JPH0221120A - Garbage incineration method - Google Patents

Garbage incineration method

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Publication number
JPH0221120A
JPH0221120A JP17158988A JP17158988A JPH0221120A JP H0221120 A JPH0221120 A JP H0221120A JP 17158988 A JP17158988 A JP 17158988A JP 17158988 A JP17158988 A JP 17158988A JP H0221120 A JPH0221120 A JP H0221120A
Authority
JP
Japan
Prior art keywords
combustion
air
carbon
combustion chamber
partial
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
JP17158988A
Other languages
Japanese (ja)
Other versions
JPH0656252B2 (en
Inventor
Kozo Fujita
藤田 航三
Isamu Tatsuno
勇 辰野
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.)
Sasakura Engineering Co Ltd
Original Assignee
Sasakura Engineering 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 Sasakura Engineering Co Ltd filed Critical Sasakura Engineering Co Ltd
Priority to JP63171589A priority Critical patent/JPH0656252B2/en
Publication of JPH0221120A publication Critical patent/JPH0221120A/en
Publication of JPH0656252B2 publication Critical patent/JPH0656252B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

PURPOSE:To reduce the damage on a furnace wall in an unburnt substance combustion chamber and improve durability by supplying partial combustion air to the lower side of a fire grate and carbon combustion air to the bottom of an unburnt substance combustion furnace respectively, and increasing/decreasing the quantity of both the partial combustion air and the carbon combustion air. CONSTITUTION:When a waste A is thrown into a partial combustion chamber 13 of a primary combustion furnace 1, air is supplied from an air supply port 16, and the waste A is ignited by an ignition burner 25, unburnt substances, such as carbon drop from a fire grate 12 consecutively into an unburnt substance combustion chamber 14 as the partial combustion advances. When the temperature in a combustible gas outlet 4 rises gradually, in keeping with the progress in the partial combustion, a flow rate control valve 24 for an air supply pipe 18 is opened by way of a control unit 20 so as to supply air to the bottom of the unburnt substance combustion chamber 14. Therefore, an unburnt substance B in the combustion chamber 14 starts carbon combustion. When the temperature is increased to a certain degree inside the chamber 14, the flow rate control valve is closed so as to inhibit the carbon combustion of the unburnt substances. It is, therefore, possible to prevent the generation of clinkers inside the unburnt substance combustion chamber and improve durability as well.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、合成樹脂やゴム等を含む産業・都市廃棄物を
焼却するための焼却装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an incinerator for incinerating industrial and municipal wastes containing synthetic resins, rubber, and the like.

〔従来の技術と発明が解決しようとする課題〕合成樹脂
やゴム等を含む産業・都市廃棄物を焼却する場合、最近
では、焼却時に発生する有害ガスの略完全なりリーン化
を図ること、及び燃焼温度を下げることより燃焼炉にお
ける耐久性の向上を図る等のために、廃棄物を、−旦、
一次燃焼炉内において部分燃焼してガス化し、次いで、
この一次燃焼炉において発生した可燃性ガスを、二次燃
焼炉内に導き、この二次燃焼炉内において二次燃焼空気
との混合によって完全燃焼すると云ういわゆる乾溜ガス
化焼却方式が採用されている。
[Problems to be solved by conventional technology and inventions] When incinerating industrial/municipal waste containing synthetic resins, rubber, etc., it has recently become necessary to achieve almost complete lean reduction of harmful gases generated during incineration; In order to improve the durability of the combustion furnace by lowering the combustion temperature, the waste is
It is partially combusted and gasified in the primary combustion furnace, and then
The so-called dry distillation gasification and incineration method is used, in which the combustible gas generated in the primary combustion furnace is guided into the secondary combustion furnace, where it is completely combusted by mixing with secondary combustion air. .

そして、この乾溜ガス化焼却方式に使用されている従来
の一次燃焼炉は、例えば、特公昭55−44283号公
報に記載されているように、一次燃焼炉の底部にロスト
ルを形成し、このロストルの下部に燃焼用の空気を供給
し、ロストル上において廃棄物の部分燃焼と、部分燃焼
後における未燃物の炭素燃焼とを行うように構成したも
のであった。
The conventional primary combustion furnace used in this dry distillation gasification and incineration method, for example, as described in Japanese Patent Publication No. 55-44283, has a rostre formed at the bottom of the primary combustion furnace. Air for combustion was supplied to the lower part of the combustion chamber, and the waste was partially combusted on the rostrum, and after the partial combustion, the unburnt material was combusted with carbon.

