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JPH081289B2 - Garbage processing equipment - Google Patents
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JPH081289B2 - Garbage processing equipment - Google Patents

Garbage processing equipment

Info

Publication number
JPH081289B2
JPH081289B2 JP61062328A JP6232886A JPH081289B2 JP H081289 B2 JPH081289 B2 JP H081289B2 JP 61062328 A JP61062328 A JP 61062328A JP 6232886 A JP6232886 A JP 6232886A JP H081289 B2 JPH081289 B2 JP H081289B2
Authority
JP
Japan
Prior art keywords
exhaust gas
garbage
food waste
microwave
container
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 - Lifetime
Application number
JP61062328A
Other languages
Japanese (ja)
Other versions
JPS62218711A (en
Inventor
之良 小野
西野  敦
次郎 鈴木
康弘 竹内
主税 掘部
邦義 井戸田
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP61062328A priority Critical patent/JPH081289B2/en
Publication of JPS62218711A publication Critical patent/JPS62218711A/en
Publication of JPH081289B2 publication Critical patent/JPH081289B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)
  • 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発生する生ごみ,古紙
等の焼却装置に関する。
TECHNICAL FIELD The present invention relates to an incinerator for kitchen garbage, waste paper, etc. generated at home or in business.

従来の技術 従来の生ごみ処理装置は、ディスポーザーと呼ばれる
機械的処理装置と、ガス燃料,液体燃料を用いる焼却装
置がある。
2. Description of the Related Art Conventional food waste disposers include mechanical disposers called mechanical disposers and incinerators that use gas fuel or liquid fuel.

前者は、ミキサーに用いられるような刃で、生ごみを
機械的にみじん切りとし、下水に流して処理する方式で
あり、後者は、燃料をバーナで燃焼し、その燃焼熱で生
ごみを焼却してしまうものである。
The former is a method of mechanically chopping raw garbage with a blade such as that used in a mixer and treating it by flowing it into sewage.The latter burns the fuel in a burner and incinerates the garbage by the heat of combustion. It is something that will end up.

また、新しい提案として、マグネトロンを備えた生ご
み処理庫に生ごみを入れ、マイクロ波により生ごみを加
熱して焼却する構成の装置もある。
In addition, as a new proposal, there is also a device in which food waste is put in a food waste processing cabinet equipped with a magnetron and heated by microwave to incinerate.

発明が解決しようとする問題点 しかし、前述した構成の従来の生ごみ処理装置には以
下に示すような問題点がそれぞれある。
Problems to be Solved by the Invention However, the conventional food waste processing apparatuses having the above-described configurations have the following problems, respectively.

ディスポーザーは、機械的に生ごみを細かく処理する
ものの、排水中に含まれる固形分は依然として多く、そ
のため、下水道の詰まりが発生し、大きな社会問題とな
ってきている。
Although the disposer mechanically finely disposes of garbage, the wastewater still contains a large amount of solids, which causes clogging of the sewer system, which has become a major social problem.

燃料により生ごみを焼却する方法は、焼却炉内が高温
化するため外部との断熱を必要とし、燃焼安定性を確保
するために装置が大型化する欠点があった。また、火力
を用いるため火災発生の危険性が大きい。
The method of incinerating food waste with fuel has a drawback that the inside of the incinerator is heated to a high temperature and needs to be insulated from the outside, and the size of the device is increased to ensure combustion stability. Moreover, since fire power is used, there is a high risk of fire.

また、従来のマグネトロンを備えた生ごみ処理装置
は、下水道問題や小型化,安全性共に従来の他の方式の
問題点を解決する特長を有しているものの、まだ、その
構成において不充分なものであり、特に、排ガス臭気が
著しく悪いという欠点を有している。
Further, the conventional garbage disposal device equipped with a magnetron has the characteristics of solving the problems of other conventional methods such as sewerage problems, downsizing, and safety, but its structure is still insufficient. In particular, it has a drawback that the odor of exhaust gas is extremely bad.

