInfo
- Publication number
- JPH0619944Y2 JPH0619944Y2 JP2128289U JP2128289U JPH0619944Y2 JP H0619944 Y2 JPH0619944 Y2 JP H0619944Y2 JP 2128289 U JP2128289 U JP 2128289U JP 2128289 U JP2128289 U JP 2128289U JP H0619944 Y2 JPH0619944 Y2 JP H0619944Y2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- wet solid
- air supply
- supply port
- air
- 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
Links
Landscapes
- Incineration Of Waste (AREA)
Description
【考案の詳細な説明】 （産業上の利用分野） この考案は湿潤固型物連続焼却炉に係りその目的は芝、
剪定処理木材、厨芥、台所の生ごみ等高発熱量から低発
熱量の焼却物を連続して無煙で燃焼させることができる
湿潤固型物連続焼却炉の提供にある。[Detailed Description of the Invention] (Industrial field of application) This invention relates to a wet solid continuous incinerator whose purpose is turf,
It is to provide a wet solid continuous incinerator capable of continuously burning smokeless materials such as pruned wood, kitchen waste and kitchen garbage with high to low calorific value without smoke.
（従来技術） ゴルフ場の刈り取った芝や庭木等の剪定後の処理木材或
いは台所の生ごみ等は水分を多量に含むためこれを燃焼
処理するに際しては、バッチ投入による直接燃焼は大変
むづかしかった。(Prior Art) Directly burned by batch feeding is very difficult when burning wood such as mowed grass and garden trees after pruning, wood or kitchen garbage, which contains a large amount of water. It was
従って、これらを何らかの方法で、例えば天然乾燥或い
は、加熱乾燥等の手段で、予め乾燥させた後定量供給し
て燃焼させるか或いは、他の非常に燃焼しやすい油、合
成樹脂等と混合して定量供給しながら燃焼させる等の方
法が採用されていた。Therefore, these are dried in advance by a certain method, for example, by means of natural drying or heat drying, and then fed in a fixed amount and burned, or mixed with other extremely combustible oil, synthetic resin or the like. The method of burning while supplying a fixed amount was adopted.
しかしながら、従来のこのような燃焼方法或いは燃焼装
置においてはまず湿潤固型物を、乾燥させるため、天日
で乾燥させようとすると、その乾燥に時間が多量に要す
るうえ、その乾燥作業のための場所が必要であり又定量
供給する等欠点があった。However, in such a conventional combustion method or combustion apparatus, since the wet solid matter is first dried, if it is attempted to be dried in the sun, it takes a lot of time to dry it, and the There were drawbacks such as the need for space and the constant supply.
熱風乾燥等の手法を取り入れると成程効率的に乾燥を処
理することができるが、本来、焼却処理をするものに乾
燥手間やコストを余分にかけ定量供給装置を設けること
は望ましくなく、結局いづれの方法も望ましくない。Although it is possible to process the drying as efficiently as possible by incorporating a method such as hot air drying, it is originally not desirable to provide a constant quantity supply device for the incineration process with extra drying labor and cost, and eventually The method is also undesirable.
更に、台所の生ごみ等は天然天日乾燥であっても或いは
熱風乾燥であっても、乾燥時にごみ臭が周囲に飛散する
等問題があり、更に乾燥工程を除去して他の燃焼しやす
い燃焼物の混合や或いは他の、助燃剤を混合させて燃焼
する場合でも、燃焼の際に、悪臭が発生する欠点は避け
られず、更に水分が焼却効率を低下させて助燃油の消費
量が多くなる等の欠点があった。In addition, kitchen garbage, whether natural sun-dried or hot-air dried, has a problem that dust odors are scattered around during drying, and it is easy to burn by removing the drying process. Even when the combustion products are mixed or other combustion aids are mixed and burned, the disadvantage that a bad odor is generated during combustion is unavoidable, and the moisture further reduces the incineration efficiency, resulting in the consumption of the supplementary fuel oil. There were drawbacks such as increasing the number.
（考案の解決課題） この考案は、貯留部に含水率の高い湿潤芝剪定処理木材
や厨芥等を単に貯留して燃焼部で燃焼するだけで燃焼と
乾燥を同時に且つ連続的に行ないしかも煙を発生させる
ことがない湿潤固型物連続焼却炉を創出せんとしたもの
である。(Problem to be solved by the device) This device is capable of simultaneously and continuously performing combustion and drying by simply storing the moist turf pruning treated wood or kitchen waste having a high water content in the storage portion and burning it in the combustion portion. The idea was to create a wet solid continuous incinerator that does not generate.