しかし、このものは、ロストルの下側に、廃棄物の部分
燃焼に必要な空気と、部分燃焼後の未燃物の炭素燃焼に
必要な空気とを同時に供給するもので、そのロストル上
では、廃棄物の部分燃焼の進行に引き続いて、この部分
燃焼後における未燃物の炭素燃焼が行なわれることによ
り、廃棄物の部分燃焼と未燃物における炭素燃焼とが相
互に促進されて、著しく高温になるから、廃棄物中に含
まれるガラス及び金属等の不燃物が凝結すること、及び
廃棄物中に含まれるアルカリ塩の溶融で焼却残灰を凝結
すると云ういわゆるクリンカーが急速に成長して、燃焼
を阻害する頻度が多発し、且つ、一次燃焼炉の耐久性が
低下するのであり、しかも、廃棄物の部分燃焼と未燃物
における炭素燃焼とが相互に促進される現象が局部的に
発生し、一次燃焼炉内に投入された廃棄物の層には、廃
棄物の部分燃焼と未燃物の炭素燃焼とが相互に局部的に
促進される部分に空洞部ができ、遂には、燃焼用の空気
がこの空洞部を吹き抜けることになるから、廃棄物の燃
焼を部分燃焼の状態に制御することができなくなる事態
を招来するのであった。
However, this system simultaneously supplies the air necessary for partial combustion of waste and the air necessary for carbon combustion of unburned material after partial combustion to the bottom of the rostle. Following the progress of partial combustion of the waste, carbon combustion of the unburned material occurs after this partial combustion, so that the partial combustion of the waste and the carbon combustion of the unburned material are mutually promoted, resulting in a significantly high temperature. As a result, incombustible materials such as glass and metals contained in waste condense, and so-called clinker, which condenses incineration ash by melting alkali salts contained in waste, rapidly grows. Combustion is often inhibited, and the durability of the primary combustion furnace is reduced. Moreover, a phenomenon occurs locally where partial combustion of waste and carbon combustion in unburned materials are mutually promoted. However, in the layer of waste fed into the primary combustion furnace, cavities are formed in areas where partial combustion of waste and carbon combustion of unburned materials are mutually promoted locally, and eventually combustion occurs. Since the air used for combustion blows through this cavity, it becomes impossible to control the combustion of the waste to a state of partial combustion.

そこで、特公昭58−24473号公報は、次燃焼炉内
において、ゴム等の廃棄物を部分燃焼し、次いで、この
部分燃焼後における未燃焼物の炭素燃焼を行うに際して
、一次燃焼炉内に、上部における部分燃焼室と壱の下部
における未燃物燃焼室とに8成するロストルを設けて、
廃棄物をロストル上の部分燃焼室において部分燃焼し、
この部分燃焼後の未燃物を、ロストルより下部の未燃物
燃焼室に順次落下することにより、この未燃物燃焼室で
炭素燃焼するように構成することを提案しており、廃棄
物の部分燃焼と、未燃物の炭素燃焼とを分けて行うので
、その燃焼が相互に促進される現象が少なくなり、空洞
部の発生を低減できる。
Therefore, Japanese Patent Publication No. 58-24473 discloses that when waste such as rubber is partially combusted in the secondary combustion furnace and then carbon combustion of the unburned material after this partial combustion is performed, Providing eight rostles in the partial combustion chamber in the upper part and the unburnt combustion chamber in the lower part,
Partial combustion of the waste in a partial combustion chamber on the rostol,
It is proposed that the unburned materials after this partial combustion be sequentially dropped into the unburned materials combustion chamber below the rostre, so that carbon is burned in this unburned materials combustion chamber. Since the partial combustion and the carbon combustion of unburned materials are performed separately, the phenomenon in which the combustion is mutually promoted is reduced, and the occurrence of cavities can be reduced.

しかし、その反面、このものは、燃焼に必要な空気、つ
まり、廃棄部の部分燃焼に必要な空気及び未燃物の炭素
燃焼に必要な空気を、−纏めにして、前記未燃物燃焼室
の底部に供給する構成にしており、未燃物燃焼室内には
、未燃物の炭素燃焼に必要な空気と、廃棄物の部分燃焼
に必要な空気とが同時に供給され、未燃物燃焼室内にお
ける未燃物の炭素燃焼が、部分燃焼用空気のために旺盛
になり、その炭素燃焼時における燃焼温度が著しく高く
なるから、未燃物の炭素燃焼中において、クリンカーが
急速に成長し、未燃物の燃焼を阻害するばかりか、焼却
残灰の取り出しをきわめて困難にし、更に、未燃物燃焼
室が高温になることは、当該未燃物燃焼室における炉壁
の損傷が大きくなり、その耐久性を低下するのであった
However, on the other hand, in this case, the air necessary for combustion, that is, the air necessary for partial combustion of the waste section and the air necessary for carbon combustion of unburned materials, is collected and brought together into the unburned material combustion chamber. The air required for carbon combustion of unburned materials and the air required for partial combustion of waste are simultaneously supplied into the unburned materials combustion chamber. The carbon combustion of unburned materials becomes active due to the air for partial combustion, and the combustion temperature during carbon combustion becomes significantly high. During the carbon combustion of unburned materials, clinker grows rapidly and Not only does this hinder the combustion of the fuel, but it also makes it extremely difficult to remove the residual ash.Furthermore, the high temperature of the unburned combustion chamber increases the damage to the furnace wall in the unburned combustion chamber, which can cause serious damage to the furnace wall. This resulted in a decrease in durability.