本発明は、上記従来の問題点を解決するためになされ
たものであり、下水問題がなく、小型化,安全性共に優
れ、かつ排ガス臭気が著しく低減された生ごみ処理装置
を提供するものである。
The present invention has been made to solve the above-mentioned conventional problems, and provides a food waste treatment device that has no sewage problem, is small in size, has excellent safety, and has significantly reduced exhaust gas odor. is there.

問題点を解決するための手段 本発明は、少なくとも、マグネトロン,空気供給口,
および排ガス流出口を有する生ごみ処理庫と、前記生ご
み処理庫内に設置された生ごみ容器と、前記生ごみ処理
庫の排ガス流出口に連結する排ガス流路中に設けられた
触媒体と、前記生ごみ処理庫内に空気を供給する給気装
置とを備え、かつ、生ごみ処理庫からの排ガスと、供給
空気との熱交換を行なう熱交換器を、生ごみ処理庫から
触媒体に至る排ガス流路中に設置した生ごみ処理装置の
構成としたものである。
Means for Solving the Problems The present invention includes at least a magnetron, an air supply port,
And a garbage disposal having an exhaust gas outlet, a garbage container installed in the garbage disposal, and a catalyst body provided in an exhaust gas passage connected to the exhaust outlet of the garbage disposal. A heat exchanger for exchanging heat between the exhaust gas from the food waste processing warehouse and the supply air, comprising a gas supply device for supplying air into the food waste processing warehouse. This is the configuration of the food waste treatment device installed in the exhaust gas flow path leading to.

作用 上記構成の生ごみ処理装置において、生ごみ処理中に
生ごみから発生する未燃焼炭化水素化合物およびその不
完全燃焼生成物の臭気成分を多量に含む排ガスが庫内よ
り放出される。この排ガスはあらかじめヒータにより加
熱−活性化された触媒体に通じ、上記臭気成分の浄化が
行なわれる。ここで生ごみ処理庫と、触媒との間には熱
交換器を設置しているので、排ガス中に含まれる多量の
水分をこの熱交換器により凝縮・除去するとともに、生
ごみ処理に用いる供給空気を加熱し、生ごみの燃焼を円
滑に行なうものである。また、触媒に与えられる排ガス
は水分が除かれているので、触媒活性が保たれ、排ガス
臭気を著しく低減することができることとなる。
Action In the food waste treating apparatus having the above structure, exhaust gas containing a large amount of unburned hydrocarbon compounds generated from food waste during the garbage processing and odor components of incomplete combustion products thereof is discharged from the inside of the warehouse. This exhaust gas is passed through a catalyst body that has been heated and activated in advance by a heater to purify the odorous components. Since a heat exchanger is installed between the food waste treatment cabinet and the catalyst, a large amount of water contained in the exhaust gas is condensed and removed by this heat exchanger and supplied for the food waste treatment. It heats air to smoothly combust food waste. Further, since the exhaust gas given to the catalyst has no water content, the catalytic activity is maintained and the exhaust gas odor can be remarkably reduced.

実施例 以下本発明の一実施例を図面にもとづき説明する。図
において16は生ごみ処理庫であり、前記扉13を有し、内
部には生ごみ容器4を出し入れ自在に設けている。この
生ごみ容器4は側壁に貫通孔12を有するとともに内底に
マイクロ波吸収セラミック5を有し、生ごみ17を収容し
ている。前記生ごみ処理庫16の上部にはマグネトロン1
を設備し、マイクロ波がマイクロ波透過隔壁15を透して
生ごみ処理庫16内に放射されるようになっており、生ご
み処理庫16内にマイクロ波拡散装置14を設備し、マグネ
トロン1近くにはマグネトロン冷却ファン18を設けてい
る。
Embodiment An embodiment of the present invention will be described below with reference to the drawings. In the figure, reference numeral 16 is a garbage disposal, which has the door 13 and in which the garbage container 4 can be freely inserted and taken out. This food waste container 4 has a through hole 12 in its side wall and a microwave absorbing ceramic 5 in its inner bottom, and stores food waste 17. A magnetron 1 is placed on the upper part of the garbage disposal 16.
The microwave is transmitted through the microwave transmitting partition wall 15 to be radiated into the garbage disposal 16 and the microwave diffusing device 14 is installed in the garbage disposal 16. A magnetron cooling fan 18 is provided nearby.