（課題を解決するための手段） すなわち、この考案は、有蓋中空筒状の貯留部とこの貯
留部に連続連結された有底中空筒状の燃焼部とからな
り、この燃焼部は上部の特定箇所全周が断面くの字状に
絞られて狭絞部とされ少なくとも空気供給口がこの狭絞
部の上斜面に形成されこの空気供給口は狭絞部上斜線
（）に直交する角度で空気が噴射する様に設けられこ
の狭絞部の上斜線（）と垂直線(v)とがなす角（θ）
は30〜60°とされてなり、燃焼部下部に助燃バーナーが
設けられると共に助燃バーナーの対向位置に煙道が設け
られてなる湿潤固型物連続焼却炉を提供することにより
中間に火格子等を設けることなく上記欠点を悉く解消す
ることに成功した。(Means for Solving the Problem) That is, the present invention is composed of a hollow hollow cylindrical storage part with a lid and a bottomed hollow cylindrical combustion part continuously connected to this storage part. The whole circumference is narrowed in a V shape in cross section to form a narrowed portion, and at least an air supply port is formed on the upper slope of this narrowed portion. This air supply port is at an angle orthogonal to the upper slanted line () of the narrowed portion. The angle (θ) formed by the oblique line () and the vertical line (v) that is provided so that air is jetted.
Is 30 to 60 °, and an auxiliary combustion burner is installed in the lower part of the combustion section, and a flue is installed opposite to the auxiliary combustion burner. We have succeeded in eliminating the above drawbacks without providing.
（考案の構成） 以下この考案の構成を第１図乃至第５図に基づいて詳細
に説明する。(Configuration of the Invention) The configuration of the invention will be described in detail below with reference to FIGS. 1 to 5.
第１図に於いて、(1)は蓋(2)をその頂部に設けた中空筒
状の貯留部で、(3)は燃焼部で、この燃焼部(3)はその上
部に狭絞部(4)を有している。In FIG. 1, (1) is a hollow cylindrical storage part provided with a lid (2) on its top, (3) is a combustion part, and this combustion part (3) is a narrowing part at its upper part. It has (4).
この狭絞部(4)は断面くの字状で中空筒状の燃焼部(3)の
上部の特定箇所に且つ全周に形成されている。The narrowed portion (4) is formed in a specific location on the upper portion of the hollow tubular combustion portion (3) having a V-shaped cross section and over the entire circumference.
(5)は燃焼下部に形成された助燃バーナーで、(6)はこの
助燃バーナーの対向位置に設けられた煙道である。(5) is an auxiliary combustion burner formed in the lower part of combustion, and (6) is a flue provided at a position facing the auxiliary combustion burner.
この狭絞部(4)の上斜線（）と垂直線(v)とがなす角
（θ）は30〜60°とされている。The angle (θ) formed by the upper diagonal line () and the vertical line (v) of the narrowed portion (4) is 30 to 60 °.
(7)は空気供給口で、この空気供給口(7)は少なくとも狭
絞部(4)の上斜面(4a)に設けられている。(7) is an air supply port, and this air supply port (7) is provided at least on the upper slope (4a) of the narrowed portion (4).
尚、下斜面(4b)に空気供給口(8)が、図示する実施例に
於いては設けられている。An air supply port (8) is provided on the lower slope (4b) in the illustrated embodiment.
更に燃焼部(3)の底(9)にも空気供給口(10)が形成されて
いる。Furthermore, an air supply port (10) is formed in the bottom (9) of the combustion section (3).
この考案に於いては少なくとも狭絞部(4)の上斜面(4a)
に空気供給口(7)が設けられることが望ましく他の空気
供給口(8)，(10)は有ればより望ましい。In this invention, at least the upper slope (4a) of the narrowed portion (4)
It is desirable that the air supply port (7) is provided in the other, and it is more desirable if the other air supply ports (8) and (10) are provided.
このような構成からなる湿潤固型物連続焼却炉は、まず
第２図に示す蓋(2)を開放し、この蓋(2)の開放部から芝
或いは剪定木材等の湿潤固型物(11)を一度に上部まで多
量に供給貯留し蓋(2)を閉める。In the wet solid continuous incinerator having such a structure, first, the lid (2) shown in FIG. 2 is opened, and the wet solid (11) such as grass or pruned wood is opened from the opening of the lid (2). ) Is supplied and stored in large amounts up to the upper part at a time, and the lid (2) is closed.