また、廃棄物の部分燃焼に必要な空気量及び未燃物の炭
素燃焼に必要な空気量は、合成樹脂のようにガス化成分
が炭素成分より少ない廃棄物の場合と、ゴム等のように
ガス化成分よりも炭素成分が多い廃棄物の場合とでは相
違するから、前記のように、部分燃焼に必要な空気と未
燃物の炭素燃焼に必要な空気とを、同時に未燃物燃焼室
の底部に供給するものでは、廃棄物の成分比率が変わっ
た場合に、部分燃焼の状態及び炭素燃焼の状態を、その
成分比率に応じた最適の状態にすることが困難である点
も問題であった。
In addition, the amount of air required for partial combustion of waste and the amount of air required for carbon combustion of unburned materials are different for wastes such as synthetic resins where the gasification component is less than the carbon component, and for wastes such as rubber. This is different in the case of waste containing more carbon than gasified components, so as mentioned above, the air necessary for partial combustion and the air necessary for carbon combustion of unburned materials are simultaneously supplied to the unburned material combustion chamber. Another problem with the type of fuel that is supplied to the bottom of the waste is that if the component ratio of the waste changes, it is difficult to optimize the partial combustion state and carbon combustion state according to the component ratio. there were.

本発明は、この従来の乾溜ガス化焼却装置が有する問題
を解消することを目的とするものである。
The present invention aims to solve the problems of the conventional dry distillation gasification incinerator.

〔課題を解決するための手段〕[Means to solve the problem]

この目的を達成するため請求項1は、廃棄物を部分燃焼
してガス化するための一次燃焼炉と、該一次燃焼炉でガ
ス化した可燃性ガスを完全燃焼するための二次燃焼炉と
から成り、前記一次燃焼炉内に、当該一次燃焼炉の内部
を上部における部分燃焼室とその下部における未燃物燃
焼室とに8成するロストルを設けて成る焼却装置におい
て、前記一次燃焼炉内への燃焼用空気の供給手段を、前
記ロストルの下面部への部分燃焼用の空気供給手段と、
未燃物燃焼室の底部への炭素燃焼用の空気供給手段とで
構成した。
To achieve this object, claim 1 provides a primary combustion furnace for partially burning and gasifying waste, and a secondary combustion furnace for completely burning the combustible gas gasified in the primary combustion furnace. An incinerator is provided in the primary combustion furnace, the inside of the primary combustion furnace being divided into a partial combustion chamber in the upper part and an unburned material combustion chamber in the lower part. an air supply means for partial combustion to the lower surface of the rostre;
It is composed of an air supply means for carbon combustion to the bottom of the unburned material combustion chamber.

また、請求項2は、前記請求項1に加えて、前記ロスト
ルの下面部への部分燃焼用の空気供給手段に、前記二次
燃焼炉の出口温度が高くなるとロストルの下面部への空
気量を減少するようにした制御手段を、前記未燃物燃焼
室の底部への炭素燃焼用の空気供給手段に、前記未燃物
燃焼室の温度が高くなると未燃物燃焼室の底部への空気
量を減少するようにした制御手段を各々設ける構成にし
た。
In addition to the above-mentioned claim 1, a second aspect of the present invention provides that, in addition to the first aspect, the air supply means for partial combustion to the lower surface of the rosttle is configured such that when the outlet temperature of the secondary combustion furnace becomes high, an amount of air is increased to the lower surface of the rosttle. A control means configured to reduce the amount of air supplied to the bottom of the unburned combustion chamber for carbon combustion is provided with a control means configured to reduce the amount of air supplied to the bottom of the unburned combustion chamber when the temperature of the unburned combustion chamber becomes high. A configuration is adopted in which each control means is provided to reduce the amount.

