JPH01142313A - Incinerator - Google Patents
IncineratorInfo
- Publication number
- JPH01142313A JPH01142313A JP30234087A JP30234087A JPH01142313A JP H01142313 A JPH01142313 A JP H01142313A JP 30234087 A JP30234087 A JP 30234087A JP 30234087 A JP30234087 A JP 30234087A JP H01142313 A JPH01142313 A JP H01142313A
- Authority
- JP
- Japan
- Prior art keywords
- combustion chamber
- gas
- waste
- secondary combustion
- combustion
- 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
Links
- 238000002485 combustion reaction Methods 0.000 claims abstract description 109
- 239000002699 waste material Substances 0.000 claims abstract description 24
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000005485 electric heating Methods 0.000 abstract description 5
- 238000004056 waste incineration Methods 0.000 abstract 1
- 239000000446 fuel Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000011144 upstream manufacturing Methods 0.000 description 5
- 239000004071 soot Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000006096 absorbing agent Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000010849 combustible waste Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、家庭あるいは業務上発生する生ごみ、古紙、
し尿等の可燃性廃棄物の焼却装置に関する。[Detailed Description of the Invention] Industrial Application Field The present invention is applicable to kitchen waste, waste paper, etc. generated at home or in business.
Related to incineration equipment for combustible waste such as human waste.
従来の技術
焼却装置としてガス燃料、液体燃料を用いろ焼却装置が
ある。これは燃料をバーナて燃焼し、その熱で廃棄物を
焼却してしまうものである。また、新しい提案としてヒ
ータ、マグネトロンのような電力を加熱源として備えた
焼却装置がある。Conventional technology incinerators include incinerators that use gas fuel or liquid fuel. This burns fuel and uses the heat to incinerate waste. In addition, as a new proposal, there is an incinerator equipped with electric power such as a heater or magnetron as a heating source.
燃料で廃棄物を焼却する方法は、装置が複雑で大型であ
る欠点を持つ、これに対して電力加熱部を備えた焼却装
置は小型でかつ、制御性に優れたものとなる。しかしこ
の電力加熱方式は燃料を用いた方式と較べて、燃焼部の
温度が低く臭気、ススが発生しやすい欠点があるもので
あった。The method of incinerating waste with fuel has the disadvantage that the device is complicated and large.In contrast, an incinerator equipped with an electric heating section is small and has excellent controllability. However, compared to methods using fuel, this electric heating method has the disadvantage that the temperature of the combustion part is low and odor and soot are easily generated.
廃棄物を完全燃焼する方法は一般に次のようなものであ
る。まず廃棄物は電気、ガス、石油のような補助熱源で
乾燥したのち、これらの熱で着火させる。着火したのち
は主に自熱で分解して分解ガス燃焼をおこなう。分解が
終了したのち残った炭化物を燃焼する。このような段階
を踏んだ燃焼制御が望ましいが、分解ガスは燃焼しにく
いものであり臭気が発生しやすい。The methods for completely burning waste are generally as follows. The waste is first dried using auxiliary heat sources such as electricity, gas, or oil, and then ignited using this heat. After being ignited, it decomposes mainly using its own heat and burns the decomposed gas. After the decomposition is complete, the remaining carbide is burned. Although such stepwise combustion control is desirable, cracked gas is difficult to burn and tends to generate odor.
この理由は廃棄物の分解ガスの濃度は着火時、燃焼末期
は薄くなって、燃焼空気と混合して希釈され燃えにくく
、また、分割ガスが濃い場合は燃焼空気が少ないとスス
がでるものである。このような燃焼中の廃棄物の分解ガ
スの濃度は一定しにくいので、燃焼しにくくスス、臭気
が発生しやすくなる。The reason for this is that the concentration of waste decomposition gas becomes thinner at the time of ignition and at the end of combustion, and when mixed with combustion air, it is diluted and becomes difficult to burn.Also, if the split gas is concentrated, soot will be produced if there is little combustion air. be. Since the concentration of decomposed gas from such waste during combustion is difficult to maintain, combustion is difficult and soot and odor are easily generated.
