JPH0674890B2 - Waste treatment equipment - Google Patents
Waste treatment equipmentInfo
- Publication number
- JPH0674890B2 JPH0674890B2 JP1017118A JP1711889A JPH0674890B2 JP H0674890 B2 JPH0674890 B2 JP H0674890B2 JP 1017118 A JP1017118 A JP 1017118A JP 1711889 A JP1711889 A JP 1711889A JP H0674890 B2 JPH0674890 B2 JP H0674890B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion chamber
- waste
- catalyst
- temperature
- primary
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002699 waste material Substances 0.000 title claims description 74
- 238000002485 combustion reaction Methods 0.000 claims description 85
- 239000003054 catalyst Substances 0.000 claims description 58
- 238000010438 heat treatment Methods 0.000 claims description 25
- 238000007664 blowing Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 description 13
- 230000004913 activation Effects 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000003763 carbonization Methods 0.000 description 8
- 230000005611 electricity Effects 0.000 description 7
- 238000001035 drying Methods 0.000 description 6
- 238000001514 detection method Methods 0.000 description 5
- 230000005684 electric field Effects 0.000 description 5
- 239000011810 insulating material Substances 0.000 description 5
- 239000000567 combustion gas Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000004380 ashing Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000010849 combustible waste Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
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で発生する生ごみや可燃
性のごみやし尿等の廃棄物の処理に利用される廃棄物処
理装置に関するものである。Description: TECHNICAL FIELD The present invention relates to a waste treatment device used for treating waste such as food waste, combustible waste, human waste, etc. generated at home or in business. .
従来の技術 従来の廃棄物処理装置は、ディスポーザーと呼ばれる機
械式処理装置と、焼却炉と呼ばれる燃焼式処理装置との
2方式があった。しかし、これらの装置は下水道を詰ま
らせたり、発煙や発臭などを起こしやすく、環境汚染を
生じるなどの大きな欠点があった。2. Description of the Related Art There are two types of conventional waste treatment devices: a mechanical treatment device called a disposer and a combustion type treatment device called an incinerator. However, these devices have major drawbacks such as clogging of sewers, smoke and odor, and environmental pollution.
そこで、これらの問題を解決するために、マグネトロン
やヒータを利用し、廃棄物を分解燃焼する廃棄物処理装
置が提案されている。この装置について第2図をもとに
説明する。Therefore, in order to solve these problems, a waste treatment device that decomposes and burns the waste by using a magnetron or a heater has been proposed. This device will be described with reference to FIG.
第2図において、燃焼室をマイクロ波減衰部1で1次燃
焼室2と2次燃焼室3に分割し、1次燃焼室2の内部に
廃棄物収納部4を設置し、廃棄物5をセットする。燃焼
用空気の供給、および2次空気室6に設けた触媒加熱用
ヒータ7の通電を開始して、触媒8を加熱する。触媒8
の温度が高温になり、活性温度以上になるとマグネトロ
ン9の通電を開始する。In FIG. 2, the combustion chamber is divided into a primary combustion chamber 2 and a secondary combustion chamber 3 by a microwave attenuator 1, a waste storage unit 4 is installed inside the primary combustion chamber 2, and a waste 5 is disposed. set. The supply of combustion air and the energization of the catalyst heating heater 7 provided in the secondary air chamber 6 are started to heat the catalyst 8. Catalyst 8
When the temperature becomes higher than the activation temperature, the magnetron 9 starts to be energized.