この湿潤固型物(11)は狭絞部(4)の内周面(4a)にて供給
され、貯留物(11)の荷重を受けるが狭絞部(4)のため焼
却物(11)はこの部分でブリッジ現象が起こり燃焼部(12)
にある焼却物(11)には供給貯留物の荷重がかからない。This wet solid matter (11) is supplied by the inner peripheral surface (4a) of the narrowed portion (4) and receives the load of the stored material (11), but because of the narrowed portion (4) the incinerated material (11) The bridge phenomenon occurs in this part and the combustion part (12)
The incineration (11) at is not loaded by the supply reservoir.
燃焼室(12)で燃えている熱により狭絞部(4)の焼却物(1
1)は乾燥され、空気ノズル孔(7)より噴出する空気によ
り、狭絞部(4)の焼却物(11)は燃える。Due to the heat burning in the combustion chamber (12), the incineration (1
1) is dried and the air ejected from the air nozzle hole (7) burns the incinerated material (11) in the narrowed portion (4).
この時、場所(11b)の焼却物(11)は灰となり結果、焼却
物(11)の体積減少が起こり狭絞部(4)で焼却物(11)のブ
リッジ(11c)を支えていた部分(11b)が落下するために、
貯蔵槽(1)の焼却物(11)は燃焼室(12)で燃焼減量した分
だけ、自然落下力で下(11a)方向から順次下る。この現
象の繰り返し作用で貯蔵槽(1)にある焼却物(11)を定量
づつ乾燥、燃焼、落下を繰り返すのである。At this time, the incinerated matter (11) in the place (11b) turns into ash, resulting in a decrease in the volume of the incinerated matter (11) and the portion that supported the bridge (11c) of the incinerated matter (11) in the narrowed portion (4). Because (11b) falls,
The incineration material (11) in the storage tank (1) is gradually lowered from the lower (11a) direction by a natural dropping force by the amount of combustion loss in the combustion chamber (12). By the repeated action of this phenomenon, the incinerated material (11) in the storage tank (1) is repeatedly dried, burned, and dropped in a quantitative manner.
この狭絞部(4)の上斜線（）と垂直線(v)とがなす角
（θ）を30〜60°とした理由は、この狭絞部(4)によっ
て形成されるブリッジの形成量が30°以下では充分でな
く、また60°を超えるとブリッジ力が大きくなり貯蔵物
の自然落下しなくなるため結局30〜60°が最も好ましい
範囲であるというこの考案者の実験的知得に基づくもの
である。The angle (θ) formed by the upper diagonal line () and the vertical line (v) of the narrowed portion (4) is set to 30 to 60 ° because the amount of the bridge formed by the narrowed portion (4) is set. Is less than 30 °, and if it exceeds 60 °, the bridging force becomes large and the stored goods do not fall naturally, so that 30-60 ° is the most preferable range based on the experimental knowledge of the present inventor. It is a thing.
第２図に示す如く少なくとも空気供給口(7)から空気を
湿潤固型物(11)に向かってまず送り出す。As shown in FIG. 2, air is first sent out from at least the air supply port (7) toward the wet solid material (11).
助燃バーナー(5)から炎(13)を湿潤固型物(11)方向に向
かって送り出すと、この空間(12)の境界面(14)が燃焼面
となって燃焼が開始される。When the flame (13) is sent from the auxiliary combustion burner (5) toward the wet solid matter (11), the boundary surface (14) of the space (12) serves as a combustion surface to start combustion.
空気供給口(7)，(8)，(10)から空気を供給することによ
って湿潤固型物(11)の燃焼する。By supplying air from the air supply ports (7), (8) and (10), the wet solid matter (11) burns.
上斜面(4a)に形成された空気供給口(7)は、上斜線
（）にに対し垂直方向に空気を供給することにより、
塵芥等の湿潤固型物(11)が狭絞部(4)の内周(4c)上でブ
リッヂ現象の順滑な作用を促進するものである。The air supply port (7) formed on the upper slope (4a) supplies air in a direction perpendicular to the upper slope (),
The wet solid matter (11) such as dust promotes the smooth action of the bridge phenomenon on the inner circumference (4c) of the narrowed portion (4).
尚、この空気供給口(7)から湿潤固型物(11)内に供給さ
れる空気は湿潤固型物(11)の乾燥も促進する。The air supplied from the air supply port (7) into the wet solid material (11) also accelerates the drying of the wet solid material (11).
燃焼部(3)内では湿潤固型物(11)がどんどん燃焼するた
め貯留部(1)も高温となって湿潤固型物(11)の水分が飛
散する。In the combustion section (3), the wet solid matter (11) burns more and more, so that the temperature of the storage section (1) also rises and the moisture of the wet solid matter (11) scatters.
蒸散した水分は煙道(6)から燃焼済固型物と共に煙道方
向へ導かれる。The evaporated water is guided from the flue (6) toward the flue along with the burned solid matter.