発明が解決しようとする問題点
このように電力加熱手段を持つ焼却の装置は小型化可能
となるが、廃棄物の燃焼熱は一般に低く、ガス、石油等
の補助燃料を用いる場合に比べて排気の臭気が強くなる
欠点が生じる。Problems to be Solved by the Invention In this way, incineration equipment with electric heating means can be made smaller, but the heat of combustion of waste is generally low, and the exhaust gas is lower than when using auxiliary fuels such as gas or oil. The disadvantage is that the odor becomes stronger.
本発明は上記従来技術に鑑み、電力加熱方式の焼却装置
において排気臭気を小さくす、ることを目的とする。SUMMARY OF THE INVENTION In view of the above-mentioned prior art, an object of the present invention is to reduce exhaust odor in an electric heating type incinerator.
問題点を解決するための手段
本発明は、廃棄物を収納する一次燃焼室と、前記−次席
焼室に燃焼用の空気を供給する手段と、前記−次席焼室
の廃棄物を加熱する手段と、前記−次席焼室の下流に設
けられた多段に分割された二次燃焼室を有するもので、
前記二次燃焼室の第1段燃焼室には着火手段、および燃
焼空気の供給孔と、前記−次席焼室に開口するガス通過
孔を有し、第2段燃焼室以下には前記第1段燃焼室より
多数の燃焼空気孔を設け、かつそれぞれの二次燃焼室が
中央に間口を有する制炎板で仕切られている構成とする
ものである。Means for Solving the Problems The present invention provides a primary combustion chamber for storing waste, means for supplying combustion air to the secondary combustion chamber, and means for heating the waste in the secondary combustion chamber. and a secondary combustion chamber divided into multiple stages provided downstream of the secondary combustion chamber,
The first stage combustion chamber of the secondary combustion chamber has an ignition means, a combustion air supply hole, and a gas passage hole opening to the secondary combustion chamber, and the second stage combustion chamber and below have the first stage combustion chamber. A larger number of combustion air holes are provided than the stage combustion chambers, and each secondary combustion chamber is partitioned by a flame control plate having an opening in the center.
作用
このような構成の本発明の焼却装置では、−次席焼室の
分解ガス量が一定化しやすい。これは気化する所と、燃
焼する所を位置的にも、熱的にも分離しているとともに
、分解ガスが大量に発生している時は、強い発火を抑制
するため一次空気量は少なくし、ガスの搬送に足りる程
度としているためである。Function: In the incinerator of the present invention having such a configuration, the amount of decomposed gas in the secondary incineration chamber can be easily stabilized. This separates the vaporization area from the combustion area both physically and thermally, and when a large amount of decomposed gas is generated, the amount of primary air is reduced to suppress strong ignition. , this is because it is sufficient for transporting gas.
このため主燃焼部である二次燃焼室には比較的濃い分解
ガスが送られ、着火時、燃焼末期も燃え易い。また、二
次燃焼室は多段に分割されており、上流の燃焼室は小微
の空気が供給されているのでガスは濃く燃焼しやすい。For this reason, a relatively concentrated decomposed gas is sent to the secondary combustion chamber, which is the main combustion part, and it is easy to burn at the time of ignition and at the final stage of combustion. In addition, the secondary combustion chamber is divided into multiple stages, and the upstream combustion chamber is supplied with a small amount of air, so the gas is concentrated and burns easily.
下流の燃焼室は二次空気が多黴に供給されているが、こ
の下流の二次空気は制炎板で規制され1流の二次燃焼室
を薄めることはない。燃焼量が増加した時この下流の燃
焼室で完全燃焼するものである。The downstream combustion chamber is supplied with a large amount of secondary air, but this downstream secondary air is regulated by a flame control plate and does not dilute the first-flow secondary combustion chamber. When the amount of combustion increases, complete combustion occurs in this downstream combustion chamber.
