JPH01200112A - Refuse incinerator - Google Patents

Refuse incinerator

Info

Publication number
JPH01200112A
JPH01200112A JP2455988A JP2455988A JPH01200112A JP H01200112 A JPH01200112 A JP H01200112A JP 2455988 A JP2455988 A JP 2455988A JP 2455988 A JP2455988 A JP 2455988A JP H01200112 A JPH01200112 A JP H01200112A
Authority
JP
Japan
Prior art keywords
refuse
accumulating part
incinerator
combustion
garbage
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
JP2455988A
Other languages
Japanese (ja)
Other versions
JPH0660731B2 (en
Inventor
Seizo Katsui
征三 勝井
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.)
PURANTETSUKU KK
Plantex Ltd
Original Assignee
PURANTETSUKU KK
Plantex 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 PURANTETSUKU KK, Plantex Ltd filed Critical PURANTETSUKU KK
Priority to JP63024559A priority Critical patent/JPH0660731B2/en
Publication of JPH01200112A publication Critical patent/JPH01200112A/en
Publication of JPH0660731B2 publication Critical patent/JPH0660731B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To enable prevention of the occurrence of pollution, e.g., smell generated during the initial stage of operation, by a method wherein a refuse accumulating part having capacity lower than that of an incinerator body is mounted to the upper stream part of an incinerator body, and combustion during the initial stage of operation is effected by the accumulating part. CONSTITUTION:During normal operation, refuse charged in a hopper 1 is accumulated at an accumulating part 4. After the refuse is preliminarily dried by means of high temperature gas fed to the accumulating part 4, it is fed in an incinerator body 10 for incineration. Right before the stop of operation, refuse residing in the accumulating part 4 is burnt off without feeding it to the incinerator body 10 side, and the incineration ash is preserved at the incinerating part 4 in a state to be left at a high temperature. During the starting of operation, a small amount of refuse is charged in the accumulating part 4, through effective utilization of heat possessed by the incineration ash and a heat accumulating part, e.g., refractory heat insulating material, the refuse is ignited together with air the temperature of which is increased. Combustion is started by the accumulating part 4 by means of the ignited refuse serving as a pilot fire to promote increase of the temperature of the incinerator body 10. At a stage in which combustion at the accumulating part 4 is progressed, accumulated incineration ash is orderly fed in the incinerator body 10 to perform rapid and smooth migration to normal operation.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、一般廃棄物や産業廃棄物などを焼却するごみ
焼却炉に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a garbage incinerator that incinerates general waste, industrial waste, and the like.

(従来の技術) 従来、例えばストーカ炉を間歇運転する場合、運転終了
時から翌朝の運転開始時までの間に焼却炉内の温度が低
下するため、運転開始時に助燃バーナ等によって冷えた
焼却炉内の温度を上昇させるが、上記助燃バーナ等を用
いれば燃料費が嵩むため、−aには、埋火方式が採用さ
れている。
(Prior art) Conventionally, for example, when operating a stoker furnace intermittently, the temperature inside the incinerator decreases between the end of operation and the start of operation the next morning. However, if the auxiliary combustion burner or the like is used, the fuel cost will increase, so a buried fire method is adopted for -a.

この方式は、運転終了時から運転開始時までの休業時間
中に生じる炉内温度の低下を抑制しようとするもので、
運転終了直前に焼却炉内に1時間分程度のごみを追加投
入し、これに少量の空気を供給しながら炉内に残った火
種と耐火物の蓄熱を利用して、休業時間中も少量ずつ燃
焼を継続させることで、運転開始時の炉内温度をできる
だけ高く維持するようになされていた。
This method attempts to suppress the drop in temperature inside the furnace that occurs during the downtime between the end of operation and the start of operation.
Just before the end of operation, approximately one hour's worth of waste is added to the incinerator, and a small amount of air is supplied to this incinerator, using the remaining embers and heat stored in the refractories inside the incinerator to continue discharging the waste little by little during the closure period. By continuing combustion, the temperature inside the furnace at the start of operation was maintained as high as possible.