〔発明の作用・効果〕[Action/effect of the invention]

前記請求項1のように、廃棄物の部分燃焼に必要な空気
をロストルの下面部に供給する一方、部分燃焼後におけ
る未燃物の炭素燃焼に必要な空気を未燃物燃焼室の底部
に供給すると、部分燃焼に必要な空気は、未燃物の炭素
燃焼の箇所を通過することがなく、換言すると、未燃物
の炭素燃焼が、部分燃焼に必要な空気によって促進され
ることがなく、未燃物の炭素燃焼を、未燃物燃焼室の底
部に供給する炭素燃焼用の空気によってのみ行うことが
できるから、未燃物の炭素燃焼に際しての温度が、部分
燃焼用の空気のために上昇することを回避できる。
As in claim 1, the air necessary for partial combustion of waste is supplied to the bottom of the rostre, while the air necessary for carbon combustion of unburned materials after partial combustion is supplied to the bottom of the unburnt combustion chamber. When supplied, the air required for partial combustion does not pass through the point where the carbon of the unburnt material is combusted, and in other words, the carbon combustion of the unburned material is not promoted by the air required for the partial combustion. , since carbon combustion of unburned materials can be performed only by the carbon combustion air supplied to the bottom of the unburned material combustion chamber, the temperature during carbon combustion of unburned materials is lower than that of the air for partial combustion. It is possible to avoid rising to

しかも、部分燃焼用の空気をロストルの下面部に、炭素
燃焼用の空気を未燃物燃焼炉の底部に各々供給するもの
で、この両者の空気量を別々に増減することができるか
ら、合成樹脂のようにガス化成分の方が多い廃棄物の場
合には、部分燃焼用の空気量を多く、炭素燃焼用の空気
量を少なくすることにより、また、ゴム等のように炭素
成分の方が多い廃棄物の場合には、部分燃焼用の空気量
を少なく、炭素燃焼用の空気量を多くすることにより、
部分燃焼の状態及び炭素燃焼の状態を、廃棄物の成分比
率に応じて調節することが的確にできるのである。
Moreover, the air for partial combustion is supplied to the bottom of the rostor, and the air for carbon combustion is supplied to the bottom of the unburned material combustion furnace, and the amount of air for both can be increased or decreased separately. In the case of waste that has more gasified components, such as resin, by increasing the amount of air for partial combustion and decreasing the amount of air for carbon combustion. In the case of waste with a large amount of carbon, reduce the amount of air for partial combustion and increase the amount of air for carbon combustion.
The state of partial combustion and the state of carbon combustion can be accurately adjusted according to the component ratio of the waste.

このように請求項1によると、未燃物の炭素燃焼に際し
ての燃焼温度の上昇を抑制することができるから、未燃
物燃焼室における炉壁の損傷を低減できて、その耐久性
を向上できると共に、未燃物の炭素燃焼に際してのタリ
ン力−の発生を防止でき、タリンカーの発生による炭素
燃焼の阻害を回避できると共に、焼却残灰の取り出しの
容易性を向上できるのであり、しかも、部分燃焼の状態
及び炭素燃焼の状態を、廃棄物の成分比率に応じて調節
することが的確にできるから、廃棄物の成分比率が変わ
った場合に、成分比率に対応した部分燃焼の状態と、炭
素燃焼の状態とを確実に得ること力Vでき、換言すると
、廃棄物の成分比率の変化に対して確実に対応できる効
果を奏する。
According to claim 1, since it is possible to suppress the increase in combustion temperature during carbon combustion of unburned materials, damage to the furnace wall in the unburned materials combustion chamber can be reduced and its durability can be improved. At the same time, it is possible to prevent the generation of talin force during carbon combustion of unburned materials, avoid the inhibition of carbon combustion due to the generation of talin carbon, and improve the ease of removing the incineration ash. Since the state of carbon combustion and the state of carbon combustion can be adjusted accurately according to the component ratio of waste, when the component ratio of waste changes, the state of partial combustion and carbon combustion corresponding to the component ratio can be adjusted accurately. In other words, it has the effect of being able to reliably respond to changes in the component ratio of waste.