第４図乃至第５図は、この考案に於いて付設するこの湿
潤固型物連続焼却炉の後処理装置を示すものである。FIG. 4 to FIG. 5 show the post-treatment device of the wet solid-state continuous incinerator additionally provided in the present invention.
(15)は再燃炉、(16)は再燃バーナー、(17)は集塵機、(1
8)は吸引装置、(19)は煙突である。(15) is a reburn furnace, (16) is a reburn burner, (17) is a dust collector, and (1
8) is a suction device, and (19) is a chimney.
再燃炉(15)は、不完全燃焼で煙道(6)から送られてきた
固型物を再燃バーナー(16)の助けにより再度燃焼させ
る。The reburning furnace (15) reburns the solid matter sent from the flue (6) by incomplete combustion with the help of the reburning burner (16).
この再燃炉(15)は分解した有機ガス等を燃焼させる。This reburning furnace (15) burns decomposed organic gas and the like.
集塵機(17)は、灰等の固型分を吸収処理する。The dust collector (17) absorbs solid components such as ash.
尚、この燃焼部(3)から暖気運動によって煙道(6)から煙
突(19)方向に向かって、煙は押し出されるが、更に加え
て吸引装置(18)を作動させてその吸引作用により、押出
と吸引を連続作用することによって更に燃焼や灰の除却
がスムーズに移動する。The smoke is pushed out of the combustion section (3) by the warming motion toward the chimney (19) from the flue (6), but in addition, the suction device (18) is operated to suck the smoke. Combustion and ash removal move smoothly by continuous operation of extrusion and suction.
このようにして煙突(19)から、煤や煙、埃、有毒ガス等
が処理された燃焼ガスが大気に向かって放出される。In this way, the chimney (19) releases the combustion gas obtained by treating soot, smoke, dust, toxic gas, etc., to the atmosphere.
燃焼部(3)に於いては、貯槽(1)内の湿潤固型物(11)が順
次燃焼部(3)の方に自重で順次移動して、燃焼されるか
らに一定量の湿潤固型物(11)を貯槽(1)内に貯留放置す
るだけで連続して湿潤固型物の燃焼が可能である。In the combustion section (3), the wet solid matter (11) in the storage tank (1) sequentially moves toward the combustion section (3) by its own weight, and a certain amount of wet solid matter is burned. The wet solid material can be burned continuously only by leaving the mold material (11) stored in the storage tank (1).
（考案の効果） 以上詳述した如く、この考案に係る湿潤固型物連続焼却
炉は有毒中空筒状の貯留部とこの貯留部に連続連結され
た有底中空筒状の燃焼部とからなり、この燃焼部は上部
の特定箇所全周が断面くの字状に絞られて狭絞部とされ
少なくとも空気供給口がこの狭絞部の上斜面に形成され
この空気供給口は狭絞部上斜線（）に直交する角度で
空気が噴射する様に設けられこの狭絞部の上斜線（）
と垂直線(v)とがなす角（θ）は30〜60°とされてな
り、燃焼部下部に助燃バーナーが設けられると共に助燃
バーナーの対向位置に煙道が設けられてなる湿潤固型物
連続焼却炉であるから、湿潤固型物を乾燥させることな
く、湿潤した状態のままで且つ連続してしかも貯留部内
部で連続運転に障害を与えるブリッヂ現象等の現象を生
じないという効果を奏する。(Effect of the Invention) As described in detail above, the wet solid-state continuous incinerator according to the present invention comprises a poisonous hollow cylindrical storage section and a bottomed hollow cylindrical combustion section continuously connected to this storage section. , The combustion part is narrowed in a V-shaped cross section at a specific part of the upper part to form a narrowed part, and at least the air supply port is formed on the upper slope of the narrowed part, and the air supply port is located on the narrowed part. It is installed so that air is jetted at an angle orthogonal to the diagonal line ().
The angle (θ) formed by the vertical line (v) and the vertical line (v) is 30 to 60 °, and a solidified wet body is provided with an auxiliary combustion burner at the lower part of the combustion section and a flue at the opposite position of the auxiliary combustion burner. Since it is a continuous incinerator, it has an effect of not causing a phenomenon such as a bridge phenomenon that impairs continuous operation in a wet state and continuously without drying a wet solid matter in the storage section. .