(発明が解決しようとする課題) しかしながら、上記した埋火方式の場合では、休業時間
中において、時間の経過に伴い排ガス温度が次第に低下
するため電気集じん器等の後続設備の腐食を招くおそれ
があり、このため排ガスは空気予熱器、電気集じん器、
誘引通風機などをバイパスして、直接煙突に導かれるこ
とが多く、これによって、煙突からはばいじんを含んだ
有色煙を排出することになる。また、燃焼温度が低下す
るため、排ガス中の臭気成分の熱分解が十分でなく、ご
み質や気象条件などによっては臭気公害を発生すること
もある。さらに、休業時間中も燃焼が継続しているため
、防火など施設管理上の問題があった。
(Problem to be Solved by the Invention) However, in the case of the above-mentioned buried fire method, the temperature of the exhaust gas gradually decreases over time during closed hours, which may lead to corrosion of subsequent equipment such as electrostatic precipitators. For this reason, exhaust gas is collected by air preheaters, electrostatic precipitators,
In many cases, the smoke is guided directly into the chimney, bypassing an induced draft fan, etc., and as a result, colored smoke containing soot and dust is emitted from the chimney. Furthermore, since the combustion temperature is lowered, the thermal decomposition of odor components in the exhaust gas is insufficient, and odor pollution may occur depending on the quality of the waste, weather conditions, etc. Furthermore, since combustion continued during business hours, there were problems with fire prevention and other facility management.

これら問題を解決するものとして、炉内のごみを焼却し
つくしてから運転停止する方式、いわゆる焚切り方式が
ある。この方式では休業時間中において、未処理ガスが
排出されないので前述の問題は生じないものの、炉内に
ごみの燃焼に伴う熱源がなくなり翌朝までに温度が下が
るため、運転開始時において、長時間の助燃が必要にな
るとともに、バーナによる助燃では炉内温度の上昇が遅
いため、炉内温度が適温になる間に燃焼するごみは不完
全燃焼により黒煙及び臭気公害を発生させるという問題
があった。
As a solution to these problems, there is a so-called burn-off method, in which the garbage in the furnace is completely incinerated and then the operation is stopped. Although this method does not cause the above-mentioned problem because untreated gas is not discharged during business downtime, there is no longer a heat source in the furnace due to the combustion of waste, and the temperature drops by the next morning, so it takes a long time at the start of operation. In addition to the need for auxiliary combustion, auxiliary combustion using a burner causes the temperature inside the furnace to rise slowly, so there is a problem that garbage that burns while the temperature inside the furnace reaches the appropriate temperature causes incomplete combustion and generates black smoke and odor pollution. .

一方、流動床炉を間歇運転する場合は、炉内に投入され
るごみが破砕されているため着火が早く、燃焼時間が短
い上に流動砂の保有熱量も大きいので、炉の始動が簡単
であり運転停止も速やかに行えるため、休業時間中及び
運転開始時に有色煙、黒煙、臭気等の公害が発生しない
という利点がある。しかし、ストーカ炉と比較すると、
ごみの破砕や砂を流動・循環させる設備が余分に必要に
なるばかりでなく、所要電力もはるかに大きくなる。
On the other hand, when operating a fluidized bed furnace intermittently, the waste thrown into the furnace is crushed, so it ignites quickly, the combustion time is short, and the fluidized sand retains a large amount of heat, making it easy to start the furnace. Since operation can be stopped quickly, there is an advantage that no pollution such as colored smoke, black smoke, or odor is generated during closed hours or when starting operation. However, compared to a stoker furnace,
Not only would extra equipment be needed to crush the trash and move and circulate the sand, but the power requirements would also be far greater.

また、砂を流動させるためには、大量の空気を必要とす
るが、そのために流動砂の保有熱量が失われやすく、ご
み質が悪化するとストーカ炉よりも助燃量が増大すると
いう問題も起こる。
In addition, a large amount of air is required to fluidize the sand, which causes the fluidized sand to easily lose its retained heat, and when the quality of the waste deteriorates, the problem arises that the amount of auxiliary combustion increases compared to a stoker furnace.

(課題を解決するための手段) 本発明のごみ焼却炉は、一般廃棄物や産業廃棄物などの
ごみを焼却するごみ焼却炉であって、焼却炉本体の上流
部に、投入口から投入されたごみを堆積する堆積部が設
けられ、この堆積部は焼却炉本体よりも小容量で且つ蓄
熱性に優れ、さらに、堆積部には、乾燥用もしくは燃焼
用の気体が供給されるとともに、該堆積部の下部に形成
された排出口から焼却炉本体にごみを供給する供給手段
が設けられたものである。
(Means for Solving the Problems) The garbage incinerator of the present invention is a garbage incinerator that incinerates garbage such as general waste and industrial waste, and the garbage incinerator is fed into the upstream part of the incinerator body from the input port. A depositing section is provided for accumulating waste, and this depositing section has a smaller capacity than the incinerator main body and has excellent heat storage properties.Furthermore, drying or combustion gas is supplied to the depositing section, and the waste is A supply means is provided for supplying waste to the incinerator main body from an outlet formed at the lower part of the deposition section.