前記生ごみ処理庫16はその上部に排ガス流出口2を有
するとともに、下部に空気供給口3を有している。前記
排ガス流出口2からは熱交換器7と触媒8を通る排気通
路が形成され、空気供給口3には送風機6より前記熱交
換器7を通る空気供給路が接続されている。そして熱交
換器7からはドレンパイプ10を導出し、ドレンポット11
で受水するようにしている。なお、触媒8には触媒加熱
ヒータ9が付設してある。
The food waste processing cabinet 16 has an exhaust gas outlet 2 at its upper portion and an air supply port 3 at its lower portion. An exhaust passage passing through the heat exchanger 7 and the catalyst 8 is formed from the exhaust gas outlet 2, and an air supply passage from the blower 6 passing through the heat exchanger 7 is connected to the air supply inlet 3. Then, the drain pipe 10 is led out from the heat exchanger 7, and the drain pot 11
I try to receive water at. A catalyst heater 9 is attached to the catalyst 8.

前記熱交換器7は、排ガス流出口2から送られてくる
生ごみ処理排ガスを冷却し、排ガス中に含まれる多量の
水分を凝縮,除去する機能を有し、また同時に、送風機
6より送られてくる生ごみ処理用空気を加熱し、温風と
して生ごみ処理庫16内に供給する機能をもっている。そ
して熱交換器7で凝縮した凝縮水は、ドレンパイプ10を
経て、ドレンポット11に蓄積されるようになっており、
したがってドレンポット11は、凝縮水がドレンポット11
内にいっぱいになった際、容易に捨てられるように着脱
自在な構成となっている。
The heat exchanger 7 has a function of cooling the food waste treatment exhaust gas sent from the exhaust gas outlet 2 and condensing and removing a large amount of water contained in the exhaust gas. At the same time, the heat exchanger 7 is sent by the blower 6. It has a function of heating the incoming food waste processing air and supplying it as hot air into the food waste processing cabinet 16. Then, the condensed water condensed in the heat exchanger 7 is adapted to be accumulated in the drain pot 11 via the drain pipe 10.
Therefore, in the drain pot 11, condensed water is drained from the drain pot 11.
It is removable so that it can be easily discarded when it is full.

前記生ごみ容器4は、マイクロ波透過性物質で形成さ
れることが望ましく、マイクロ波浸透深さ1m以上の無機
焼結体,燃焼体,ガラス体が望ましい、これは、マイク
ロ波透過性が悪い物質(マイクロ波吸収体)を用いて生
ごみ容器とした場合、容器自身がマイクロ波により高温
化し、装置使用を重ねるごとに、容器にかかる急熱急冷
によって、容器が破損しやすいためである。また、上述
したマイクロ波透過性容器を用いる場合、容器内にマイ
クロ波吸収セラミック5を用いることが望ましい。これ
は、生ごみ焼却後もマグネトロンが作動していた場合、
マイクロ波を吸収する物質が処理庫内にないと、マグネ
トロン自身を破損する危険性があるためである。さらに
生ごみ処理容器壁には、生ごみ燃焼安定性のために貫通
孔12を設けることが望ましい。
The food waste container 4 is preferably formed of a microwave permeable material, and is preferably an inorganic sintered body, a combustion body, or a glass body having a microwave penetration depth of 1 m or more, which has poor microwave permeability. This is because when a raw garbage container is made of a substance (microwave absorber), the container itself is heated to a high temperature by microwaves, and the container is likely to be damaged by rapid heating and rapid cooling applied each time the device is used. When using the above-mentioned microwave permeable container, it is desirable to use the microwave absorbing ceramic 5 in the container. This is because if the magnetron was still operating after the garbage was incinerated,
This is because there is a risk of damaging the magnetron itself if there is no substance that absorbs microwaves in the processing chamber. Further, it is desirable to provide a through hole 12 on the wall of the raw garbage processing container for the stability of raw garbage burning.