実施例
図は本発明の一実施例の焼却装置の断面図である。図に
おいてlは一次燃焼室である。−次席焼室1の前部には
廃棄物の人口rs2が設けられている。廃棄物は一次燃
焼室1に設けられた受は皿3に入れられている。この受
は皿3の一部は炭化珪素のような電波吸収体4が設けら
れている。また−次席焼室lの側壁の開口5はマグネト
ロン6の発信部と導波管7で連通している。The embodiment diagram is a sectional view of an incinerator according to an embodiment of the present invention. In the figure, l is the primary combustion chamber. - In the front part of the secondary baking chamber 1, a waste population rs2 is provided. The waste is placed in a tray 3 provided in the primary combustion chamber 1. A portion of the tray 3 of this receiver is provided with a radio wave absorber 4 such as silicon carbide. Furthermore, the opening 5 in the side wall of the secondary baking chamber l communicates with the transmitter of the magnetron 6 through a waveguide 7.
また、−次席焼室の他の側壁には一次空気孔8が設けら
れている。この−水室気孔8へ燃焼用空気は、送風機9
およびダンパー10によって供給されている。−次席焼
室1の下流は、着火ヒータ11と、−次席焼室1よりの
ガス通過孔12、および二次燃焼孔13(直径2mn+
、4個所)を有する第1段の二次燃焼室14である。こ
の二次燃焼室14の下流に第2段、第3段の二次燃焼室
15゜16がもうけられ、それぞれに二次空気孔17(
直径2no++、12g所)、18(直径2nw、12
i所)があけられている、それぞれの二次燃焼室は中央
に開口を持つ制炎板19で仕切られている。In addition, a primary air hole 8 is provided in the other side wall of the secondary baking chamber. Combustion air is supplied to this water chamber pore 8 by a blower 9.
and is supplied by the damper 10. - Downstream of the secondary grilling chamber 1, an ignition heater 11, - a gas passage hole 12 from the secondary grilling chamber 1, and a secondary combustion hole 13 (diameter 2 mm +
, four locations) of the first stage secondary combustion chamber 14. Second and third stage secondary combustion chambers 15 and 16 are provided downstream of this secondary combustion chamber 14, and each has a secondary air hole 17 (
Diameter 2no++, 12g), 18 (diameter 2nw, 12
Each secondary combustion chamber, which is opened at point i), is partitioned by a flame suppressing plate 19 having an opening in the center.
この二次燃焼孔には前記送風419より燃焼空気が送ら
れている。二次燃焼室16下流には燃焼温度検知部20
、触媒21、および排気孔22、排気希釈部23がおか
れている。また前記二次燃焼室14.15.16の側壁
の二次燃焼孔13,17゜18の上流にヒータ24が設
けである。Combustion air is sent to this secondary combustion hole from the air blower 419. A combustion temperature detection section 20 is located downstream of the secondary combustion chamber 16.
, a catalyst 21, an exhaust hole 22, and an exhaust gas dilution section 23 are provided. Further, a heater 24 is provided upstream of the secondary combustion holes 13, 17° 18 in the side wall of the secondary combustion chamber 14, 15, 16.
次に動作について説明する。Next, the operation will be explained.
一次燃焼室1の受は皿3にセットされた廃棄物はマグネ
トロン6の発信、送風機9の運転、および加熱ヒータ2
4の通電によって乾燥を開始する。The receiver of the primary combustion chamber 1 transmits the waste set in the tray 3 by transmitting the magnetron 6, operating the blower 9, and heating the heater 2.
Drying is started by applying electricity in step 4.
2450Mf(zのマイクロ波は導波管7をとうり、電
波透過性の断熱材を通過して一次燃焼室1に放出され内
部に高い電界を作る。電波は燃焼室lの金属壁で反射す
るので、はとんど廃棄物中の水分に吸収される。このた
め廃棄物は急速に乾燥する。The microwave of 2450 Mf (z takes the waveguide 7, passes through the radio wave transparent insulation material, and is emitted into the primary combustion chamber 1, creating a high electric field inside. The radio waves are reflected by the metal wall of the combustion chamber l. Therefore, most of the water is absorbed by the water in the waste, which causes the waste to dry quickly.
また同時に電波吸収体4も廃棄物の乾燥進行とともに、
電波を吸収し始め高温化していく、この電波吸収体4の
高熱で廃棄物は分解しガスを発生する。At the same time, as the waste material dries, the radio wave absorber 4 also
The high heat of the radio wave absorber 4, which begins to absorb radio waves and becomes high in temperature, decomposes the waste and generates gas.
二次燃焼室14に設けた着火ヒータ11は二次燃焼室1
4のガス濃度が除徐に濃くなり可燃ガスとなると着火さ
せる。The ignition heater 11 provided in the secondary combustion chamber 14
When the gas concentration in step 4 gradually increases and becomes a combustible gas, it is ignited.
さらに二次燃焼室14の火炎が大きくなると、火炎は下
流の第2段の二次燃焼室15で燃焼する。When the flame in the secondary combustion chamber 14 further becomes larger, the flame burns in the secondary combustion chamber 15 of the second stage downstream.
また、さらに増加したときは第3段の二次燃焼室16で
燃焼するものである。したがって廃棄物の発生するガス
量が変動しても不完全燃焼しにくい。Further, when the amount increases further, it is burned in the third stage secondary combustion chamber 16. Therefore, even if the amount of gas generated by the waste fluctuates, incomplete combustion is unlikely to occur.
また燃焼温度検知部20で燃焼量を検出しマイクロ波を
コントロールすれば、この二次燃焼室の燃焼能力を超す
燃焼量の増加は抑制される。Furthermore, if the combustion temperature detection section 20 detects the combustion amount and controls the microwave, an increase in the combustion amount exceeding the combustion capacity of the secondary combustion chamber can be suppressed.
各二次燃焼室の二次燃焼孔13.17.18が制炎板の
上流近傍に設けであるが、これはこの二次空気が上流か
ら流れてくる未燃ガスを二次燃焼孔の根元に誘引し効果
的に未燃ガスと空気を混合するためである。すなわち二
次空気孔の下流が制炎板19で規制しているので、二次
燃焼孔は下流の火炎を誘引せず、未燃ガスが集中的に引
き寄せられている。また二次燃焼空気は各二次燃焼室の
中央で衝突している。制炎板19の間口はこの衝突して
いる二次空気で塞がり、上流の未燃ガスはこのためにも
、前述の二次燃焼孔13. 17. 18の根元へ迂回
し、混合しつつ燃焼して、下流の段へ移行する力を受け
ている。このような作用は各段の二次燃焼室に共通のも
のである。The secondary combustion holes 13, 17, and 18 of each secondary combustion chamber are provided near the upstream of the flame suppressing plate, and this means that this secondary air directs unburned gas flowing from upstream to the root of the secondary combustion hole. This is to effectively mix unburned gas and air. That is, since the downstream side of the secondary air hole is regulated by the flame control plate 19, the secondary combustion hole does not attract downstream flames, and unburnt gas is concentratedly attracted thereto. Further, the secondary combustion air collides at the center of each secondary combustion chamber. The frontage of the flame suppressing plate 19 is blocked by this colliding secondary air, and for this reason, the unburned gas in the upstream is trapped in the secondary combustion hole 13. 17. It is detoured to the root of No. 18, burns while mixing, and receives a force that transfers to the downstream stage. This action is common to the secondary combustion chambers of each stage.