(作用) 平常運転時には、ホッパに投入されたごみは堆積部に堆
積しこの堆積部に供給されている高−温の気体により予
備乾燥された後、ごみを従来構造の焼却炉本体内に送り
焼却する。運転停止直前には、堆積部に滞留しているご
みを焼却炉本体側に送らずに焚切ってしまい、この焼却
灰を堆積部で高温のまま保存する。そして、例えば翌朝
の運転開始時には、堆積部に少量のごみを投入し堆積部
に堆積している高温の焼却灰と、耐火断熱材等の蓄熱部
の保有する熱量を有効利用して昇温させた空気とで、こ
のごみを着火させ、それを火種として堆積部で燃焼を開
始して、焼却炉本体の昇温を促進させる。そして、堆積
部での燃焼が進んだ段階で、堆積していた焼却灰を順次
焼却炉本体内に送り込み、平常運転に迅速且つ円滑に移
行する。
(Function) During normal operation, the garbage put into the hopper is deposited in the accumulation section, and after being pre-dried by the high-temperature gas supplied to this accumulation section, the garbage is sent into the incinerator main body of the conventional structure. Incinerate. Immediately before the operation is stopped, the garbage accumulated in the pile is burned off without being sent to the incinerator main body, and the incinerated ash is stored at a high temperature in the pile. For example, when starting operation the next morning, a small amount of garbage is put into the pile and the temperature is raised by effectively utilizing the high-temperature incinerated ash accumulated in the pile and the amount of heat held by heat storage parts such as fireproof insulation materials. The waste is ignited by the air, and the waste is used as a spark to start combustion in the accumulation area, promoting the temperature rise of the incinerator body. Then, at a stage when combustion in the accumulation section has progressed, the accumulated incineration ash is sequentially sent into the incinerator main body, and normal operation is quickly and smoothly resumed.

(実施例) 以下、本発明の一実施例を図面を参照して説明する。(Example) Hereinafter, one embodiment of the present invention will be described with reference to the drawings.

第゛1図は、本発明に係るごみ焼却炉の概略構成を示し
、第2図はこのごみ焼却炉に設けられた堆積部の概略構
成を示している。
FIG. 1 shows a schematic structure of a waste incinerator according to the present invention, and FIG. 2 shows a schematic structure of a depositing section provided in this waste incinerator.

本例では、焼却炉としてストーカ炉を例にとって説明す
る。
In this example, a stoker furnace will be used as an example of an incinerator.

図において、1はホッパで、ごみピット(図示省略)に
貯留されたごみがクレーン(図示省略)でこのホッパ1
に投入される。ホッパlは、フィーダ2を介してシュー
ト3に連通されており、ホッパ1に投入されたごみは、
フィーダ2によりシュート3に供給され、このシュート
3から堆積部4に堆積される。シュート3は水冷壁や耐
熱性を有する部材で構成されている。シュート3には開
閉ゲート7が設けられ、この開閉ゲート7の閉塞により
シュート3は遮断される。また、開閉ゲート7よりも下
方に位置するシュート3の途中部と焼却炉本体lOの上
部とはダンパ9を有する煙路8で連通されており、堆積
部4で発生したガスが煙路8を経て焼却炉本体lOの上
部に送られるようになされている。前記開閉ゲート7は
、堆積部4の上部に設けてもよく、この場合、煙路8は
開閉ゲート7よりも下方に位置する堆積部4の上部に接
続されることになる。
In the figure, 1 is a hopper, and garbage stored in a garbage pit (not shown) is transported to the hopper by a crane (not shown).
will be put into the The hopper l is communicated with the chute 3 via the feeder 2, and the garbage thrown into the hopper 1 is
It is supplied to a chute 3 by a feeder 2, and is deposited from this chute 3 into a deposition section 4. The chute 3 is composed of a water-cooled wall and a heat-resistant member. The chute 3 is provided with an opening/closing gate 7, and when the opening/closing gate 7 is closed, the chute 3 is blocked. Further, the middle part of the chute 3 located below the opening/closing gate 7 and the upper part of the incinerator main body 1O are communicated by a flue 8 having a damper 9, so that the gas generated in the deposition part 4 flows through the flue 8. The fuel is then sent to the upper part of the incinerator main body IO. The opening/closing gate 7 may be provided at the upper part of the depositing section 4, and in this case, the flue 8 will be connected to the upper part of the depositing section 4 located below the opening/closing gate 7.