一方、請求項2によると、一次燃焼炉における部分燃焼
室内での廃棄物の部分燃焼により、可燃性ガスの発生量
が多くなって二次燃焼炉の出口温度が高くなれば、ロス
トルの下面部への部分燃焼用の空気量の減少にて、廃棄
物の部分燃焼が抑制され、二次燃焼炉の出口温度がそれ
以上に高くなることを防止できるから、二次燃焼炉にお
ける耐久性の向上を図ることかできると共に、二次燃焼
室からの排気ガスが有する熱を、ボイラー等の熱回収装
置によって回収する場合において、熱回収装置に対する
熱負荷の変動を低減できるのであり、また、未燃物燃焼
室での未燃物の炭素燃焼に際して、未燃物燃焼室の温度
が高くなれば、未燃物燃焼室の底部への炭素燃焼用の空
気量の減少にて、炭素燃焼が抑制され、未燃物燃焼室の
温度がそれ以上に高(なることを防止できるから、未燃
物燃焼室内におけるタリンカーの発生を防止すること、
及び未燃物燃焼室の耐久性を向上することを、より効果
的に達成できるのである。
On the other hand, according to claim 2, if the amount of combustible gas generated increases due to the partial combustion of waste in the partial combustion chamber in the primary combustion furnace and the outlet temperature of the secondary combustion furnace becomes high, the lower surface of the rostor By reducing the amount of air for partial combustion, the partial combustion of waste is suppressed, and the outlet temperature of the secondary combustion furnace can be prevented from increasing further, improving the durability of the secondary combustion furnace. In addition, when the heat contained in the exhaust gas from the secondary combustion chamber is recovered by a heat recovery device such as a boiler, fluctuations in the heat load on the heat recovery device can be reduced. During carbon combustion of unburned materials in the combustion chamber, if the temperature of the unburned materials combustion chamber increases, the amount of air for carbon combustion at the bottom of the unburned materials combustion chamber decreases, suppressing carbon combustion. , Since the temperature of the unburned material combustion chamber can be prevented from becoming higher than that, it is possible to prevent the generation of coal in the unburned material combustion chamber;
And it is possible to more effectively achieve the improvement of the durability of the unburnt combustion chamber.

〔実施例〕〔Example〕

以下、本発明の実施例を図面ついて説明すると、図にお
いて符号1は、上部に廃棄物の投入口3と可燃性ガス出
口4とを備えた一次燃焼炉を、符号2は、二次燃焼より
バーナ26と送風機5からの二次燃焼用空気供給ノズル
6とを備えた二次燃焼炉を各々示し、前記一次燃焼炉l
の上部における可燃性ガス出口4は、前記二次燃焼炉2
の上部に接続され、前記二次燃焼炉2の下部に接続した
燃焼ガス出ロアは、集塵装置8、ボイラー等の熱回収装
置9及び排風用送風機10を経て煙突11に接続されて
いる。なお、前記廃棄物の投入口3には、シャッター3
aと蓋3bとを備え、シャッター3aを閉じた状態で蓋
3bを開いて投入口3内に廃棄物を投入し、次いで、蓋
3bを閉じた状態でシャッター3aを開くことにより、
廃棄物を、一次燃焼炉1内に落下するように構成されて
いる。
Hereinafter, embodiments of the present invention will be explained with reference to the drawings. In the drawings, reference numeral 1 indicates a primary combustion furnace equipped with a waste inlet 3 and a combustible gas outlet 4 at the upper part, and reference numeral 2 indicates a secondary combustion furnace. Each secondary combustion furnace is shown including a burner 26 and a secondary combustion air supply nozzle 6 from the blower 5, and the primary combustion furnace l
The combustible gas outlet 4 in the upper part of the secondary combustion furnace 2
The combustion gas output lower connected to the upper part of the secondary combustion furnace 2 and the lower part of the secondary combustion furnace 2 is connected to the chimney 11 via a dust collector 8, a heat recovery device 9 such as a boiler, and an exhaust blower 10. . Note that a shutter 3 is provided at the waste input port 3.
a and a lid 3b, and by opening the lid 3b with the shutter 3a closed and introducing waste into the input port 3, and then opening the shutter 3a with the lid 3b closed,
The waste is configured to fall into the primary combustion furnace 1.

前記一次燃焼炉l内における略中程部には、揺動回動す
る可動式のロストル12を設けることにより、一次燃焼
炉1の内部を前記ロストル12より上部における部分燃
焼室13と、前記ロストル12より下部における未燃物
燃焼室14とに8成する。
A movable rotor 12 that swings and rotates is provided approximately in the middle of the primary combustion furnace 1, so that the inside of the primary combustion furnace 1 can be divided into a partial combustion chamber 13 above the rostrtle 12 and a partial combustion chamber 13 above the rostrtle 12. 12 and an unburned material combustion chamber 14 below.

前記ロストル12の下面部には、送風機15からの部分
燃焼用の空気供給口16を開口する一方、前記未燃物燃
焼室14の底部には、送風機17がらの炭素燃焼用の空
気供給管18を設ける。
An air supply port 16 for partial combustion from the blower 15 is opened at the bottom of the rostre 12, while an air supply pipe 18 for carbon combustion from the blower 17 is opened at the bottom of the unburned material combustion chamber 14. will be established.