次に本実施例の動作について説明する。まず、生ごみ
17を入れた生ごみ容器4を、前扉13から、生ごみ処理庫
16内に入れ、図のように設置する。次に、作動スイッチ
(図示せず)を入れると、まず触媒加熱用ヒータ9に通
電され触媒8が加熱される。触媒体が、充分活性化温度
まで加熱されると、送風機6,マグネトロン1,マグネトロ
ン冷却ファン18,マイクロ波拡散装置が作動開始する。
生ごみ容器4に入っている生ごみ17は、マグネトロン1
から発生するマイクロ波を吸収し、急速に加熱される。
なお、マグネトロン1と生ごみ処理庫16内の間に、マイ
クロ波透過隔壁15を設けてあるのでマグネトロン1は保
護される。マイクロ波を吸収した生ごみ17はまず水分を
放出して脱水される。生ごみより発生した水蒸気は、空
気供給口3より入ってくる供給空気と共に、排ガス流出
口2より熱交換器7に送られる。熱交換器7では、排ガ
ス中に含まれる水分を大部分凝縮して除去する。熱交換
器7で水分除去した排ガスは触媒8に送られ、ここで、
排ガス中に含まれる臭気成分が浄化され、外気に放出さ
れる。前記した脱水生ごみは、さらにマイクロ波を吸収
し、急速に加熱され、一部が炭化するようになる。前述
したように、マグネトロン1によって作り出される強力
な電界のために、上記生ごみの炭化部分に対して、庫内
で断続的に放電がおこり、それまでに生ごみ容器4内に
たまっていた生ごみ分解可燃性ガスが、この放電により
着火する。上記可燃ガスの燃焼熱およびマイクロ波照射
により、生ごみは燃焼しつづけ、灰化するまでこの燃焼
は継続される。生ごみ処理終了は、予め生ごみ処理量に
応じて設定されたタイマー(図示せず)によって行なわ
れる。生ごみ処理後に照射されたマイクロ波は、マイク
ロ波吸収セラミック5により吸収される。
Next, the operation of this embodiment will be described. First, raw garbage
From the front door 13, put the garbage container 4 containing 17 into the garbage container.
Place in 16 and install as shown. Next, when the operation switch (not shown) is turned on, the catalyst heating heater 9 is first energized to heat the catalyst 8. When the catalyst body is sufficiently heated to the activation temperature, the blower 6, the magnetron 1, the magnetron cooling fan 18, and the microwave diffusion device start operating.
The garbage 17 contained in the garbage container 4 is the magnetron 1
It absorbs the microwaves generated by and is heated rapidly.
In addition, since the microwave transmitting partition wall 15 is provided between the magnetron 1 and the inside of the garbage disposal 16, the magnetron 1 is protected. The garbage 17 that has absorbed microwaves is first dehydrated by releasing water. The water vapor generated from the garbage is sent to the heat exchanger 7 from the exhaust gas outlet 2 together with the supply air entering from the air supply port 3. In the heat exchanger 7, most of the water contained in the exhaust gas is condensed and removed. The exhaust gas from which water has been removed by the heat exchanger 7 is sent to the catalyst 8, where
The odorous components contained in the exhaust gas are purified and released to the outside air. The above-mentioned dehydrated food waste further absorbs microwaves and is rapidly heated to be partially carbonized. As described above, due to the strong electric field generated by the magnetron 1, the carbonized portion of the food waste is intermittently discharged in the warehouse, and the raw food accumulated in the food waste container 4 by that time. The combustible gas that decomposes dust is ignited by this discharge. Due to the heat of combustion of the combustible gas and microwave irradiation, the garbage continues to burn, and this combustion is continued until it is ashed. The end of the garbage processing is performed by a timer (not shown) set in advance according to the amount of garbage processed. The microwave applied after the garbage processing is absorbed by the microwave absorbing ceramic 5.