2450MHzのマイクロ波がマグネトロン9より発信され、
導波管10を通り1次燃焼室2内に照射される。このため
に、マイクロ波はすべて廃棄物5に吸収され、廃棄物5
の水分が蒸発し、廃棄物5は急速に乾燥する。廃棄物5
がある程度高温になると、廃棄物5から可燃性のガスを
発生しながら、廃棄物5の炭化が始まる。この可燃性ガ
スは1次空気口11より供給される1次空気と混合して、
2次燃焼室3に供給される。2次燃焼室3に送られた可
燃性混合気は、2次燃焼室3内に設けられた点火器12に
より着火し、2次空気口13より供給される2次空気と混
合して2次燃焼する。燃焼ガスは、触媒8で浄化された
後に、排気筒14より排出される。2450MHz microwave is transmitted from the magnetron 9,
Irradiation into the primary combustion chamber 2 through the waveguide 10. For this reason, all microwaves are absorbed by the waste 5 and the waste 5
The water in the waste material evaporates, and the waste material 5 dries rapidly. Waste 5
When the temperature of the waste 5 rises to a certain degree, carbonization of the waste 5 starts while generating a flammable gas from the waste 5. This combustible gas is mixed with the primary air supplied from the primary air port 11,
It is supplied to the secondary combustion chamber 3. The combustible air-fuel mixture sent to the secondary combustion chamber 3 is ignited by an igniter 12 provided in the secondary combustion chamber 3 and mixed with secondary air supplied from a secondary air port 13 to be secondary. To burn. The combustion gas is purified by the catalyst 8 and then discharged from the exhaust stack 14.
以後、廃棄物5は可燃性ガスを発生しながら炭化を促進
させ、廃棄物5が完全に炭化して可燃性ガスが発生しな
くなるまで、2次燃焼室3内で火炎燃焼が続く。廃棄物
5が完全に炭化すると、2次燃焼室3内での火炎は消炎
し、1次燃焼室2内で固体燃焼(いこり燃焼)を始め、
灰化に至る。このようにして、廃棄物を処理している。Thereafter, the waste 5 promotes carbonization while generating combustible gas, and flame combustion continues in the secondary combustion chamber 3 until the waste 5 is completely carbonized and no combustible gas is generated. When the waste 5 is completely carbonized, the flame in the secondary combustion chamber 3 is extinguished, and solid combustion (industrial combustion) is started in the primary combustion chamber 2,
Leads to ashing. In this way, the waste is treated.
発明が解決しようとする課題 しかし、このような従来の廃棄物処理装置には、以下に
示すような課題があった。Problems to be Solved by the Invention However, such a conventional waste treatment device has the following problems.
マグネトロンより発せられたマイクロ波は、燃焼室内に
置かれた廃棄物に電界が集中するように、燃焼室内の電
界分布を調整してある。マイクロ波により廃棄物の乾燥
が進行すると廃棄物から多量の水蒸気が発生する。この
水蒸気には廃棄物の臭気が含まれており、廃棄物の乾燥
時に強烈な臭気を発生する。このために触媒を設け、臭
気の除去を行っている。しかし、水蒸気は触媒毒であ
り、また触媒温度の低下を引き起こし、触媒の活性をか
なり低下する。したがって、触媒加熱手段を設け、触媒
温度を高温に維持し、触媒の活性の低下を防いでいるわ
けである。The electric field distribution in the combustion chamber is adjusted so that the microwave generated from the magnetron concentrates the electric field on the waste placed in the combustion chamber. When the drying of the waste progresses by the microwave, a large amount of water vapor is generated from the waste. This water vapor contains the odor of waste, and produces a strong odor when the waste is dried. Therefore, a catalyst is provided to remove odor. However, water vapor is a catalyst poison and causes a decrease in catalyst temperature, which considerably reduces the activity of the catalyst. Therefore, the catalyst heating means is provided to maintain the catalyst temperature at a high temperature and prevent the activity of the catalyst from decreasing.
この結果、乾燥時にはマグネトロンと触媒加熱手段とを
同時に使用するために、電気使用量が非常に大きくなる
という課題があった。As a result, since the magnetron and the catalyst heating means are used at the same time during drying, there is a problem that the amount of electricity used becomes very large.
本発明は簡単な構成で、電気使用量を少なくても、乾燥
時に臭気の無い廃棄物処理装置を提供することを目的と
する。It is an object of the present invention to provide a waste treatment device which has a simple structure and has little odor when dried even if the amount of electricity used is small.