前記部分燃焼用の空気供給口16には、前記二次燃焼炉
2からの燃焼ガス出ロアに取付く温度計19にて検出し
た温度Tlにより制御ユニット20を介して開閉制御さ
れる流量制御弁21を設ける。また、前記炭素燃焼用の
空気供給管18には、前記一次燃焼炉1における可燃性
ガス出口4に取付く温度計22、及び前記未燃物燃焼室
14の上部に取付く温度計23にて検出した温度により
制御ユニット20を介して開閉制御される流量制御弁2
4を設ける。
The air supply port 16 for partial combustion has a flow rate control valve that is controlled to open and close via the control unit 20 based on the temperature Tl detected by a thermometer 19 attached to the lower combustion gas outlet from the secondary combustion furnace 2. 21 will be provided. Further, in the air supply pipe 18 for carbon combustion, a thermometer 22 attached to the combustible gas outlet 4 in the primary combustion furnace 1 and a thermometer 23 attached to the upper part of the unburned material combustion chamber 14 are connected. A flow rate control valve 2 whose opening and closing are controlled via a control unit 20 according to the detected temperature.
4 will be provided.

一次燃焼炉1における部分燃焼室13内に、廃棄物Aを
投入し、部分燃焼用の空気供給口16がら空気を供給し
た状態で、廃棄物Aに点火バーナー25にて着火すると
、廃棄物Aの中におけるガス化成分が部分燃焼によって
ガス化して、可燃性ガスが発生し、この可燃性ガスが可
燃性ガス出口4を介して二次燃焼炉2内に導かれ、当該
二次燃焼炉2内において、空気供給ノズル6からの二次
空気と混合されたのち、二次燃焼用バーナ26によって
略完全燃焼されたのち、燃焼ガス出ロアがら集塵装置8
、熱回収装置9及び排風用送風機lOを経て煙突11に
排出されるのであり、この場合において、燃焼ガス出ロ
アにおける出口温度T1が成る温度(例えば、約100
0℃)にまで高くなれば、制御ユニッ1−20を介して
、前記部分燃焼用の空気供給口16における流量制御弁
21がその開度を閉じて、廃棄物Aの部分燃焼を抑制す
ることにより、燃焼ガス出ロアにおける出口温度T1が
、これ以上に高くなることがないように自動制御される
Waste A is put into the partial combustion chamber 13 of the primary combustion furnace 1, and when the waste A is ignited with the ignition burner 25 while air is supplied from the air supply port 16 for partial combustion, the waste A The gasified components in the inside are gasified by partial combustion to generate combustible gas, and this combustible gas is led into the secondary combustion furnace 2 via the combustible gas outlet 4, and the secondary combustion furnace 2 After being mixed with secondary air from the air supply nozzle 6 in the air supply nozzle 6 and almost completely combusted by the secondary combustion burner 26, the combustion gas is removed from the lower dust collector 8.
, the exhaust gas is discharged to the chimney 11 via the heat recovery device 9 and the exhaust blower lO, and in this case, the temperature at which the outlet temperature T1 at the combustion gas output lower is reached (for example, about 100
0° C.), the flow rate control valve 21 in the air supply port 16 for partial combustion closes its opening via the control unit 1-20 to suppress partial combustion of the waste A. Accordingly, the outlet temperature T1 at the combustion gas output lower is automatically controlled so as not to become higher than this.

一方、前記廃棄物Aの部分燃焼室13内での部分燃焼の
進行に伴い、炭素等の未燃物は、ロストル12よりその
下部における未燃物燃焼室14に順次落下する。
On the other hand, as the partial combustion of the waste A progresses in the partial combustion chamber 13, unburned materials such as carbon sequentially fall from the rostrum 12 to the unburned material combustion chamber 14 located below it.

この部分燃焼の進行に伴い、一次燃焼炉1からの可燃性
ガス出口4における温度T2が次第に上昇するから、こ
の温度T2が成る温度(例えば、約800℃)になった
ときにおいて、前記ロストル12を揺動回動することに
より、未燃物の落下の促進を図ると共に、制御ユニソ)
20を介して前記炭素燃焼用の空気供給管18に対する
流量制御弁24を自動的に開き作動する。
As this partial combustion progresses, the temperature T2 at the combustible gas outlet 4 from the primary combustion furnace 1 gradually increases. By swinging and rotating the
20, the flow rate control valve 24 for the carbon combustion air supply pipe 18 is automatically opened and operated.

