JPH08303731A - Small size incinerator - Google Patents

Small size incinerator

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Publication number
JPH08303731A
JPH08303731A JP13586995A JP13586995A JPH08303731A JP H08303731 A JPH08303731 A JP H08303731A JP 13586995 A JP13586995 A JP 13586995A JP 13586995 A JP13586995 A JP 13586995A JP H08303731 A JPH08303731 A JP H08303731A
Authority
JP
Japan
Prior art keywords
flue
incinerator
combustion chamber
chamber
temperature
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.)
Pending
Application number
JP13586995A
Other languages
Japanese (ja)
Inventor
Katsuji Yamashita
勝治 山下
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
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 Individual filed Critical Individual
Priority to JP13586995A priority Critical patent/JPH08303731A/en
Publication of JPH08303731A publication Critical patent/JPH08303731A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE: To permit complete combustion at a low temperature without enlarging the occupying volume of an incinerator. CONSTITUTION: This small size incinerator 1 is provided with an incinerating chamber 2, incinerating wastes, a combustion chamber 3, provided above the incinerating chamber 2 to burn unburnt gas generated out of the incinerating chamber 2, a first flue 4, pinched between the ceiling of the incinerating chamber 2 and the floor of the combustion chamber 3, a second flue 5, neighbored to the ceiling of the combustion chamber 3, a third flue 6, neighbored to the wall of the incinerating chamber 2 and communicated with the incinerating chamber 2 as well as the first flue 4, and a fourth flue 7, beighbored to the wall, of the combustion chamber 3 and communicated with the combustion chamber 3 as well as the second flue 5.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、小型焼却炉に関す
る。この小型焼却炉は、医療廃棄物や高分子化合物を低
温で完全燃焼させる場合に好適に利用されうる。
FIELD OF THE INVENTION The present invention relates to a small incinerator. This small incinerator can be suitably used for completely burning medical waste and polymer compounds at low temperatures.

【0002】[0002]

【従来の技術】廃ガスから黒煙や硫黄酸化物、窒素酸化
物、塩化水素などを減少させるためには完全燃焼させる
しかなく、既存の焼却炉は概ね次のような方法で完全燃
焼しようとしている。
2. Description of the Related Art In order to reduce black smoke, sulfur oxides, nitrogen oxides, hydrogen chloride, etc. from waste gas, there is no choice but to completely burn them, and existing incinerators generally try to burn them by the following methods. There is.

【0003】すなわち、小型焼却炉で焼却するものは、
通常、紙、木片、プラスティック、布切れなどの固体が
大部分である。これらの燃焼は、それら固体の大部分が
熱分解によりガスとなって放出されそのガスが燃焼する
ものである。このガス状態の成分の大半は炭素と水素か
らできている炭化水素である。そして、水素の方が炭素
より燃焼性がはるかによいため、よほど燃焼条件が良く
ないと水素だけ燃えてしまい、あとに未燃の炭素が残
り、黒煙となる。一度未燃炭素が生成されると、同じ焼
却室内で再燃焼することは困難である。
That is, what is incinerated in a small incinerator is
The majority are usually solids such as paper, wood chips, plastics, and pieces of cloth. In these combustions, most of the solids are released as gas by thermal decomposition and the gas burns. Most of the components in this gaseous state are hydrocarbons composed of carbon and hydrogen. And, since hydrogen has far better flammability than carbon, if the combustion conditions are not so good, only hydrogen will burn, and unburned carbon will remain and become black smoke. Once unburned carbon is produced, it is difficult to reburn in the same incinerator.

【0004】そこで、多くの小型焼却炉では、先ず焼却
物を焼却室のバーナーで燃焼し、そこで発生した未燃ガ
ス(主として炭素ガス)を煙道を経由させて未燃ガス燃
焼室に送り、アフターバーナーで完全燃焼していた。す
なわち、炉が2個装備されていた。この場合、焼却物の
燃焼力を高めるため、或いは排出した未燃ガスを完全燃
焼に近ずけるためには、一定の温度(高温)、混合され
た空気(酸素)と未燃ガス、これら三つの燃焼条件が整
備されることが必要である。
Therefore, in many small incinerators, the incinerator is first burned by the burner in the incinerator, and the unburned gas (mainly carbon gas) generated there is sent to the unburned gas combustion chamber via the flue. It was completely burned by the afterburner. That is, it was equipped with two furnaces. In this case, in order to increase the burning power of the incinerated material or to bring the discharged unburned gas close to complete combustion, a constant temperature (high temperature), mixed air (oxygen) and unburned gas, these three One combustion condition needs to be prepared.

【0005】一方、小型焼却炉の焼却においては、出来
る限り低温で無煙焼却することが、炉の延命化、炉の亀
裂もしくは爆発の防止、焼却物の入れ替え時間の短縮
化、燃料の節約及び行政指導等の点で望ましい。特に特
別管理廃棄物に属する感染性医療廃棄物の焼却に際して
は、出口温度を概ね800℃にしてから廃棄物を焼却す
るように感染性医療廃棄物処理のガイドラインで義務づ
けられている。従って、このような特殊な廃棄物は、8
00℃を安定的にクリアーしたうえで、なるべく高温に
ならないように無煙焼却することが望ましい。
On the other hand, in the incineration of a small incinerator, smokeless incineration at a temperature as low as possible prolongs the life of the furnace, prevents cracking or explosion of the furnace, shortens the replacement time of the incineration material, saves fuel and administers. It is desirable in terms of instruction. In particular, when incinerating infectious medical waste that belongs to specially controlled waste, the guidelines for treating infectious medical waste require that the outlet temperature be set to approximately 800 ° C. before incinerating the waste. Therefore, such special waste is 8
It is desirable to steadily clear the temperature of 00 ° C and then smokelessly incinerate it so that the temperature does not rise as high as possible.

【0006】[0006]

【発明が解決しようとする課題】しかし、焼却炉でゴミ
を焼却する際に発生する未燃ガスをアフターバーナーを
装置した未燃ガス燃焼室で完全燃焼して煙を出さなくす
るためには、適度な空気と一定のかなりの高温が必要で
ある。特に、塩化ビニール、合成ゴムなど大量の黒煙を
排出する廃棄物を無煙焼却しようとすれば通常1300
℃以上の温度を必要としているようである。(空気との
混合具合によりかなりの差がある。)加えて、焼却物そ
のものが燃焼される際に高熱エネルギーを発生する場合
も多い。
However, in order to completely burn the unburned gas generated when incinerating waste in an incinerator in an unburned gas combustion chamber equipped with an afterburner to prevent smoke emission, it is appropriate. It requires clean air and a constant high temperature. Especially, if you try to smokelessly incinerate a large amount of black smoke such as vinyl chloride and synthetic rubber, it is usually 1300.
It seems that it needs a temperature above ℃. (There is a considerable difference depending on the degree of mixing with air.) In addition, high heat energy is often generated when the incinerator itself is burned.

【0007】また、感染性廃棄物等では、感染の危険が
あるので分別したり、中身を確認することが不可能な場
合も多い。このため、溶剤などの高可燃物を含む種々雑
多な廃棄物が混在し、しかもプラスティック容器などに
厳封されて、これを開封することが禁じられているよう
な廃棄物を無煙で焼却しようとするときなどでは、とも
すれば、1500℃を超え2000℃近くなり、爆裂の
危険が生じるような異常な高温になる場合も珍しくな
い。
[0007] Infectious waste and the like often cannot be separated or the contents thereof cannot be confirmed because of the risk of infection. For this reason, various miscellaneous wastes including highly flammable materials such as solvents are mixed, and the wastes that are strictly sealed in plastic containers and forbidden to open are to be smokelessly incinerated. At times, it is not uncommon for the temperature to exceed 1500 ° C. and approach 2000 ° C., resulting in an abnormally high temperature that may cause explosion.

【0008】かといって、従来の小型焼却炉において
は、どうしても空気と未燃ガスが混合するスペースや、
煙道の長さが制約される。また、それらの設備を別に設
ければ、今度は空気と混合した未燃ガスの温度が下が
り、結局、未燃ガスが燃焼室で不完全燃焼になりやす
く、黒煙発生の原因になる。
However, in the conventional small incinerator, the space where air and unburned gas are mixed,
The length of the flue is limited. Further, if these facilities are separately provided, the temperature of the unburned gas mixed with the air is lowered, and the unburned gas is likely to be incompletely burned in the combustion chamber, which causes black smoke.

【0009】それゆえ、この発明の目的は、炉の占有体
積を拡大することなく、低温で完全燃焼させることを可
能にする小型焼却炉を提供することにある。
Therefore, it is an object of the present invention to provide a small incinerator which enables complete combustion at a low temperature without increasing the occupied volume of the furnace.

【0010】[0010]

【課題を解決するための手段】その目的を達成するため
に、この発明の小型焼却炉は、廃棄物を焼却する焼却室
と、焼却室の上方に設けられて、焼却室から発生する未
燃ガスを燃焼する燃焼室と、焼却室の天井と燃焼室の床
とで挟まれる煙道(以下、「第一の煙道」という。)と
を備えたことを特徴とする。
In order to achieve the object, a small-sized incinerator according to the present invention is provided with an incinerator for incinerating waste and an unburned gas generated from the incinerator provided above the incinerator. It is characterized by including a combustion chamber for burning gas and a flue (hereinafter, referred to as “first flue”) sandwiched between the ceiling of the incinerator and the floor of the combustion chamber.

【0011】この小型焼却炉において、燃焼室の天井に
隣接する第二の煙道を備えていると好ましい。更に好ま
しいのは、焼却室の壁に隣接し、焼却室及び第一の煙道
に連通する第三の煙道と、燃焼室の壁に隣接し、燃焼室
及び第二の煙道に連通する第四の煙道とを備えているも
のである。最も好ましいのは、第三の煙道及び第四の煙
道が、それぞれ焼却室及び燃焼室の各壁と交差する上下
方向の仕切りにて分割され、未燃ガスが第三の煙道内及
び第四の煙道内で仕切りを介して上下方向に往復するよ
うにしたものである。第三の煙道内及び第四の煙道内に
は、突起を設けてもよい。
In this small incinerator, it is preferable to provide a second flue adjacent to the ceiling of the combustion chamber. More preferred is a third flue adjacent to the wall of the incinerator and in communication with the incinerator and the first flue, and adjacent to the wall of the combustion chamber and in communication with the combustion chamber and the second flue. It is equipped with a fourth flue. Most preferably, the third flue and the fourth flue are divided by vertical partitions that intersect the walls of the incinerator and combustion chamber, respectively, and the unburned gas is in the third flue and the third flue. It is designed to reciprocate up and down in the flue through a partition. Protrusions may be provided in the third flue and the fourth flue.

【0012】[0012]

【作用】無煙燃焼は、以下の3条件を満たすことで達成
される。 <空気>小型焼却炉では通常空気は大量にあるため、煤
煙(黒煙)防止の決め手の一つは両者を良く混合するこ
とである。空気と良く混合した可燃性ガスは燃焼速度が
速く、火炎は短くなる。反対に空気と良く混合していな
い火炎は長くなる。火炎が長くなると火炎面が放射冷却
され、燃焼性の良い水素だけ燃焼し、燃焼性の悪い炭素
が残り黒煙となる。さらに、火炎が長くなると炉壁にあ
たり、やはり冷却されて黒煙が発生することとなる。
The smokeless combustion is achieved by satisfying the following three conditions. <Air> In a small incinerator, there is usually a large amount of air, so one of the decisive factors for preventing soot (black smoke) is to mix both well. Combustible gas mixed well with air has a high burning velocity and a short flame. Conversely, flames that do not mix well with air will be longer. When the flame becomes longer, the flame surface is radiatively cooled and only hydrogen with good flammability burns, leaving carbon with poor flammability as black smoke. Furthermore, when the flame becomes long, it hits the furnace wall and is cooled, and black smoke is generated.

【0013】<温度>燃焼室内の温度をある一定以上の
状態にしておけば、煤煙の発生を防ぐことができる。燃
焼室温度は熱分解ガスの燃焼によって生じるものである
が、熱分解によるガス発生が一定でないため、燃焼もそ
れに従って大きく変動する。そのため燃焼室内の温度も
著しく変動し、一時的でも温度が低下すると、ガスの一
部は不完全燃焼して煤煙を発生する。しかし燃焼が激し
くなり炉内の温度が上昇すると、煤煙の発生は徐々に解
消する。
<Temperature> If the temperature in the combustion chamber is kept above a certain level, the generation of soot can be prevented. The combustion chamber temperature is generated by the combustion of pyrolysis gas, but since the gas generation due to pyrolysis is not constant, the combustion also fluctuates accordingly. Therefore, the temperature in the combustion chamber also fluctuates remarkably, and when the temperature drops temporarily, a part of the gas is incompletely burned to generate soot. However, if the combustion becomes violent and the temperature inside the furnace rises, the generation of soot will gradually disappear.

【0014】<時間>ガスと空気が一定時間燃焼室内に
滞留すると煤煙発生はみられなくなる。これは、ガスと
空気の混合を良くし、これらの温度を上昇させるのに必
要な時間である。通常空気は炉外から直接導入される
が、火炎に対しては火炎面の冷却効果を持つため、しば
しば煤煙発生の原因になる。従って、燃焼室内、又は煙
道で燃焼ガスの温度をできるだけ下降させず、空気とガ
スが充分混合する滞留時間を持つような構造が必要であ
る。
<Time> If the gas and air stay in the combustion chamber for a certain period of time, no soot is generated. This is the time required to get a good mix of gas and air and to raise their temperature. Normally, air is introduced directly from the outside of the furnace, but since it has a cooling effect on the flame surface for flames, it often causes soot and smoke. Therefore, it is necessary to have a structure in which the temperature of the combustion gas is not lowered as much as possible in the combustion chamber or the flue and the residence time is such that the air and the gas are sufficiently mixed.

【0015】この発明の小型焼却炉は、焼却室の天井と
燃焼室の床とで挟まれる空間を煙道としているので、焼
却室及び燃焼室の熱が、それぞれ天井及び床を伝導して
煙道に供給される。従って、炉外から新たな熱エネルギ
ーを供給しなくても煙道の温度が上がり、上記温度条件
を充足する。
In the small incinerator according to the present invention, the space between the ceiling of the incinerator and the floor of the combustion chamber is used as the flue, so that the heat of the incinerator and the combustion chamber is conducted through the ceiling and floor to produce smoke. Supplied on the road. Therefore, the temperature of the flue rises without supplying new heat energy from outside the furnace, and the above temperature condition is satisfied.

【0016】燃焼室の天井に隣接する第二の煙道を備え
ていれば、燃焼室でも残った未燃ガスが完全に燃焼す
る。上記のように第三の煙道を備えていれば、未燃ガス
が第一の煙道に送られる前に第三の煙道において、充分
時間をかけて空気と混合され、且つ焼却室の壁を介して
焼却室から伝わる熱で予熱されるので、第一の煙道で自
然燃焼が起こる。同じく第四の煙道を備えていれば、残
った未燃ガスが第二の煙道に送られる前に第四の煙道に
おいて、充分時間をかけて空気と混合され、且つ燃焼室
の壁を介して燃焼室から伝わる熱で予熱されるので、第
二の煙道で自然燃焼が起こる。
If the second flue adjacent to the ceiling of the combustion chamber is provided, the unburned gas remaining in the combustion chamber is completely burned. If a third flue is provided as described above, the unburned gas will be mixed with the air in the third flue for a sufficient amount of time before being sent to the first flue and in the incinerator. It is preheated by the heat transferred from the incinerator through the walls, so spontaneous combustion occurs in the first flue. Also with a fourth flue, the remaining unburned gas is mixed with air in the fourth flue for a sufficient time before being sent to the second flue, and the walls of the combustion chamber are It is preheated by the heat transferred from the combustion chamber via the so that spontaneous combustion occurs in the second flue.

【0017】第三の煙道及び第四の煙道が、それぞれ焼
却室及び燃焼室の各壁と交差する上下方向の仕切りにて
分割され、未燃ガスが第三の煙道内及び第四の煙道内で
仕切りを介して上下方向に往復するようにしてあれば、
更に空気との混合時間及び予熱時間が長くなり、上記3
条件に適合する。
The third flue and the fourth flue are divided by vertical partitions that intersect the walls of the incinerator and the combustion chamber, respectively, and the unburned gas is in the third flue and the fourth flue. If you are going to reciprocate vertically through the partition in the flue,
Furthermore, the mixing time with air and the preheating time become longer,
Meets the conditions.

【0018】[0018]

【実施例】この発明の実施例の小型焼却炉を図面ととも
に説明する。図1は、小型焼却炉の骨組みを示す斜視
図、図2は小型焼却炉を示す断面図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS A small incinerator according to an embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a perspective view showing a framework of a small incinerator, and FIG. 2 is a sectional view showing the small incinerator.

【0019】小型焼却炉1は、廃棄物を焼却する焼却室
2と、焼却室2の上方に設けられて、焼却室2から発生
する未燃ガスを燃焼する燃焼室3と、焼却室2の天井と
燃焼室3の床とで挟まれる第一煙道4と、燃焼室3の天
井に隣接する第二煙道5と、焼却室2の壁に隣接し、焼
却室2及び第一煙道4に連通する第三煙道6と、燃焼室
3の壁に隣接し、燃焼室3及び第二煙道に連通する第四
煙道7とを備えている。
The small incinerator 1 comprises an incineration chamber 2 for incinerating waste, a combustion chamber 3 provided above the incineration chamber 2 for burning unburned gas generated from the incineration chamber 2, and an incineration chamber 2. The first flue 4 sandwiched between the ceiling and the floor of the combustion chamber 3, the second flue 5 adjacent to the ceiling of the combustion chamber 3, and the wall of the incineration chamber 2 adjacent to the incineration chamber 2 and the first flue. A third flue 6 communicating with 4 and a fourth flue 7 adjacent to the wall of the combustion chamber 3 and communicating with the combustion chamber 3 and the second flue.

【0020】焼却室2及び燃焼室3の一側面には、それ
ぞれメインバーナー21及びアフターバーナー31が固
定されている。そして、各バーナーの近くに温度センサ
ー22,32及び空気取り入れ口23,33が併置され
ている。温度センサー22,32は焼却室2の反対側面
に設けられた制御器8に接続して温度信号を送ってい
る。
A main burner 21 and an afterburner 31 are fixed to one side surface of the incineration chamber 2 and the combustion chamber 3, respectively. Further, the temperature sensors 22 and 32 and the air intake ports 23 and 33 are arranged in parallel near each burner. The temperature sensors 22 and 32 are connected to a controller 8 provided on the opposite side of the incineration chamber 2 to send a temperature signal.

【0021】第三煙道6及び第四煙道7は、それぞれ焼
却室2及び燃焼室3の各壁と交差する上下方向の仕切り
61,71にて分割され、未燃ガスが第三煙道内及び第
四煙道内で仕切り61,71を介して上下方向に往復す
るようになっている。
The third flue 6 and the fourth flue 7 are divided by vertical partitions 61 and 71 which intersect the respective walls of the incineration chamber 2 and the combustion chamber 3, respectively, and unburned gas is contained in the third flue. In the fourth flue, it reciprocates in the vertical direction via partitions 61 and 71.

【0022】焼却室2、燃焼室3及び各煙道4〜7の内
外面は、耐熱材料にて形成されている。第二煙道の上方
には、第二煙道及び外気に連通する煙突9が設けられて
いる。この小型焼却炉を用いて、廃棄物を焼却する場
合、以下の手順をとる。
The inner and outer surfaces of the incineration chamber 2, the combustion chamber 3 and the flues 4 to 7 are made of a heat resistant material. A chimney 9 that communicates with the second flue and the outside air is provided above the second flue. When incinerating waste using this small incinerator, follow the procedure below.

【0023】(1)焼却室2背面の扉24(図1では省
略)を開けて、焼却物を焼却室2に投入する。焼却室2
内及び燃焼室3内の燃焼温度の上限を1000℃以内に
制御させる。すなわち、温度センサー22,32が10
00℃を検知すれば、各バーナー21,31の燃料は一
時停止し送風だけ行う。その間、燃焼物は余熱で燃焼す
る。炉温が徐々に下降し、あらかじめ黒煙のでない最低
温度に任意設定してある温度になれば再びバーナー2
1,31が点火し1000℃(感染性医療廃棄物の場合
には設定温度800℃)まで燃焼して停止する。これを
順次繰り返す。
(1) The door 24 (not shown in FIG. 1) on the rear surface of the incineration chamber 2 is opened and the incinerator is put into the incineration chamber 2. Incineration room 2
The upper limit of the combustion temperature inside and inside the combustion chamber 3 is controlled within 1000 ° C. That is, the temperature sensors 22 and 32 are 10
When the temperature of 00 ° C. is detected, the fuel in each burner 21, 31 is temporarily stopped and only the air is blown. Meanwhile, the combusted material burns with residual heat. When the furnace temperature gradually drops and reaches a temperature that has been arbitrarily set to the minimum temperature without black smoke in advance, the burner 2 is restarted.
1,31 ignite and burn up to 1000 ° C (set temperature 800 ° C for infectious medical waste) and stop. This is repeated sequentially.

【0024】(2)未燃ガスは、焼却室2の天井付近に
設けられた孔25を通じて第三煙道6に流れる。未燃ガ
スは、仕切り61の向こう側の空間を下降し、下端に達
したところで仕切り61の孔62を通過して手前側空間
を上昇する。その間、未燃ガスは焼却室2の壁面と常に
接触している。このように焼却室2の壁面を幅広く利用
した第三煙道を通過する未燃ガスは、焼却室2の放射熱
ですぐにその温度が上昇する。都合によって第三煙道6
の内部に適宜突起物(図示省略)を配設することで未燃
ガスと空気の混合を容易にし、且つガスの経路を折り曲
げて、それらが十分に混合し、昇温するための滞留時間
を与える。
(2) The unburned gas flows into the third flue 6 through the hole 25 provided near the ceiling of the incinerator 2. The unburned gas descends in the space on the other side of the partition 61 and, when reaching the lower end, passes through the hole 62 of the partition 61 and rises in the space on the front side. During that time, the unburned gas is constantly in contact with the wall surface of the incineration chamber 2. As described above, the temperature of the unburned gas passing through the third flue that widely uses the wall surface of the incinerator 2 is immediately increased by the radiant heat of the incinerator 2. Third flue 6 due to circumstances
By appropriately arranging protrusions (not shown) inside, the unburned gas and the air can be easily mixed, and the gas path is bent so that they are sufficiently mixed and the residence time for raising the temperature is increased. give.