課題を解決するための手段 本発明は、廃棄物を収納する1次燃焼室とその下流に位
置した2次燃焼室とからなる燃焼室を有し、1次燃焼室
とマグネトロンを導波管で連結し、燃焼用空気を1次燃
焼室及び2次燃焼室に1次空気及び2次空気として別個
に供給、1次燃焼室の下流に位置した2次空気の供給経
路内に加熱手段設け、2次燃焼室の下流に触媒を設け、
触媒の温度を検出する手段を設け、触媒温度検出手段か
らの信号が一定になるように、マグネトロンと加熱手段
を交互に通電するものである。Means for Solving the Problems The present invention has a combustion chamber including a primary combustion chamber that stores waste and a secondary combustion chamber located downstream thereof, and the primary combustion chamber and the magnetron are waveguides. Connecting and supplying combustion air to the primary combustion chamber and the secondary combustion chamber separately as primary air and secondary air, and providing heating means in the secondary air supply path located downstream of the primary combustion chamber, A catalyst is installed downstream of the secondary combustion chamber,
A means for detecting the temperature of the catalyst is provided, and the magnetron and the heating means are alternately energized so that the signal from the catalyst temperature detecting means becomes constant.
作 用 本発明の作用は次の通りである。Operation The operation of the present invention is as follows.
始動時に触媒加熱手段に通電し、触媒を昇温させる。触
媒温度検出手段の信号により、触媒が活性温度に到達し
たことを確認すると、触媒加熱手段の通電を停止し、マ
グネトロンの通電を開始する。1次燃焼室内にマイクロ
波が照射されると、廃棄物に含まれる水分が蒸発し、廃
棄物の乾燥が進行する。この廃棄物から発生する水蒸気
により触媒温度が低下し、触媒温度が活性温度以下にな
る。そこで、マグネトロンの通電を停止し、触媒加熱手
段の通電を再び開始する。以後、触媒が活性温度を維持
するように、マグネトロンと触媒加熱手段を交互に通電
する。At the time of starting, the catalyst heating means is energized to raise the temperature of the catalyst. When it is confirmed by the signal of the catalyst temperature detecting means that the catalyst has reached the activation temperature, the energization of the catalyst heating means is stopped and the magnetron is energized. When the primary combustion chamber is irradiated with microwaves, the water contained in the waste is evaporated and the waste is dried. The steam generated from this waste lowers the catalyst temperature, and the catalyst temperature falls below the activation temperature. Therefore, the energization of the magnetron is stopped and the energization of the catalyst heating means is started again. After that, the magnetron and the catalyst heating means are alternately energized so that the catalyst maintains the activation temperature.
この制御方法により、本装置を運転中はマグネトロンと
触媒加熱手段のどちらか1つしか通電されないために、
電気使用量が非常に少なくなる。By this control method, since only one of the magnetron and the catalyst heating means is energized while the apparatus is in operation,
Electricity consumption is very low.
さらに、マイクロ波が間欠に照射されることになり、マ
イクロ波の照射が停止している間に、乾燥が進行した部
分に、回りのまだ湿っている部分から水分が浸透してく
る。したがってマイクロ波を間欠で照射されるために、
乾燥が局所的に進行することなく廃棄物を均一に乾燥で
きる。乾燥が進み、廃棄物の温度が高温になってくる。
マイクロ波の照射が停止している間に、高温になった場
合から回りへ熱が伝導し、廃棄物の温度が急速に低下す
る。このために廃棄物は均一に温度が上昇し、炭化が均
一に行われる。Further, the microwaves are intermittently applied, and while the irradiation of the microwaves is stopped, water penetrates into the part where the drying has progressed from the still moist part around. Therefore, because the microwave is emitted intermittently,
The waste can be uniformly dried without locally drying. Drying progresses, and the temperature of waste becomes high.
While the microwave irradiation is stopped, heat is conducted to the surroundings from the high temperature and the temperature of the waste is rapidly decreased. For this reason, the temperature of the waste uniformly rises and the carbonization is performed uniformly.