堆積部4の側壁及び底壁は蓄熱性及び耐火性に優れた壁
体5で構成されており、これによって堆積部4内は高い
蓄熱性を有する。焼却炉本体10側に位置する堆積部4
の下部には排出口4aが形成されている。また、この堆
積部4の下部には該堆積部4に堆積したごみまたは灰を
排出口4aから焼却炉本体10に押し出すブツシャ6 
(供給手段)が設けられている。供給手段としては、ブ
ツシャ6に限らず、例えばコンベヤなどでもよい。
The side walls and bottom wall of the depositing section 4 are constituted by walls 5 having excellent heat storage properties and fire resistance, so that the inside of the depositing section 4 has high heat storage properties. Accumulation section 4 located on the incinerator main body 10 side
A discharge port 4a is formed in the lower part of the discharge port 4a. Further, at the lower part of the accumulation section 4, there is a button 6 for pushing out the garbage or ash accumulated in the accumulation section 4 from the discharge port 4a to the incinerator main body 10.
(supply means) is provided. The supply means is not limited to the busher 6, but may be a conveyor, for example.

さらに、堆積部4の上下部には、ごみ乾燥用もしくはご
み燃焼用の空気を該堆積部4に供給する供給管20が分
岐されてそれぞれ接続されており、この供給管20は底
部の壁体5に埋設された空気予熱器21を介して図示し
ない空気送風装置に接続されている。空気予熱器21は
、焼却炉内の燃焼により壁体5に蓄熱された熱量を利用
してここを通過する空気を昇温させるためのもので、こ
の昇温された空気は堆積部4にごみ乾燥用もしくはごみ
燃焼用として供給される。詳しくは、平常運転時に供給
される空気はごみ乾燥用として用いられ、運転開始時に
はごみ燃焼用として用いられる。
Furthermore, supply pipes 20 are branched and connected to the upper and lower parts of the depositing section 4, respectively, for supplying air for drying garbage or burning trash to the depositing section 4. It is connected to an air blower (not shown) via an air preheater 21 embedded in 5. The air preheater 21 is used to raise the temperature of the air passing through it by using the amount of heat stored in the wall 5 due to combustion in the incinerator, and this heated air is stored in the accumulation section 4 as waste. It is supplied for drying or waste combustion. Specifically, the air supplied during normal operation is used for drying garbage, and at the start of operation, it is used for burning garbage.

なお、本例では、堆積部4に供給する気体は壁体5に蓄
熱された熱を利用して昇温させた空気を利用したが、こ
れに限らず、焼却炉本体10内の滞留ガスまたは、焼却
炉本体10のケーシングを2重構造にし、そこに滞留し
た高温空気を利用しても良い。
In this example, the gas supplied to the deposition section 4 is air heated by using the heat stored in the wall 5. However, the present invention is not limited to this. Alternatively, the casing of the incinerator body 10 may have a double structure, and the high temperature air retained therein may be utilized.

図中の符号20a、20b、20cはダンパである。Reference numerals 20a, 20b, and 20c in the figure are dampers.

焼却炉本体10は、従来公知である乾燥火格子11及び
燃焼火格子12などが設けられている。
The incinerator body 10 is provided with a conventionally known drying grate 11, combustion grate 12, and the like.

さらに、焼却炉本体10の上部には後続設備が連設され
ている。この後続設備は、ガス冷却室15、空気予熱器
16、電気集じん器17、誘引通風機18、煙突19と
を備え、これらは上記の順にそれぞれ設けられている。
Further, the upper part of the incinerator main body 10 is connected with subsequent equipment. This subsequent equipment includes a gas cooling chamber 15, an air preheater 16, an electrostatic precipitator 17, an induced draft fan 18, and a chimney 19, which are provided in the above order.

次に、このように構成されたごみ焼却炉によるごみの焼
却について説明する。
Next, the incineration of garbage by the garbage incinerator configured as described above will be explained.

まず、平常運転時において、ホッパlに投入されたごみ
は、フィーダ2、シュート3を介して堆積部4に堆積す
る。そして、堆積部4のごみに空気予熱器21で昇温さ
れた空気を供給しごみを予備乾燥させた後、ブツシャ6
によりごみを解きほぐしながら乾燥火格子11に一定量
供給し、乾燥火格子11、燃焼火格子12へと送られ、
焼却灰として下方に排出される。
First, during normal operation, garbage put into the hopper 1 is deposited in the depositing section 4 via the feeder 2 and the chute 3. Then, air heated by the air preheater 21 is supplied to the waste in the accumulation section 4 to pre-dry the waste, and then the waste is pre-dried.
While loosening the garbage, a certain amount is supplied to the drying grate 11, and then sent to the drying grate 11 and the combustion grate 12,
It is discharged downward as incineration ash.

次に、運転停止直前においては、ブツシャ6を停止させ
、堆積部4に滞留したごみを焼却炉本体10内の放射熱
と高温の空気により燃焼させこの堆積部4で焼却灰にす
る。この燃焼時に発生したガスは上部に配設した煙路8
を経て焼却炉本体IO内に送られる。焼却炉本体10で
は残量したごみを焼却しつくすまで作業を継続している
ので、発生するガスは煙路8からきたガスとともにガス
冷却室15、空気予熱器16、電気集じん器17、誘引
通風機18を経て公害防止処理された後、煙突19から
大気中に放出される。そして、全ての燃焼が終われば開
閉ゲート7、ダンパ9を閉鎖し、堆積部4に堆積された
焼却灰をこの堆積部4で高温のまま保持する。
Next, just before the operation is stopped, the bushier 6 is stopped, and the garbage accumulated in the accumulation section 4 is burned by the radiant heat and high temperature air in the incinerator main body 10, and is turned into incinerated ash in the accumulation section 4. The gas generated during this combustion is absorbed by the smoke channel 8 installed at the top.
is sent to the incinerator main body IO. Since the work continues in the incinerator body 10 until the remaining amount of garbage is completely incinerated, the generated gas is sent to the gas cooling chamber 15, air preheater 16, electrostatic precipitator 17, and attractant along with the gas coming from the flue 8. After passing through the ventilation fan 18 and undergoing pollution prevention treatment, it is released into the atmosphere from the chimney 19. Then, when all combustion is completed, the opening/closing gate 7 and the damper 9 are closed, and the incinerated ash deposited in the depositing section 4 is held at a high temperature in the depositing section 4.

そして、翌朝の運転開始時には、まず、開閉ゲート7、
ダンパ9を開き、フィーダ2、シュート3を経て堆積部
4にごみを少量ずつ投入するとともに、壁体5内に埋設
された空気予熱器21によって昇温された空気をごみ燃
焼用として供給管20から供給すると、投入されたごみ
は即時着火する。
When the operation starts the next morning, first, open/close gate 7,
The damper 9 is opened and garbage is introduced little by little into the accumulation section 4 via the feeder 2 and the chute 3, and the air heated by the air preheater 21 buried in the wall 5 is used for combustion of the garbage through the supply pipe 20. When supplied from the source, the garbage thrown in will ignite immediately.

よって、投入するごみ量を徐々に増加してやれば火勢は
強くなりこの影響で炉内温度は上昇し始める。そして、
堆積部4に堆積した焼却灰をブツシャ6により乾燥火格
子11に徐々に送り出して行けば、堆積部4の焼却灰の
排出が終わった時点で焼却炉内の温度は十分に上昇し、
平常運転に移行できる状態になる。
Therefore, if the amount of garbage thrown in is gradually increased, the fire will become stronger and the temperature inside the furnace will begin to rise due to this effect. and,
If the incinerated ash accumulated in the accumulation section 4 is gradually sent out to the drying grate 11 by the pusher 6, the temperature inside the incinerator will rise sufficiently by the time the incineration ash from the accumulation section 4 is finished being discharged.
The state is ready for normal operation.

この場合、初期の燃焼は狭い堆積部4で行われるため昇
温時間が早く、臭気、黒煙の発生を防止することができ
る。また、平常運転へ移行するための昇温も、ごみの発
生熱で行うので、バーナによる助燃よりもはるかに早く
、電気集じん器17の稼動も早(することができる。
In this case, since the initial combustion is carried out in the narrow deposition section 4, the temperature rise time is quick, and the generation of odor and black smoke can be prevented. In addition, since the temperature rise for transitioning to normal operation is also performed using the heat generated by the waste, it is much faster than auxiliary combustion using a burner, and the electrostatic precipitator 17 can be operated quickly.

なお、焼却炉としては、ストーカ炉に限るものでなく、
例えば竪型炉などでもよい。
Incinerators are not limited to stoker furnaces.
For example, a vertical furnace may be used.

(発明の効果) 以上述べたように、本発明によれば、焼却炉本体の上流
部に該焼却炉本体よりも小容量の堆積部を設けこの堆積
部で運転初期の燃焼を行うため、運転初期に生じる臭気
、黒煙等の公害を防止することができる。また、焼却炉
内の昇温はごみの発生熱によって行うので、バーナによ
る昇温よりもはるかに早く、平常運転に速やかに移行す
ることができる。そして、流動床炉と比しても同等以上
の公害防止が可能であるだけでなく、流動床炉よりも設
備費は安く、運転、経費も節減できる。
(Effects of the Invention) As described above, according to the present invention, a depositing section with a smaller capacity than the incinerator main body is provided in the upstream part of the incinerator main body, and combustion is performed in this depositing section in the initial stage of operation. Pollution such as odors and black smoke that occur in the initial stage can be prevented. Furthermore, since the temperature inside the incinerator is raised using the heat generated by the waste, it is much faster than raising the temperature using a burner, and the incinerator can quickly return to normal operation. Not only is it possible to prevent pollution to the same degree or more than a fluidized bed furnace, but the equipment cost is lower than that of a fluidized bed furnace, and operation and expenses can be reduced.

さらに、平常運転時において、堆積部には、乾燥用の空
気が送られるとともに、ブツシャ等の供給手段によりご
みを解きほぐす動作を行うので、ごみの予備乾燥効果が
あり、これによって、焼却炉本体の火格子面積を縮少す
ることが可能になる。
Furthermore, during normal operation, drying air is sent to the accumulation section and a supply means such as a bushing is used to loosen the waste, which has the effect of pre-drying the waste. It becomes possible to reduce the grate area.

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

第1図は本発明に係るごみ焼却炉の概略構成を示す構成
図、第2図はごみ焼却炉に設けられた堆積部の概略構成
を示す構成図である。 4・・・堆積部      5・・・壁体6・・・ブツ
シャ(供給手段) lO・・・焼却炉本体 出願人 株式会社 プランテック
FIG. 1 is a block diagram showing a schematic structure of a waste incinerator according to the present invention, and FIG. 2 is a block diagram showing a schematic structure of a depositing section provided in the waste incinerator. 4... Accumulation part 5... Wall body 6... Butsusha (supply means) lO... Incinerator main body Applicant Plantech Co., Ltd.

Claims (1)

【特許請求の範囲】 1)一般廃棄物や産業廃棄物などのごみを焼却するごみ
焼却炉であって、 焼却炉本体の上流部に、投入口から投入さ れたごみを堆積する堆積部が設けられ、この堆積部は焼
却炉本体よりも小容量で且つ蓄熱性に優れ、さらに、堆
積部には、乾燥用もしくは燃焼用の気体が供給されると
ともに、該堆積部の下部に形成された排出口から焼却炉
本体にごみを供給する供給手段が設けられたことを特徴
とするごみ焼却炉。
[Scope of Claims] 1) A garbage incinerator for incinerating garbage such as general waste and industrial waste, which is provided with a depositing section in the upstream part of the incinerator main body to deposit garbage input from an input port. This stacking section has a smaller capacity than the incinerator main body and has excellent heat storage properties.Furthermore, the stacking section is supplied with drying or combustion gas, and the exhaust gas formed at the bottom of the stacking section is supplied with gas for drying or combustion. A garbage incinerator characterized by being provided with a supply means for supplying garbage from an outlet to an incinerator main body.
JP63024559A 1988-02-03 1988-02-03 Garbage incinerator Expired - Lifetime JPH0660731B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63024559A JPH0660731B2 (en) 1988-02-03 1988-02-03 Garbage incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63024559A JPH0660731B2 (en) 1988-02-03 1988-02-03 Garbage incinerator

Publications (2)

Publication Number Publication Date
JPH01200112A true JPH01200112A (en) 1989-08-11
JPH0660731B2 JPH0660731B2 (en) 1994-08-10

Family

ID=12141515

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63024559A Expired - Lifetime JPH0660731B2 (en) 1988-02-03 1988-02-03 Garbage incinerator

Country Status (1)

Country Link
JP (1) JPH0660731B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019168185A (en) * 2018-03-26 2019-10-03 Jfeエンジニアリング株式会社 Waste incinerator and waste incineration method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50113273U (en) * 1974-02-22 1975-09-16

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50113273U (en) * 1974-02-22 1975-09-16

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019168185A (en) * 2018-03-26 2019-10-03 Jfeエンジニアリング株式会社 Waste incinerator and waste incineration method

Also Published As

Publication number Publication date
JPH0660731B2 (en) 1994-08-10

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