第１図はこの考案の一実施例に係る湿潤固型物連続焼却
炉の断面説明図、第２図乃至第３図はこの考案の一実施
例に係る湿潤固型物連続焼却炉の使用状態説明図、第４
図はこの考案の一実施例に係る湿潤固型物連続焼却炉の
後処理装置をも含めた流れ説明図、第５図は第４図の平
面説明図である。 (1)…貯留部、(2)…蓋 (3)…燃焼部、(4)…狭絞部 (4a)…上斜面、(4b)…下斜面 (5)…助燃バーナー、(6)…煙道 (7)…空気供給口、(9)…底部FIG. 1 is a cross-sectional explanatory view of a wet solid material continuous incinerator according to an embodiment of the present invention, and FIGS. 2 to 3 are usage states of the wet solid material continuous incinerator according to an embodiment of the present invention. Explanatory drawing, 4th
FIG. 5 is a flow chart including a post-treatment system for a wet solid matter continuous incinerator according to an embodiment of the present invention, and FIG. 5 is a plan view of FIG. (1) ... Reservoir, (2) ... Lid (3) ... Combustion, (4) ... Narrowing (4a) ... Upper slope, (4b) ... Lower slope (5) ... Burning burner, (6) ... Flue (7) ... air inlet, (9) ... bottom
Claims (1)
連結された有底中空筒状の燃焼部とからなり、この燃焼
部は上部の特定箇所全周が断面くの字状に絞られて狭絞
部とされ少なくとも空気供給口がこの狭絞部の上斜面に
形成されこの空気供給口は狭絞部上斜線（）に直交す
る角度で空気が噴射する様に設けられこの狭絞部の上斜
線（）と垂直線(v)とがなす角（θ）は30〜60°とさ
れてなり、燃焼部下部に助燃バーナーが設けられると共
に助燃バーナーの対向位置に煙道が設けられてなる湿潤
固型物連続焼却炉。1. A hollow cylindrical storage part having a lid and a combustion part having a bottomed hollow cylinder continuously connected to the storage part, and the combustion part has a cross-section having a cross-section around a specific portion of an upper part thereof. At least an air supply port is formed on the upper slope of the narrowed part, and the air supply port is provided so that air is jetted at an angle orthogonal to the upper oblique line () of the narrowed part. The angle (θ) formed by the upper diagonal line () and the vertical line (v) of the throttle part is set to 30 to 60 °, and an auxiliary combustion burner is installed in the lower part of the combustion part and a flue is installed in the position opposite to the auxiliary combustion burner. A wet solid continuous incinerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2128289U JPH0619944Y2 (en) | 1989-02-22 | 1989-02-22 | Wet solid continuous incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2128289U JPH0619944Y2 (en) | 1989-02-22 | 1989-02-22 | Wet solid continuous incinerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02115634U JPH02115634U (en) | 1990-09-17 |
| JPH0619944Y2 true JPH0619944Y2 (en) | 1994-05-25 |
Family
ID=31238385
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2128289U Expired - Lifetime JPH0619944Y2 (en) | 1989-02-22 | 1989-02-22 | Wet solid continuous incinerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0619944Y2 (en) |
-
1989
- 1989-02-22 JP JP2128289U patent/JPH0619944Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02115634U (en) | 1990-09-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA1039580A (en) | Refuse incinerator | |
| JP4465013B2 (en) | Smokeless combustion equipment | |
| EP0891517B1 (en) | Apparatus and method for burning organic material | |
| JPH0619944Y2 (en) | Wet solid continuous incinerator | |
| CN213421107U (en) | Incinerator for fully incinerating garbage | |
| JP3091181B2 (en) | Incinerator | |
| CN2408359Y (en) | Refuse incinerating boiler | |
| CN205026682U (en) | Garbage incinerator | |
| JP2511553Y2 (en) | Incinerator | |
| KR100231976B1 (en) | A trash burner | |
| KR20150065990A (en) | Stove having a fuel drying chamber | |
| KR200193831Y1 (en) | Firewood a burner | |
| JPH04302908A (en) | Incinerator | |
| KR100961275B1 (en) | A livestock excrement incineration boiler | |
| EP0040265B1 (en) | Apparatus for converting garbage into a fuel gas | |
| KR810002051B1 (en) | Incinerators for town refuse | |
| JPH0718541B2 (en) | Garbage incinerator | |
| JP2609986B2 (en) | Incinerator | |
| KR900003841Y1 (en) | Inverted combustion stove | |
| JPH0212404Y2 (en) | ||
| KR820000407Y1 (en) | Incinerators for town refuse | |
| SU1755009A1 (en) | Portable incinerator | |
| JP3044852U (en) | Incinerator | |
| JPH03194309A (en) | Stabilizing burner in incinerator and smoke consuming incinerator provided with same | |
| JPH0722224U (en) | Waste incinerator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |