JPS62218715A - Garbage disposing device - Google Patents
Garbage disposing deviceInfo
- Publication number
- JPS62218715A JPS62218715A JP6234286A JP6234286A JPS62218715A JP S62218715 A JPS62218715 A JP S62218715A JP 6234286 A JP6234286 A JP 6234286A JP 6234286 A JP6234286 A JP 6234286A JP S62218715 A JPS62218715 A JP S62218715A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- heat
- garbage
- microwaves
- 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.)
- Granted
Links
- 239000010813 municipal solid waste Substances 0.000 title abstract description 14
- 239000003054 catalyst Substances 0.000 claims abstract description 22
- 239000010806 kitchen waste Substances 0.000 claims description 9
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 claims description 7
- 229910002113 barium titanate Inorganic materials 0.000 claims description 7
- 230000003197 catalytic effect Effects 0.000 claims description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 6
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 5
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 5
- 239000004408 titanium dioxide Substances 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- 239000005350 fused silica glass Substances 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims 1
- 235000011941 Tilia x europaea Nutrition 0.000 claims 1
- 150000004645 aluminates Chemical class 0.000 claims 1
- 239000004571 lime Substances 0.000 claims 1
- 238000000746 purification Methods 0.000 abstract description 8
- 238000002485 combustion reaction Methods 0.000 abstract description 7
- 230000003647 oxidation Effects 0.000 abstract description 5
- 238000007254 oxidation reaction Methods 0.000 abstract description 5
- 230000018044 dehydration Effects 0.000 abstract description 4
- 238000006297 dehydration reaction Methods 0.000 abstract description 4
- 230000020169 heat generation Effects 0.000 abstract description 4
- 238000003303 reheating Methods 0.000 abstract description 3
- 239000000779 smoke Substances 0.000 abstract description 2
- 238000000354 decomposition reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000010794 food waste Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 241001536352 Fraxinus americana Species 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- Constitution Of High-Frequency Heating (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、生ゴミをマイクロ波で焼却減量処理する厨
芥処理装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a kitchen waste processing device for reducing the amount of food waste by incinerating it using microwaves.
従来の技術
従来、この種の厨芥処理装置は第3図に示すようにマイ
クロ波共振体とした箱形の本体1の内底部にマイクロ波
で発熱する発熱容器2を配置している。また、本体1の
一側面に化ゴミ40投入口3が設けられ、この投入口3
は開閉自在な蓋16により開閉される。本体1の他の側
面に供給口6を設け、この供給口6に臨ませて本体1内
にマイクロ波を送り込むマイクロ波発生用のマグネトロ
ン装置6を取付けている。供給口6の下方には給気ロア
を設け、給気送風機8と連結され本体1内に燃焼に必要
な空気を供給する。また給気送風機8はマグネトロン装
置5側にも分岐し、冷却風を送り込む。本体1の上部に
はゴミ燃焼により発生する排ガスの排気口9を設け、こ
の排気口9は煙道9aを介して排ガス浄化ユニット12
、排気送風機13に接続されている。排ガス浄化ユニッ
ト12は加熱ヒータ1oと酸化触媒11とから構成され
ている。これら排ガス浄化ユニット12、排気送風機1
3は本体1を覆う外殻14の上部に取付けられている。2. Description of the Related Art Conventionally, as shown in FIG. 3, this type of kitchen waste processing apparatus has a heat-generating container 2 that generates heat using microwaves disposed at the inner bottom of a box-shaped main body 1 which is a microwave resonator. Further, an input port 3 for garbage 40 is provided on one side of the main body 1, and this input port 3
is opened and closed by a lid 16 that can be opened and closed. A supply port 6 is provided on the other side of the main body 1, and a magnetron device 6 for generating microwaves for sending microwaves into the main body 1 is attached facing the supply port 6. An air supply lower is provided below the supply port 6 and is connected to an air supply blower 8 to supply air necessary for combustion into the main body 1. The supply air blower 8 also branches to the magnetron device 5 side and sends cooling air. The upper part of the main body 1 is provided with an exhaust port 9 for exhaust gas generated by combustion of garbage, and this exhaust port 9 is connected to an exhaust gas purification unit 12 via a flue 9a.
, are connected to the exhaust blower 13. The exhaust gas purification unit 12 includes a heater 1o and an oxidation catalyst 11. These exhaust gas purification unit 12, exhaust blower 1
3 is attached to the upper part of an outer shell 14 that covers the main body 1.
上記構成により、生ゴミ4を発熱容器2に入れ、マイク
ロ波を放射すると、生ゴミ自体の内部発熱による加熱と
発熱容器2の発熱による加熱で燃焼し、この際、発生す
る排ガスは排ガス浄化ユニット12を通過する。この排
ガス浄化ユニットは加熱ヒータ1oにより排ガスを加熱
して触媒作用を高めた後、酸化触媒11により浄化排出
するものであった。With the above configuration, when food waste 4 is placed in the heat-generating container 2 and microwaves are radiated, the food waste is burned by heating due to internal heat generation of the food waste itself and heating due to heat generation from the heat-generating container 2. At this time, the generated exhaust gas is transferred to the exhaust gas purification unit. Pass 12. This exhaust gas purification unit heats the exhaust gas with a heater 1o to enhance the catalytic action, and then purifies and discharges the exhaust gas with an oxidation catalyst 11.
発明が解決しようとする問題点
このような従来の構成では、燃焼熱で充分熱い排ガスが
煙道9aを通過する間に冷却されるため、排ガス浄化ユ
ニット12へ入って酸化触媒11に接する前に加熱ヒー
タ10によシ触媒の機能温度(250℃以上)まで再加
熱を必要としていた。Problems to be Solved by the Invention In such a conventional configuration, exhaust gas that is sufficiently hot due to combustion heat is cooled while passing through the flue 9a. It was necessary to reheat the catalyst using the heater 10 to the functional temperature (250° C. or higher).
そのため、排ガスを再加熱するだめの加熱エネルギーを
必要で省エネルギーに適しないものであった。また、煙
道9aおよび加熱ヒータ1o等の構造物を要するという
問題点を有していた。Therefore, additional heating energy is required to reheat the exhaust gas, which is not suitable for energy saving. Further, there was a problem in that structures such as the flue 9a and the heater 1o were required.
本発明はこのような問題点を解決するもので、生ゴミ処
理に際して発生する排ガスを再加熱することなく排ガス
を浄化できる省エネルギー型の経済的な厨芥処理装置を
提供することを目的とするものである。The present invention is intended to solve these problems, and aims to provide an energy-saving and economical kitchen waste processing device that can purify the exhaust gas generated during food waste processing without reheating it. be.
問題点を解決するための手段
この問題点を解決するために本発明の厨芥処理装置は、
マイクロ波共振体とした本体に給気口と排気口を設け、
前記排気口にはマイクロ波により発熱する酸化物触媒体
を設けた構成である。Means for solving the problem In order to solve this problem, the kitchen waste processing apparatus of the present invention has the following features:
The main body is a microwave resonator with an air supply port and an exhaust port.
The exhaust port is provided with an oxide catalyst that generates heat by microwaves.
作 用
この構成により、本体内へマイクロ波を放射すると、生
ゴミの燃焼によシ排ガスが発生し、排気口を通過して外
部へ排出される。この排ガスは排出されるときに、マイ
クロ波によシ自己発熱して触媒機能温度に達した酸化物
触媒体によって水および炭酸ガス等に酸化分解される。Function: With this configuration, when microwaves are radiated into the main body, exhaust gas is generated due to the combustion of garbage, which passes through the exhaust port and is discharged to the outside. When this exhaust gas is discharged, it is oxidized and decomposed into water, carbon dioxide, etc. by the oxide catalyst body which self-heats by microwaves and reaches the catalytic function temperature.
実施例
以下、本発明の一実施例を第1図および第2図にもとづ
き説明する。なお従来の構成と同一部分には同一番号を
付し、その説明は省略する。EXAMPLE An example of the present invention will be described below with reference to FIGS. 1 and 2. Note that parts that are the same as those in the conventional configuration are given the same numbers, and their explanations will be omitted.
図において、外殻14内にマイクロ波共振体としだ本体
1が設けられておシ、この本体1の内底部に発熱容器2
が配置されている。そして、本体1の一側面に開閉自在
に取付けた扉15を開き投入口3よシ生ゴミ4を発熱容
器2に入れる。また、本体1の他の側面に供給口6を開
口し、この供給口6に連ら6導波管6aの奥にマグネト
ロン装置6を設けている。供給口6の下方には給気ロア
が設けられ、給気送風機8に連結されている。また、給
気送風機8の吐出側を分岐させマグネトロン装置5に冷
却風を供給する構成である。発熱容器2は炭化けい素と
チタン酸バリウムの焼結体で構成され、1ooo℃以上
の耐熱性を有し、かつマイクロ波によシ発熱する。本体
1の上部側面に設けた排気口101にはハニカム形状に
形成された酸化物触媒体10oが取付けられている。こ
の排気口101は煙道101aを介して排気送風機10
2が接続されている。なお本体1の各開口部はマイクロ
波の供給口6を除いて電波漏れ防止の手段が施されてい
る。In the figure, a microwave resonator and a main body 1 are provided in an outer shell 14, and a heat generating container 2 is provided at the inner bottom of the main body 1.
is located. Then, a door 15 attached to one side of the main body 1 so as to be openable and closable is opened, and the garbage 4 is put into the heat generating container 2 through the input port 3. In addition, a supply port 6 is opened on the other side of the main body 1, and a magnetron device 6 is provided at the back of the 6 waveguides 6a connected to the supply port 6. An air supply lower is provided below the supply port 6 and is connected to an air supply blower 8. Further, the discharge side of the supply air blower 8 is branched to supply cooling air to the magnetron device 5. The heat generating container 2 is made of a sintered body of silicon carbide and barium titanate, has a heat resistance of 100° C. or higher, and generates heat by microwaves. An oxide catalyst body 10o formed in a honeycomb shape is attached to an exhaust port 101 provided on the upper side surface of the main body 1. This exhaust port 101 is connected to the exhaust blower 10 via the flue 101a.
2 are connected. Note that each opening of the main body 1, except for the microwave supply port 6, is provided with means for preventing leakage of radio waves.
上記構成において、生ゴミ4は本体1の投入口ネトロン
装置Sへ通電するとマイクロ波が発生し、導波管6a内
を通って供給口6より本体1内へ導入される。マイクロ
波は直接生ゴミ4へ作用する。In the above configuration, when the garbage 4 is energized to the netron device S at the input port of the main body 1, microwaves are generated and introduced into the main body 1 from the supply port 6 through the waveguide 6a. The microwave acts directly on the garbage 4.
一般に生ゴミ4は含水率が高く熱伝導率が低く、しかも
生ゴミどうしの間に空間が多く介在しているため、非常
に外部加熱しにくいが、マイクロ波は瞬時に生ゴミ4の
内部1で加熱する。また、同時に発熱容器2へも作用す
る。発熱容器2は炭化けい素と強誘電体であるチタン酸
バリウムの焼結体で構成されているため、チタン酸バリ
ウムの誘電損相当分の熱を発生し、熱伝導率のよい炭化
けい素により発熱容器7全体が加熱される。この結果、
第2図に示すように発熱容器2内では、生ゴミ4の内部
加熱による熱と発熱容器2からの熱で極めて温度の高い
高温部103が形成され、生ゴミ4をほぼ完全に焼きき
りわずかに白い灰が残るだけとなる。一方、マイクロ波
による加熱が進むと、生ゴミ4は当初水の沸点まで加熱
されどんどん脱水される。そして、脱水が終わると沸点
を越始める。この脱水から発火に至る時点は、くすぶり
状態が生じ煙と臭いが発生する。これはco。In general, food waste 4 has a high water content and low thermal conductivity, and there are many spaces between the food wastes, so it is very difficult to externally heat the food waste. However, microwaves instantly heat the inside of the food waste 4. Heat it up. Moreover, it also acts on the heat generating container 2 at the same time. The heat generating container 2 is composed of a sintered body of silicon carbide and barium titanate, which is a ferroelectric substance, so it generates heat equivalent to the dielectric loss of barium titanate, and due to the good thermal conductivity of silicon carbide, it generates heat equivalent to the dielectric loss of barium titanate. The entire heat generating container 7 is heated. As a result,
As shown in FIG. 2, inside the heat-generating container 2, a high-temperature part 103 with extremely high temperature is formed by the heat generated by the internal heating of the food waste 4 and the heat from the heat-generating container 2, and the food waste 4 is almost completely burnt and only a small amount of heat is generated. Only white ash remains. On the other hand, as the heating by the microwave progresses, the garbage 4 is initially heated to the boiling point of water and is gradually dehydrated. Once dehydration is complete, the boiling point begins to be exceeded. When dehydration leads to ignition, a smoldering state occurs, producing smoke and odor. This is co.
HCやタール性状の未燃焼炭化水素が主な成分である。The main components are unburned hydrocarbons in the form of HC and tar.
これもの排ガスは排気送風機102により吸引され、ハ
ニカム構造で多数の筒状の穴が開口した酸化物触媒体1
00へ送られる。酸化物触媒体100は、結合剤である
アルミン酸石炭内へ、溶融シリカ、チタン酸バリウム、
炭化けい素、二酸化チタンを混ぜて焼結した担体をハニ
カム構造に構成し、二酸化チタンを担持母材とし、白金
族金属を触媒として担持させである。このため、マイク
ロ波を受けると強誘電物質であるチタン酸バリウムの作
用で、酸化物触媒体1oO自体が触媒の機能温度(約2
60℃以上)以上に加熱され、さらに送られて来る排ガ
スも加熱し、触媒効果により排ガスを酸化して、水また
は炭酸ガスに変えて浄化する。このとき、排ガス中の未
燃、焼生成物であるCo、HCの濃度が比較的高いため
、浄化とともに触媒酸化燃焼が発生し発熱するため、酸
化物触媒体1ooの温度は、マイクロ波発熱による温度
をはるかに上回る高温(約8oo℃)に達する。このた
め、排ガス中の酸化処理に適さない臭いの成分もこの温
度域ではほぼ完全に分解してしまい良好な脱臭ができる
ものである。そして、浄化された排ガスは、排気送風機
102によって排気されるものである。This exhaust gas is sucked by an exhaust blower 102, and the oxide catalyst body 1 has a honeycomb structure and has many cylindrical holes.
Sent to 00. The oxide catalyst body 100 contains fused silica, barium titanate,
A carrier made by sintering a mixture of silicon carbide and titanium dioxide is formed into a honeycomb structure, with titanium dioxide used as a support base material and platinum group metal supported as a catalyst. For this reason, when exposed to microwaves, the oxide catalyst body 1oO itself is heated to the functional temperature of the catalyst (approximately 2
The exhaust gas is heated to a temperature of 60°C or higher), and the exhaust gas that is sent is also heated, and the exhaust gas is oxidized by the catalytic effect, converting it into water or carbon dioxide gas and purifying it. At this time, since the concentration of Co and HC, which are unburned and burned products in the exhaust gas, is relatively high, catalytic oxidation combustion occurs along with purification and generates heat, so the temperature of the oxide catalyst body 1oo decreases due to microwave heat generation. reaches a high temperature (approximately 80°C) far above the temperature. Therefore, odor components in the exhaust gas that are not suitable for oxidation treatment are almost completely decomposed in this temperature range, and good deodorization can be achieved. The purified exhaust gas is then exhausted by the exhaust blower 102.
なお本発明では生ゴミが灰となり負荷としてゼロになっ
ても、発熱容器2と酸化物触媒体1o。In addition, in the present invention, even if the garbage becomes ash and the load becomes zero, the heat generating container 2 and the oxide catalyst body 1o.
が負荷として残るためマグネトロン装置5はいわゆる空
だき状態で損傷することはない。また、マイクロ波発熱
のだめの素材としてチタン酸バリウムを用いたが、要は
耐熱性を有する強誘電物質であればよい。まだ、本実施
例では酸化物触媒体を用いたが、デオライト系触媒やイ
ンターカーレション(積層)化合物などのセラミック系
触媒でも同様の効果を奏するものである。remains as a load, so the magnetron device 5 is not damaged in the so-called dry state. Furthermore, although barium titanate was used as the material for the microwave heat generating vessel, any ferroelectric material having heat resistance may be used. Although an oxide catalyst was used in this example, a ceramic catalyst such as a deolite catalyst or an intercalation (layering) compound can also produce similar effects.
発明の効果
以上のように本発明によれば、生ゴミはマイクロ波によ
る、直接の内部加熱と発熱容器からの熱で二重に加熱さ
れて自己燃焼し、そのとき発生する排ガスは酸化物媒体
が自己発熱するため、補助ヒータで再加熱しなくとも完
全に分解される。よって熱エネルギー損失の少ない効率
的な排ガス処理ができるとともに、従来必要であった加
熱ヒータも不要となり、製造コストを低くすることがで
きる。Effects of the Invention As described above, according to the present invention, garbage is heated twice by direct internal heating by microwaves and heat from a heat-generating container and self-combusts, and the exhaust gas generated at that time is an oxide medium. Since it self-heats, it is completely decomposed without reheating with an auxiliary heater. Therefore, efficient exhaust gas treatment with less thermal energy loss is possible, and the heater that was conventionally required is not required, making it possible to reduce manufacturing costs.
第1図は本発明の一実施例の厨芥処理装置の縦断面図、
第2図は同厨芥処理装置の発熱容器の処理状態を示す縦
断面図、第3図は従来の厨芥処理装置を示す縦断面図で
ある。
1・・・・・・本体、2・・・・・・発熱容器、3・・
・・・・投入口、6・・・・・・マグネトロン装置、6
・・・・・・供給口、7・・・・・・給気口、10o・
・・・・・酸化物触媒体、101・・・・・・排気口。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名1−
一一苓怪
2−・発讐算各−
3−−一投入℃
5−−−vり°ネトロンfヒ1
(0イー−1−ズ(τコFIG. 1 is a longitudinal cross-sectional view of a kitchen waste processing apparatus according to an embodiment of the present invention;
FIG. 2 is a longitudinal cross-sectional view showing a processing state of a heat-generating container of the same kitchen waste processing apparatus, and FIG. 3 is a longitudinal cross-sectional view showing a conventional kitchen waste processing apparatus. 1... Body, 2... Heat generating container, 3...
...Input port, 6...Magnetron device, 6
...... Supply port, 7... Air supply port, 10o.
... Oxide catalyst body, 101 ... Exhaust port. Name of agent: Patent attorney Toshio Nakao and 1 other person1-
11 Rekai 2-・Henku calculation each- 3--1 input ℃ 5---vri° Netron fhi 1 (0 E-1-z (τ co)
Claims (2)
られた給気口および排気口と、前記本体内に配置され、
マイクロ波により発熱する発熱容器を備え、前記排気口
にはマイクロ波により発熱する触媒体を設けた厨芥処理
装置。(1) A main body configured as a microwave resonator, an air supply port and an exhaust port provided in the main body, and arranged within the main body,
A kitchen waste processing device comprising a heat generating container that generates heat by microwaves, and a catalyst body that generates heat by microwaves provided at the exhaust port.
をアルミン酸石灰、溶融シリカ、チタン酸バリウム、炭
化けい素、二酸化チタンで担体を構成し、白金族金属を
触媒として担持させた特許請求の範囲第1項記載の厨芥
処理装置。(2) The catalytic body is an oxide catalytic body, and the oxide catalytic body is composed of a support made of lime aluminate, fused silica, barium titanate, silicon carbide, and titanium dioxide, and a platinum group metal is supported as a catalyst. A kitchen waste processing apparatus according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6234286A JPS62218715A (en) | 1986-03-20 | 1986-03-20 | Garbage disposing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6234286A JPS62218715A (en) | 1986-03-20 | 1986-03-20 | Garbage disposing device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62218715A true JPS62218715A (en) | 1987-09-26 |
JPH0573968B2 JPH0573968B2 (en) | 1993-10-15 |
Family
ID=13197351
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6234286A Granted JPS62218715A (en) | 1986-03-20 | 1986-03-20 | Garbage disposing device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62218715A (en) |
-
1986
- 1986-03-20 JP JP6234286A patent/JPS62218715A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH0573968B2 (en) | 1993-10-15 |
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