【0025】(3)空気と十分に混合され昇温した未燃
ガスは、やがて第三煙道上端の孔62を通過して焼却室
2天井と燃焼室3床に挟まれた第一煙道4に達する。こ
の場所は2個の炉すなわち焼却室2と燃焼室3の放射熱
が重複し、炉内温度にほぼ匹敵する程の高温部である。
従って、全ての煙道の中で最初にここで未燃ガスは自然
発火し、継続的に燃焼が生じる。燃焼しながら第三煙道
6と反対側端部上方の孔34から燃焼室3へ流入しアフ
ターバーナー31でさらに燃焼が促進される。燃焼室3
で無煙化された排気ガスは、燃焼室3の天井付近に設け
られた孔35を通過して第三煙道6と同じ構造の第四煙
道7に入り、(2)と同じ要領で十分混合し、昇温され
る。
(3) The unburned gas, which has been sufficiently mixed with air and heated, passes through the hole 62 at the upper end of the third flue and eventually is sandwiched between the incineration chamber 2 ceiling and the combustion chamber 3 floor. Reach 4. This place is a high temperature part where the radiant heat of the two furnaces, that is, the incineration chamber 2 and the combustion chamber 3 overlap, and is almost comparable to the temperature inside the furnace.
Therefore, of all the flues, the unburned gas is now spontaneously ignited here, with continuous combustion occurring. While burning, it flows into the combustion chamber 3 through the hole 34 above the end opposite to the third flue 6, and the combustion is further promoted by the afterburner 31. Combustion chamber 3
The smoke-free exhaust gas passes through the hole 35 provided in the vicinity of the ceiling of the combustion chamber 3 and enters the fourth flue 7 having the same structure as the third flue 6, and the same procedure as (2) is sufficient. Mix and heat up.

【0026】(4)続いて、十分混合され昇温した排気
ガスは、燃焼室3の天井裏面の高温部の第二煙道を通過
する。もしこの際に、排気ガス中に炭素(黒煙)が残存
しておれば再び自然発火して燃焼が起こる。こうして煙
突9から排出されるガスは、無煙無臭化される。
(4) Subsequently, the exhaust gas, which is sufficiently mixed and heated, passes through the second flue at the high temperature portion on the back surface of the ceiling of the combustion chamber 3. At this time, if carbon (black smoke) remains in the exhaust gas, spontaneous combustion will occur again and combustion will occur. Thus, the gas discharged from the chimney 9 is made smokeless and odorless.

【0027】この実施例の小型焼却炉によれば、煙道の
熱エネルギーとして、焼却室又は燃焼室からの放射伝導
熱を利用しているので、外部から熱エネルギーを供給し
なくても煙道が加熱される。従って、焼却室及び燃焼室
自体の温度が1000℃を越えない低温でも完全燃焼さ
せることができる。よって、以下のように多大の効果を
生じる。
According to the small incinerator of this embodiment, the radiative conduction heat from the incinerator or the combustion chamber is used as the heat energy of the flue, so that the flue does not have to be supplied with heat energy from the outside. Is heated. Therefore, even if the temperature of the incineration chamber and the combustion chamber itself does not exceed 1000 ° C., complete combustion can be achieved. Therefore, a great effect is produced as follows.

【0028】(1)炉材の許容温度に余裕ができ、炉の
寿命が大幅に延びる。 (2)設定温度が低いので、亀裂を起こしたり爆裂する
ような心配がなく安全である。また、高温燃焼時に炉材
がガラス化して噴出するクリンカの形成も少ない。従っ
て、炉材の保守管理が安易になり維持費が安くなる。 (3)冷却時間が短縮されるため、次の焼却物を投入す
る待ち時間が少なくてすむ。ひいては1日の焼却稼働回
数が増加する。 (4)従前より高熱エネルギーのバーナーを必要とせ
ず、商品代金もそれだけ安価である。同様に燃費も大き
く節約できる。 (5)焼却されるゴミを分別する必要がなく、多目的に
幅広く使用できる。
(1) There is a margin in the allowable temperature of the furnace material, and the life of the furnace is greatly extended. (2) Since the set temperature is low, there is no risk of cracking or explosion, which is safe. Further, there is little formation of clinker that vitrifies and ejects the furnace material during high temperature combustion. Therefore, the maintenance management of the furnace material becomes easy and the maintenance cost becomes low. (3) Since the cooling time is shortened, the waiting time for inputting the next incinerated material can be reduced. As a result, the number of incineration operations per day will increase. (4) It does not require a burner with high heat energy and the product price is lower than before. Similarly, fuel consumption can be greatly saved. (5) There is no need to separate the incinerated waste, and it can be widely used for multiple purposes.