すると、未燃物燃焼室14の底部に空気が供給されるか
ら、未燃物燃焼室14内に落下した未燃物Bは、炭素燃
焼を開始するのであり、この炭素燃焼に際して、未燃物
燃焼室14内の温度が成る温度T3 (例えば、約60
0℃)にまで高くなると、制御ユニット20を介して、
前記炭素燃焼用の空気供給管18に対する流量制御弁2
4の開度が閉じて、未燃物の炭素燃焼を抑制することに
より、未燃物燃焼室14の温度T3が、これ以上に高く
なることがないように自動制御される。
Then, since air is supplied to the bottom of the unburned material combustion chamber 14, the unburned material B that has fallen into the unburned material combustion chamber 14 starts carbon combustion. Temperature T3 at which the temperature inside the combustion chamber 14 becomes (for example, about 60
0°C), via the control unit 20,
Flow control valve 2 for the air supply pipe 18 for carbon combustion
4 is closed to suppress carbon combustion of unburned materials, the temperature T3 of the unburned material combustion chamber 14 is automatically controlled so as not to rise any higher.

そして、前記部分燃焼及び炭素燃焼が更に進行すると、
前記ロストル12を揺動回動することにより、未燃物を
落下し、ロストル12上に廃棄物がなくなるから、残り
少なくなれば、投入口3から部分燃焼室1内に新たな廃
棄物を投入し、前記未燃物燃焼室14における炭素燃焼
の熱によって、新たな廃棄物の部分燃焼を行うのである
Then, when the partial combustion and carbon combustion further progress,
By swinging and rotating the rostol 12, unburned materials are dropped and there is no waste on the rostrum 12, so when there is little left, new waste can be thrown into the partial combustion chamber 1 from the input port 3. , new waste is partially combusted by the heat of carbon combustion in the unburned material combustion chamber 14.

なお、新たな廃棄物の投入は、一次燃焼炉1からの可燃
性ガス出口4における温度T2に応じて炭素燃焼用の空
気供給管18に対する制御弁24を開く作動する時期の
前後の時期に行うようにしても良いのである。
Note that new waste is introduced before and after the time when the control valve 24 for the air supply pipe 18 for carbon combustion is operated according to the temperature T2 at the combustible gas outlet 4 from the primary combustion furnace 1. You can do it like this.

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

図面は本発明の実施例を示す図である。 1・・・・一次燃焼炉、2・・・・二次燃焼炉、3・・
・・廃棄物投入口、4・・・・可燃ガス出口、6・・・
・二次燃焼用空気供給ノズル、11・・・・煙突、12
・・・・ロストル、13・・・・部分燃焼室、14・・
・・未燃物燃焼室、16・・・・部分燃焼用の空気供給
口、18・・・・炭素燃焼用の空気供給管、19,22
.23・・・・温度計、20・・・・制御ユニット、2
1.24・・・・流量制御弁。
The drawings are diagrams showing embodiments of the invention. 1...Primary combustion furnace, 2...Secondary combustion furnace, 3...
...Waste inlet, 4...Combustible gas outlet, 6...
・Air supply nozzle for secondary combustion, 11...Chimney, 12
...Rostle, 13...Partial combustion chamber, 14...
... Unburned material combustion chamber, 16... Air supply port for partial combustion, 18... Air supply pipe for carbon combustion, 19, 22
.. 23...Thermometer, 20...Control unit, 2
1.24...Flow rate control valve.

Claims (2)