さらに着火時の燃焼量は少なく不完全燃焼をしやすいも
のであるが、この着火時は二次燃焼空気の量を少なくす
るとより燃焼は完全となる。乾燥時、着火時、また燃焼
温度検知部20が所定の燃焼量の増加を示すまでの問二
次空気は制限し、こののち増加することが低燃焼時の高
温維持のため有利である。Furthermore, the amount of combustion at the time of ignition is small and incomplete combustion tends to occur; however, if the amount of secondary combustion air is reduced at the time of ignition, the combustion will be more complete. It is advantageous to limit the amount of secondary air during drying, ignition, and until the combustion temperature detection section 20 indicates a predetermined increase in combustion amount, and then increase the amount thereafter to maintain high temperature during low combustion.
なお、上記実施例においてはマイクロ波を用いた電力加
熱方式について示したが、加熱する手段は他の手段であ
ってもよい。In addition, although the electric power heating method using microwave was shown in the said Example, the means for heating may be other means.
発明の効果 以上に述べた本発明の効果は以下の通りである。Effect of the invention The effects of the present invention described above are as follows.
分解ガスの発生量の変動が少なく、かつ変動しても広い
範囲の濃度で確実に燃焼するので、スス、臭気の発生は
すくない。このため廃棄物の種類によらず完全燃焼させ
るものである。There is little variation in the amount of decomposed gas generated, and even if it fluctuates, it burns reliably over a wide range of concentrations, so soot and odor are not generated much. For this reason, complete combustion is required regardless of the type of waste.
図は本発明の一実施例の廃棄物焼却装置を示す断面図で
ある。
l・・・−水煙焼室、6・・・発信部、11・・・着火
ヒータ、13.17.18・・・二次燃焼孔、14,1
5,16・・・二次燃焼室、19・・・制炎板。The figure is a sectional view showing a waste incinerator according to an embodiment of the present invention. l... - Water smoke combustion chamber, 6... Transmission section, 11... Ignition heater, 13.17.18... Secondary combustion hole, 14,1
5, 16... Secondary combustion chamber, 19... Flame control plate.
Claims (2)
に燃焼用の空気を供給する手段と、前記一次燃焼室の廃
棄物を加熱する手段と、前記一次燃焼室の下流に設けら
れた多段に分割された二次燃焼室を有するもので、前記
二次燃焼室の第1段燃焼室には着火手段、および燃焼空
気の供給孔と、前記一次燃焼室に開口するガス通過孔を
有し、第2段燃焼室以下には前記第1段燃焼室より多数
の燃焼空気孔を設け、かつそれぞれの二次燃焼室が中央
に開口を有する制炎板で仕切られている焼却装置。(1) A primary combustion chamber for storing waste, means for supplying air for combustion to the primary combustion chamber, means for heating the waste in the primary combustion chamber, and a device provided downstream of the primary combustion chamber. The first combustion chamber of the secondary combustion chamber has an ignition means, a combustion air supply hole, and a gas passage hole opening into the primary combustion chamber. An incinerator comprising a second-stage combustion chamber and a larger number of combustion air holes than the first-stage combustion chamber, and each secondary combustion chamber is partitioned by a flame control plate having an opening in the center.
とし、最大燃焼量に至る前に大とする制御を行う特許請
求の範囲第1項記載の焼却装置。(2) The incinerator according to claim 1, wherein the combustion air in the secondary combustion chamber is controlled to be reduced at least until ignition and increased before reaching the maximum combustion amount.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30234087A JPH01142313A (en) | 1987-11-30 | 1987-11-30 | Incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30234087A JPH01142313A (en) | 1987-11-30 | 1987-11-30 | Incinerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01142313A true JPH01142313A (en) | 1989-06-05 |
JPH0523327B2 JPH0523327B2 (en) | 1993-04-02 |
Family
ID=17907752
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30234087A Granted JPH01142313A (en) | 1987-11-30 | 1987-11-30 | Incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01142313A (en) |
-
1987
- 1987-11-30 JP JP30234087A patent/JPH01142313A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH0523327B2 (en) | 1993-04-02 |
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