廃棄物の炭化が均一に行われるために、着火直後の可燃
性ガスの多量発生を防ぐことができ、可燃性ガスの発生
が徐々に増加することになる。このために、燃焼量も徐
々に増加するので、着火時のオーバーシュートを防ぐこ
とができる。このため、着火時のに空気不足を解消し、
不完全燃焼を防止し、燃焼特性を良好にすることができ
る。Since the carbonization of the waste is performed uniformly, it is possible to prevent a large amount of combustible gas from being generated immediately after ignition, and the generation of combustible gas is gradually increased. For this reason, the combustion amount also gradually increases, so that overshoot at the time of ignition can be prevented. Therefore, eliminate the air shortage at the time of ignition,
Incomplete combustion can be prevented and combustion characteristics can be improved.
実施例 以下、本発明の実施例を図面に基づいて説明する。Embodiment An embodiment of the present invention will be described below with reference to the drawings.
第1図において、1次燃焼室15の内部に廃棄物収納部16
を設ける。廃棄物収納部16の内側は断熱材17でライニン
グされ、底面にはマイクロ波加熱体18が設置されてい
る。1次燃焼室15の上部は複数個の1次空気口19を穿っ
た断熱材20で廃棄物収納部16と1次空気室21を分離して
いる。また断熱材20の中央部にはフィルタ22を設け、廃
棄物23が燃焼する際に発生する煙分や廃棄物23の灰化過
程における灰分の飛散をこのフィルタ22でトラップする
ものである。ここで用いられている断熱材17、20、フィ
ルタ22はすべてマイクロ波を透過する物質で構成されて
おり、1次燃焼室15内の電界分布に何等影響を与えない
ものである。In FIG. 1, a waste storage unit 16 is provided inside the primary combustion chamber 15.
To provide. The inside of the waste storage unit 16 is lined with a heat insulating material 17, and a microwave heating body 18 is installed on the bottom surface. The upper part of the primary combustion chamber 15 is separated from the waste storage unit 16 and the primary air chamber 21 by a heat insulating material 20 having a plurality of primary air ports 19. Further, a filter 22 is provided in the center of the heat insulating material 20, and the filter 22 traps smoke generated when the waste 23 burns and ash scattering in the ashing process of the waste 23. The heat insulating materials 17 and 20 and the filter 22 used here are all made of a substance that transmits microwaves, and have no influence on the electric field distribution in the primary combustion chamber 15.
マイクロ波減衰部24を介して1次燃焼室15と2次燃焼室
25を接続し、廃棄物23から発生した可燃性ガスを2次燃
焼室25で火炎燃焼させる。2次燃焼室25の外側に2次空
気室26を設け、さらに2次空気室26の内部に触媒加熱用
ヒータ27を設け、触媒加熱用ヒータ27により2次空気を
加熱し、高温になった2次空気により2次燃焼室25下流
に設けた触媒28を加熱する。Primary combustion chamber 15 and secondary combustion chamber through microwave attenuator 24
25 is connected, and the combustible gas generated from the waste 23 is burned by flame in the secondary combustion chamber 25. A secondary air chamber 26 is provided outside the secondary combustion chamber 25, and a catalyst heating heater 27 is further provided inside the secondary air chamber 26. The catalyst heating heater 27 heats the secondary air to reach a high temperature. The catalyst 28 provided downstream of the secondary combustion chamber 25 is heated by the secondary air.
2次燃焼室25は内部を複数個の燃焼室に分割され、第1
室のマイクロ波減衰部24近傍に点火ヒータ29を設け、最
終室には温度検出部30を設けてある。1次燃焼室15と2
次燃焼室25との境目にはマイクロ波減衰部24を設けてあ
り、マイクロ波が2次燃焼室25へ侵入するのを防いでい
る。したがって、点火ヒータ29は、マイクロ波を受信し
てアーキングを起こすなどの影響を受けずに、可燃性混
合気を着火させることができる。The interior of the secondary combustion chamber 25 is divided into a plurality of combustion chambers.
An ignition heater 29 is provided near the microwave attenuator 24 of the chamber, and a temperature detector 30 is provided in the final chamber. Primary combustion chamber 15 and 2
A microwave attenuator 24 is provided at the boundary with the secondary combustion chamber 25 to prevent microwaves from entering the secondary combustion chamber 25. Therefore, the ignition heater 29 can ignite the combustible air-fuel mixture without being affected by receiving microwaves and causing arcing.
扉31を開け、廃棄物収納部16に廃棄物23を収納し、扉31
を閉める。1次燃焼室15の下方に設けた送風機32を始動
させ、給気パイプ33、34により1次空気および2次空気
を各燃焼室に供給する。触媒28の温度が高温になり、活
性温度以上になるとマグネトロン35の通電を開始する。Open the door 31, store the waste 23 in the waste storage unit 16, and
Close. The blower 32 provided below the primary combustion chamber 15 is started, and primary air and secondary air are supplied to each combustion chamber by the air supply pipes 33 and 34. When the temperature of the catalyst 28 rises to the activation temperature or higher, the magnetron 35 starts to be energized.
2450MHzのマイクロ波がマグネトロン35より発信され、
導波管36を通り1次燃焼室15内に照射される。導波管36
と1次燃焼室15の接続部にはマイクロ波透過体37を設
け、燃焼ガスを遮断しマグネトロン35の発信部を保護し
てある。1次空気は1次燃焼室15の外側に設けた1次空
気供給経路38を通って1次燃焼室15に供給されるため
に、1次燃焼室15の保温性を高めている。また、1次空
気が1次燃焼室15に供給される際に、マイクロ波透過体
37を冷却するように、1次空気室21と導波管36を接続し
てあるために、マイクロ波透過体37が高温になることを
防止している。2450MHz microwave is transmitted from magnetron 35,
It is irradiated into the primary combustion chamber 15 through the waveguide 36. Waveguide 36
A microwave transmissive body 37 is provided at a connecting portion between the primary combustion chamber 15 and the primary combustion chamber 15 to shut off a combustion gas to protect a transmitting portion of the magnetron 35. Since the primary air is supplied to the primary combustion chamber 15 through the primary air supply path 38 provided outside the primary combustion chamber 15, the heat insulation of the primary combustion chamber 15 is enhanced. Further, when the primary air is supplied to the primary combustion chamber 15, the microwave transparent material
Since the primary air chamber 21 and the waveguide 36 are connected to cool the 37, the microwave transmitter 37 is prevented from reaching a high temperature.
1次燃焼室15は、廃棄物収納部16に置かれた廃棄物23に
電界が集中するように、1次燃焼室15内の電界分布を調
整してある。このために、マイクロ波はすべて廃棄物23
に吸収され、廃棄物23の水分が蒸発し、廃棄物23は急速
に乾燥する。In the primary combustion chamber 15, the electric field distribution in the primary combustion chamber 15 is adjusted so that the electric field is concentrated on the waste 23 placed in the waste storage unit 16. Because of this, microwaves are all waste products23
Are absorbed into the waste 23, the water content of the waste 23 evaporates, and the waste 23 dries rapidly.
マイクロ波加熱体18がある程度高温になると、廃棄物23
から可燃性のガスを発生しながら、廃棄物23の炭化が始
まる。この可燃性ガスは1次空気口19より供給される1
次空気と混合して、2次燃焼室25に供給される。2次燃
焼室25に送られた可燃性混合気は、2次燃焼室25内に設
けられた点火ヒータ29により着火し、2次空気口39より
供給される2次空気と混合して2次燃焼する。燃焼ガス
は、触媒28で浄化された後に、希釈室40で給気パイプ41
より供給された3次空気混合した後、排気筒42より排出
される。なお、3次空気の供給経路内にはマグネトロン
のラジエタを設け、3次空気をマグネトロンの冷却用と
兼用している。When the microwave heating element 18 reaches a certain temperature, waste 23
Carbonization of the waste 23 begins while generating a flammable gas from the. This combustible gas is supplied from the primary air port 19
It is mixed with secondary air and supplied to the secondary combustion chamber 25. The combustible air-fuel mixture sent to the secondary combustion chamber 25 is ignited by an ignition heater 29 provided in the secondary combustion chamber 25 and mixed with secondary air supplied from a secondary air port 39 to be secondary. To burn. The combustion gas is purified by the catalyst 28 and then supplied to the air supply pipe 41 in the dilution chamber 40.
After mixing the supplied tertiary air, it is discharged from the exhaust pipe 42. A radiator of a magnetron is provided in the tertiary air supply path, and the tertiary air is also used for cooling the magnetron.
以後は、廃棄物23はマグネトロン35からのマイクロ波を
受けて、可燃性ガスを発生しながら炭化を促進させ、廃
棄物23が完全に炭化して可燃性ガスが発生しなくなるま
で、2次燃焼室25内で火炎燃焼が続く。廃棄物23が完全
に炭化すると、2次燃焼室25内での火炎は消炎し、1次
燃焼室15内で固体燃焼(いこり燃焼)を始める。そして
固体燃焼に移行したときに、1次空気量を増加し、炭化
した廃棄物23の燃焼を行い、灰化に至る。ここで、1次
燃焼室15および廃棄物収納部16の内側は断熱材で覆わ
れ、また1次燃焼室15の外側には1次空気供給経路38を
設けてあるために、1次燃焼室15の保温状態は非常に良
好で、マイクロ波を受信したマイクロ波加熱体18は非常
に高温になる。このために廃棄物23の灰化状態が非常に
良好になる。After that, the waste 23 receives microwaves from the magnetron 35, promotes carbonization while generating combustible gas, and secondary combustion is performed until the waste 23 is completely carbonized and no combustible gas is generated. Flame combustion continues in chamber 25. When the waste 23 is completely carbonized, the flame in the secondary combustion chamber 25 is extinguished, and solid combustion (industrial combustion) is started in the primary combustion chamber 15. Then, when the solid combustion is started, the amount of primary air is increased, the carbonized waste 23 is burned, and the ash is formed. Here, the inside of the primary combustion chamber 15 and the waste container 16 is covered with a heat insulating material, and the primary air supply path 38 is provided outside the primary combustion chamber 15, so that the primary combustion chamber 15 is provided. The heat retention state of 15 is very good, and the microwave heating body 18 that has received the microwave becomes very hot. For this reason, the ashed state of the waste 23 becomes very good.
このような本発明の具体的動作関係について以下に説明
する。The specific operation relationship of the present invention will be described below.
本発明では2次燃焼室内25の最終室に温度検出部30を設
けて触媒28の温度を検出できるようにしてある。温度検
出部30は本実施例のように2次燃焼室内24の最終室に、
触媒28に近接して設けてもよいし、触媒28に直接触媒し
て取り付けてもよい。ここで、温度検出部30は、サーモ
カップル、光センサなどで、温度、光などを検知して、
触媒28の温度を検出できるものである。In the present invention, the temperature detecting unit 30 is provided in the final chamber of the secondary combustion chamber 25 so that the temperature of the catalyst 28 can be detected. The temperature detecting unit 30 is provided in the final chamber of the secondary combustion chamber 24 as in the present embodiment.
It may be provided in the vicinity of the catalyst 28, or may be directly attached to the catalyst 28 as a catalyst. Here, the temperature detection unit 30 detects temperature, light, etc. by a thermocouple, an optical sensor, etc.,
The temperature of the catalyst 28 can be detected.
たとえば、温度検出部30にサーモカップルを用いた場合
について説明する。始動時に触媒加熱用ヒータ27に通電
し、あらかじめ触媒28を活性温度まで昇温させる。温度
検出部30からの信号により、触媒28が活性温度に到達し
たことを確認すると、触媒加熱用ヒータ27の通電を停止
し、マグネトロン35の通電を開始する。1次燃焼室15内
にマイクロ波が照射されると、廃棄物23に含まれる水分
が蒸発し、廃棄物23の乾燥が進行する。この廃棄物23か
ら発生する水蒸気により触媒28の温度が低下し、触媒温
度が活性温度以下になる。温度検出部30からの信号によ
り、触媒温度が活性温度以下になったことを検出する
と、マグネトロン35の通電を停止し、触媒加熱用ヒータ
27の通電を再び開始する。以後、触媒28が活性温度を維
持するように、温度検出部30からの信号によりマグネト
ロン35と触媒加熱用ヒータ27を交互に通電する。For example, a case where a thermocouple is used for the temperature detection unit 30 will be described. At the time of startup, the catalyst heating heater 27 is energized to preheat the catalyst 28 to the activation temperature. When it is confirmed by the signal from the temperature detection unit 30 that the catalyst 28 has reached the activation temperature, the heater 27 for heating the catalyst is de-energized and the magnetron 35 is energized. When the primary combustion chamber 15 is irradiated with microwaves, the water contained in the waste 23 is evaporated and the waste 23 is dried. The steam generated from the waste 23 lowers the temperature of the catalyst 28, so that the catalyst temperature becomes equal to or lower than the activation temperature. When it is detected by the signal from the temperature detection unit 30 that the catalyst temperature has become lower than the activation temperature, the energization of the magnetron 35 is stopped and the catalyst heating heater
Power on 27 again. After that, the magnetron 35 and the heater 27 for heating the catalyst are alternately energized by a signal from the temperature detecting unit 30 so that the catalyst 28 maintains the active temperature.
この制御方法により、本装置を運転中はマグネトロン35
と触媒加熱用ヒータ27のどちらか1つしか通電しなくと
も、触媒28の温度を活性温度に維持することができるた
めに、電気使用量が非常に少なくとも、臭気がほとんど
無く廃棄物を処理することができる。With this control method, the magnetron 35
Since the temperature of the catalyst 28 can be maintained at the activation temperature even if only one of the heater and the heater 27 for heating the catalyst is energized, the amount of electricity used is very low, and the waste is treated with almost no odor. be able to.
また、マグネトロン35と触媒加熱用ヒータ27を交互に通
電するために、廃棄物23にマイクロ波が間欠に照射され
ることになる。このために、マイクロ波の照射が停止し
ている間に、廃棄物23の乾燥が進行した部分に、回りの
まだ湿っている部分から水分が浸透し、乾燥が局所的に
進行することなく廃棄物23を均一に乾燥できる。乾燥が
進み、廃棄物23に含まれる水分が少なくなり、廃棄物23
の温度が高温になると、マイクロ波の照射が停止してい
る間に、高温になった場所から回りへ熱が伝導し、廃棄
物23の温度が急速に低下する。このために廃棄物23は均
一に温度が上昇し、炭化が均一に行われる。Further, since the magnetron 35 and the catalyst heating heater 27 are alternately energized, the waste 23 is intermittently irradiated with microwaves. For this reason, while the microwave irradiation is stopped, the portion of the waste material 23 that has been dried is infiltrated with moisture from the surrounding still moist portion, and the waste material 23 is discarded without being dried locally. The object 23 can be dried uniformly. As the drying progresses and the water content in waste 23 decreases,
When the temperature becomes high, heat is conducted from the place where the temperature is high to the surroundings while the microwave irradiation is stopped, and the temperature of the waste 23 rapidly decreases. For this reason, the temperature of the waste 23 rises uniformly and carbonization is performed uniformly.
廃棄物23の炭化が均一に行われるために、着火直後の可
燃性ガスの多量発生を防ぐことができ、可燃性ガスの発
生が徐々に増加することになる。このために、燃焼量も
徐々に増加するので、着火時のオーバーシュートを防ぐ
ことができる。このため、着火時の空気不足を解消し、
不完全燃焼を防止し、燃焼特性を良好にすることができ
る。Since the carbonization of the waste 23 is carried out uniformly, it is possible to prevent a large amount of combustible gas from being generated immediately after ignition, and the generation of the combustible gas is gradually increased. For this reason, the combustion amount also gradually increases, so that overshoot at the time of ignition can be prevented. Therefore, eliminating the air shortage at the time of ignition,
Incomplete combustion can be prevented and combustion characteristics can be improved.