【特許請求の範囲】[Claims] (1)、廃棄物を部分燃焼してガス化するための一次燃
焼炉と、該一次燃焼炉でガス化した可燃性ガスを完全燃
焼するための二次燃焼炉とから成り、前記一次燃焼炉内
に、当該一次燃焼炉の内部を上部における部分燃焼室と
その下部における未燃物燃焼室とに区成するロストルを
設けて成る焼却装置において、前記一次燃焼炉内への燃
焼用空気の供給手段を、前記ロストルの下面部への部分
燃焼用の空気供給手段と、未燃物燃焼室の底部への炭素
燃焼用の空気供給手段とで構成したことを特徴とする廃
棄物の焼却装置。
(1) Consisting of a primary combustion furnace for partially burning and gasifying waste, and a secondary combustion furnace for completely burning the combustible gas gasified in the primary combustion furnace, the primary combustion furnace In an incinerator, the incinerator is provided with a rostre that divides the inside of the primary combustion furnace into a partial combustion chamber in the upper part and an unburned material combustion chamber in the lower part, the supply of combustion air into the primary combustion furnace. A waste incineration apparatus characterized in that the means is comprised of an air supply means for partial combustion to the lower surface of the rostre and an air supply means for carbon combustion to the bottom of the unburned material combustion chamber.
(2)、廃棄物を部分燃焼してガス化するための一次燃
焼炉と、該一次燃焼炉でガス化した可燃性ガスを完全燃
焼するための二次燃焼炉とから成り、前記一次燃焼炉内
に、当該一次燃焼炉の内部を上部における部分燃焼室と
その下部における未燃物燃焼室とに区成するロストルを
設けて成る焼却装置において、前記一次燃焼炉内への燃
焼用空気の供給手段を、前記ロストルの下面部への廃棄
物部分燃焼用の空気供給手段と、未燃物燃焼室の底部へ
の未燃物炭素燃焼用の空気供給手段とで構成し、前記ロ
ストルの下面部への部分燃焼用の空気供給手段に、前記
二次燃焼炉の出口温度が高くなるとロストルの下面部へ
の空気量を減少するようにした制御手段を、前記未燃物
燃焼室の底部への炭素燃焼用の空気供給手段に、前記未
燃物燃焼室の温度が高くなると未燃物燃焼室の底部への
空気量を減少するようにした制御手段を各々設けたこと
を特徴とする廃棄物の焼却装置。
(2) Consisting of a primary combustion furnace for partially burning and gasifying waste, and a secondary combustion furnace for completely burning the combustible gas gasified in the primary combustion furnace, the primary combustion furnace In an incinerator, the incinerator is provided with a rostre that divides the inside of the primary combustion furnace into a partial combustion chamber in the upper part and an unburned material combustion chamber in the lower part, the supply of combustion air into the primary combustion furnace. The means includes an air supply means for partially burning waste to the lower surface of the roost and an air supply means for burning unburned carbon to the bottom of the unburned combustion chamber, The air supply means for partial combustion to the bottom of the unburnt combustion chamber is provided with a control means that reduces the amount of air to the bottom of the rooster when the outlet temperature of the secondary combustion furnace becomes high. A waste product characterized in that each of the air supply means for carbon combustion is provided with a control means that reduces the amount of air to the bottom of the unburned combustion chamber when the temperature of the unburned combustion chamber increases. Incinerator.
JP63171589A 1988-07-08 1988-07-08 Batch type incinerator of waste Expired - Fee Related JPH0656252B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63171589A JPH0656252B2 (en) 1988-07-08 1988-07-08 Batch type incinerator of waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63171589A JPH0656252B2 (en) 1988-07-08 1988-07-08 Batch type incinerator of waste

Publications (2)

Publication Number Publication Date
JPH0221120A true JPH0221120A (en) 1990-01-24
JPH0656252B2 JPH0656252B2 (en) 1994-07-27

Family

ID=15925961

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63171589A Expired - Fee Related JPH0656252B2 (en) 1988-07-08 1988-07-08 Batch type incinerator of waste

Country Status (1)

Country Link
JP (1) JPH0656252B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994009320A1 (en) * 1992-10-16 1994-04-28 Erithglen Limited Furnaces
CN104819469A (en) * 2015-04-01 2015-08-05 上海辰月环保科技有限公司 Garbage pyrolysis gasifier
JP2020098081A (en) * 2018-12-19 2020-06-25 株式会社プランテック Combustion control method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS553606A (en) * 1978-06-21 1980-01-11 Toshiba Corp Photo-semiconductor coupling device and its manufacturing method
JPS5918132U (en) * 1982-06-17 1984-02-03 佐藤 武弥 Combustion equipment equipped with dry distillation furnace
JPS61217618A (en) * 1985-03-22 1986-09-27 Maitei Eng Kk Automatic control method of dry distillation combustion device
US4732092A (en) * 1985-09-30 1988-03-22 G.G.C., Inc. Pyrolysis and combustion apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS553606A (en) * 1978-06-21 1980-01-11 Toshiba Corp Photo-semiconductor coupling device and its manufacturing method
JPS5918132U (en) * 1982-06-17 1984-02-03 佐藤 武弥 Combustion equipment equipped with dry distillation furnace
JPS61217618A (en) * 1985-03-22 1986-09-27 Maitei Eng Kk Automatic control method of dry distillation combustion device
US4732092A (en) * 1985-09-30 1988-03-22 G.G.C., Inc. Pyrolysis and combustion apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994009320A1 (en) * 1992-10-16 1994-04-28 Erithglen Limited Furnaces
CN104819469A (en) * 2015-04-01 2015-08-05 上海辰月环保科技有限公司 Garbage pyrolysis gasifier
CN104819469B (en) * 2015-04-01 2018-05-01 上海寅意环保科技有限公司 A kind of refuse pyrolysis gasification furnace
JP2020098081A (en) * 2018-12-19 2020-06-25 株式会社プランテック Combustion control method

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