前記のように熱交換器7を設けることにより、排ガス
中に含まれる水分を除去し、触媒8の水蒸気による被毒
を防止し、触媒活性の低下を防止することができるた
め、外気に放出される排ガスの臭気を低減することがで
き、特に、排ガス中の含有水分量が多い生ごみ処理初期
の段階での排ガス臭気を著しく低減できる。また、同時
に、供給空気も加熱されるため、生ごみ処理庫16内の生
ごみ燃焼も改善され、排ガス流出口から出る排ガス中の
臭気自体も低減することができた。
By providing the heat exchanger 7 as described above, it is possible to remove the water contained in the exhaust gas, prevent the catalyst 8 from being poisoned by water vapor, and prevent the catalyst activity from decreasing, so that it is released to the outside air. The odor of exhaust gas can be reduced, and in particular, the odor of exhaust gas can be significantly reduced at the early stage of treating garbage containing a large amount of water content in the exhaust gas. At the same time, since the supplied air is also heated, the garbage combustion in the garbage disposal 16 was improved, and the odor itself in the exhaust gas from the exhaust gas outlet could be reduced.

なお、本実施例において、送風機6は空気供給口3以
前に設けたが、本発明はこれに限定されるわけではな
く、たとえば吸気ファンを触媒8の後に設置し、空気を
吸引して庫内に導入してもよい。
In addition, in the present embodiment, the blower 6 is provided before the air supply port 3, but the present invention is not limited to this. For example, an intake fan is installed after the catalyst 8 and air is sucked in the chamber. May be introduced into.

発明の効果 上記実施例の説明より明らかなように、本発明によれ
ば、生ごみ処理庫への供給空気および生ごみ処理庫より
の排ガスを熱交換器を通すため、排ガス中の水分が効率
的に除去できるとともに、排ガス臭気が著しく低減さ
れ、また下水問題がなく、小型,安定性ともにすぐれた
生ごみ処理装置を得ることができる。
EFFECTS OF THE INVENTION As is clear from the description of the above embodiments, according to the present invention, the air supplied to the garbage disposal and the exhaust gas from the garbage disposal pass through the heat exchanger, so that the moisture in the exhaust gas is efficient. It is possible to obtain a garbage processing device that can be removed efficiently, the odor of exhaust gas is significantly reduced, there is no problem of sewage, and the size and stability are excellent.

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

図は本発明の一実施例の生ごみ処理装置の断面図であ
る。 1……マグネトロン、2……排ガス流出口、3……空気
供給口、4……生ごみ容器、6……送風機、7……熱交
換器、8……触媒、16……生ごみ処理庫。
FIG. 1 is a sectional view of a food waste processing device according to an embodiment of the present invention. 1 ... Magnetron, 2 ... Exhaust gas outlet, 3 ... Air supply port, 4 ... Garbage container, 6 ... Blower, 7 ... Heat exchanger, 8 ... Catalyst, 16 ... Garbage disposal cabinet .