発明の効果 以上のように本発明においては、触媒温度検出部からの
信号により、触媒温度を活性温度以上に維持するよう
に、マグネトロンと触媒加熱用ヒータを交互に通電する
ために、電気使用量が非常に少なくても、触媒温度を活
性温度に維持することができ、電気使用量が非常に少な
くても、臭気がほとんど無く廃棄物を処理することがで
きる。Effects of the Invention As described above, in the present invention, the amount of electricity used to alternately energize the magnetron and the heater for heating the catalyst by the signal from the catalyst temperature detection unit so as to maintain the catalyst temperature above the activation temperature. The catalyst temperature can be maintained at the active temperature even when the amount of electricity is very small, and the waste can be treated with almost no odor even when the amount of electricity used is very small.
第1図は本発明の一実施例の廃棄物処理装置の断面図、
第2図は従来例の廃棄物処理装置の断面図である。 15……1次燃焼室、25……2次燃焼室、27……触媒加熱
用ヒータ、28……触媒、30……温度検出部、35……マグ
ネトロン。FIG. 1 is a sectional view of a waste treatment device according to an embodiment of the present invention,
FIG. 2 is a cross-sectional view of a conventional waste treatment device. 15 …… Primary combustion chamber, 25 …… Secondary combustion chamber, 27 …… Catalyst heating heater, 28 …… Catalyst, 30 …… Temperature detector, 35 …… Magnetron.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 川崎 良隆 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (56)参考文献 特開 昭64−6612(JP,A) 特開 昭63−116016(JP,A) 特開 平1−196408(JP,A) 特開 平1−167510(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshitaka Kawasaki 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) Reference JP-A 64-6612 (JP, A) JP-A 63-116016 (JP, A) JP-A-1-196408 (JP, A) JP-A-1-167510 (JP, A)
Claims (1)
に位置した2次燃焼室とを備えた燃焼室を有し、前記1
次燃焼室とマグネトロンが導波管で連結され、燃焼用空
気を前記1次燃焼室及び2次燃焼室に1次空気及び2次
空気として別個に供給する送風手段を有し、前記1次燃
焼室の下流に位置した前記2次空気の供給経路内に加熱
手段が設けられ、前記2次燃焼室の下流に触媒が設けら
れ、前記触媒の温度を検出する手段が設けられ、前記触
媒温度検出手段からの信号が一定になるように、前記マ
グネトロンと前記加熱手段を交互に通電する手段を備え
たことを特徴とする廃棄物処理装置。1. A combustion chamber having a primary combustion chamber in which waste is stored and a secondary combustion chamber located downstream of the primary combustion chamber.
The secondary combustion chamber and the magnetron are connected by a waveguide, and there is a blowing means for separately supplying combustion air to the primary combustion chamber and the secondary combustion chamber as primary air and secondary air. A heating means is provided in the secondary air supply path located downstream of the chamber, a catalyst is provided downstream of the secondary combustion chamber, a means for detecting the temperature of the catalyst is provided, and the catalyst temperature is detected. A waste treatment apparatus comprising means for alternately energizing the magnetron and the heating means so that a signal from the means becomes constant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1017118A JPH0674890B2 (en) | 1989-01-26 | 1989-01-26 | Waste treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1017118A JPH0674890B2 (en) | 1989-01-26 | 1989-01-26 | Waste treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02197711A JPH02197711A (en) | 1990-08-06 |
| JPH0674890B2 true JPH0674890B2 (en) | 1994-09-21 |
Family
ID=11935125
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1017118A Expired - Fee Related JPH0674890B2 (en) | 1989-01-26 | 1989-01-26 | Waste treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0674890B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100401382B1 (en) * | 2002-12-10 | 2003-10-17 | 김태형 | Smoke consumer of a small success furnace |
-
1989
- 1989-01-26 JP JP1017118A patent/JPH0674890B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02197711A (en) | 1990-08-06 |
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