【0029】[0029]

【発明の効果】以上のように、この発明の小型焼却炉
は、焼却室及び燃焼室に煙道を接近させ、それら各室の
熱を効率よく煙道に利用しているので、炉全体の占有体
積を増やすことなく、廃棄物を低温で完全燃焼させるこ
とができる。
INDUSTRIAL APPLICABILITY As described above, in the small incinerator of the present invention, the flues are brought close to the incinerator and the combustion chamber, and the heat in each of these chambers is efficiently used for the flue. The waste can be completely combusted at low temperature without increasing the occupied volume.

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

【図1】実施例の小型焼却炉の骨組みを示す斜視図であ
る。
FIG. 1 is a perspective view showing a framework of a small incinerator according to an embodiment.

【図2】上記小型焼却炉の断面図である。FIG. 2 is a sectional view of the small incinerator.

【符号の説明】[Explanation of symbols]

1 小型焼却炉 2 焼却室 3 燃焼室 4 第一煙道 5 第二煙道 6 第三煙道 7 第四煙道 8 制御器 9 煙突 1 small incinerator 2 incinerator 3 combustion chamber 4 first flue 5 second flue 6 third flue 7 fourth flue 8 controller 9 chimney

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F23G 5/50 ZAB F23G 5/50 ZABH ZABJ ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location F23G 5/50 ZAB F23G 5/50 ZABH ZABJ

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物を焼却する焼却室と、焼却室の上
方に設けられて、焼却室から発生する未燃ガスを燃焼す
る燃焼室と、焼却室の天井と燃焼室の床とで挟まれる煙
道(以下、「第一の煙道」という。)とを備えたことを
特徴とする小型焼却炉。
1. An incineration chamber for incinerating waste, a combustion chamber provided above the incineration chamber for burning unburned gas generated from the incineration chamber, a ceiling of the incineration chamber, and a floor of the combustion chamber. A small incinerator characterized by having a flue (hereinafter referred to as the "first flue").
【請求項2】 燃焼室の天井に隣接する第二の煙道を更
に備えた請求項1に記載の小型焼却炉。
2. The miniature incinerator according to claim 1, further comprising a second flue adjacent to the ceiling of the combustion chamber.
【請求項3】 焼却室の壁に隣接し、焼却室及び第一の
煙道に連通する第三の煙道と、燃焼室の壁に隣接し、燃
焼室及び第二の煙道に連通する第四の煙道とを更に備え
た請求項2に記載の小型焼却炉。
3. A third flue adjacent to the wall of the incinerator and in communication with the incinerator and the first flue, and adjacent to the wall of the combustion chamber and in communication with the combustion chamber and the second flue. The small incinerator according to claim 2, further comprising a fourth flue.
【請求項4】 第三の煙道及び第四の煙道が、それぞれ
焼却室及び燃焼室の各壁と交差する上下方向の仕切りに
て分割され、未燃ガスが第三の煙道内及び第四の煙道内
で仕切りを介して上下方向に往復するようにした請求項
3に記載の小型焼却炉。
4. The third flue and the fourth flue are divided by vertical partitions that intersect the respective walls of the incinerator and the combustion chamber, and unburned gas is contained in the third flue and the third flue. The small incinerator according to claim 3, wherein the small incinerator is configured to reciprocate in the vertical direction through a partition in the fourth flue.
【請求項5】 第三の煙道内及び第四の煙道内に突起を
設けた請求項3又は4に記載の小型焼却炉。
5. The small incinerator according to claim 3, wherein projections are provided in the third flue and the fourth flue.
JP13586995A 1995-05-08 1995-05-08 Small size incinerator Pending JPH08303731A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13586995A JPH08303731A (en) 1995-05-08 1995-05-08 Small size incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13586995A JPH08303731A (en) 1995-05-08 1995-05-08 Small size incinerator

Publications (1)

Publication Number Publication Date
JPH08303731A true JPH08303731A (en) 1996-11-22

Family

ID=15161677

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13586995A Pending JPH08303731A (en) 1995-05-08 1995-05-08 Small size incinerator

Country Status (1)

Country Link
JP (1) JPH08303731A (en)

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