───────────────────────────────────────────────────── 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 F26B 23/08 C (72)発明者 西野 敦 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 鈴木 次郎 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 竹内 康弘 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 掘部 主税 大阪府大阪市城東区今福西6丁目2番61号 松下精工株式会社内 (72)発明者 井戸田 邦義 大阪府大阪市城東区今福西6丁目2番61号 松下精工株式会社内 (56)参考文献 特開 昭58−133817(JP,A) 特開 昭52−26034(JP,A) 特開 昭54−43331(JP,A) 特開 昭55−95019(JP,A) 特開 昭52−151266(JP,A) 特公 昭62−22072(JP,B2) 特公 昭53−44694(JP,B2)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Internal reference number FI Technical display location F26B 23/08 C (72) Inventor Atsushi Nishino 1006 Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Inventor Jiro Suzuki, 1006, Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Inventor, Yasuhiro Takeuchi, Kadoma, Osaka Prefecture 1006 Kadoma, Matsushita Electric Industrial Co., Ltd. (72) Inventor, excavator Main tax 6-61, Imafukunishi, Joto-ku, Osaka, Osaka Prefecture Matsushita Seiko Co., Ltd. (72) Inventor, Kuniyoshi Iwata 6-61, Imafukunishi, Joto-ku, Osaka, Osaka (56) Reference (56) Reference References JP-A-58-133817 (JP, A) JP-A-52-26034 (JP, A) JP-A-54-43331 (JP, A) JP-A-55-95019 (JP, A) JP-A-5 2-151266 (JP, A) JP 62-22072 (JP, B2) JP 53-44694 (JP, B2)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】少なくとも、マグネトロン、空気供給口お
よび排ガス流出口を有する生ごみ処理庫と、前記生ごみ
処理庫内に設置された生ごみ容器と、前記生ごみ処理庫
の排ガス流出口に連結する排ガス流路中に設けられた触
媒体と、前記生ごみ処理庫内に空気を供給する給気装置
とを備え、生ごみ処理庫からの排ガスと、供給空気との
熱交換により排ガスを冷却し、排ガス中の水分の除湿を
行なう熱交換器を、生ごみ処理庫から触媒体へ至る排ガ
ス流路中に設置し、かつ前記生ごみ容器がマイクロ波透
過性で、生ごみ容器内にマイクロ波吸収体を備えた生ご
み処理装置。
1. A food waste treating cabinet having at least a magnetron, an air supply port and an exhaust gas outlet, a garbage container installed in the garbage treating cabinet, and an exhaust gas outlet of the garbage treating cabinet. A catalyst provided in the exhaust gas flow path and an air supply device that supplies air into the food waste processing cabinet, and the exhaust gas from the food waste processing cabinet and the exhaust gas are cooled by heat exchange with the supply air. Then, a heat exchanger for dehumidifying the water content in the exhaust gas is installed in the exhaust gas flow path from the garbage disposal to the catalyst body, and the garbage container is microwave permeable and the microwave inside the garbage container is Garbage disposal device with wave absorber.
JP61062328A 1986-03-20 1986-03-20 Garbage processing equipment Expired - Lifetime JPH081289B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61062328A JPH081289B2 (en) 1986-03-20 1986-03-20 Garbage processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61062328A JPH081289B2 (en) 1986-03-20 1986-03-20 Garbage processing equipment

Publications (2)

Publication Number Publication Date
JPS62218711A JPS62218711A (en) 1987-09-26
JPH081289B2 true JPH081289B2 (en) 1996-01-10

Family

ID=13196959

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61062328A Expired - Lifetime JPH081289B2 (en) 1986-03-20 1986-03-20 Garbage processing equipment

Country Status (1)

Country Link
JP (1) JPH081289B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01163516A (en) * 1987-12-18 1989-06-27 Matsushita Electric Ind Co Ltd Incinerator
JPH02223712A (en) * 1989-02-23 1990-09-06 Matsushita Electric Ind Co Ltd High frequency wave incinerator with dryer
JP4040007B2 (en) * 2003-09-29 2008-01-30 三洋電機株式会社 Garbage disposal equipment

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5226034A (en) * 1975-08-20 1977-02-26 Matsushita Electric Ind Co Ltd Oil burner
JPS5443331A (en) * 1977-09-12 1979-04-05 Hitachi Ltd Steam turbine plant
JPS5653316A (en) * 1979-10-05 1981-05-12 Hitachi Zosen Corp Waste heat recovery system at waste incineration plant
JPS58133817A (en) * 1982-02-02 1983-08-09 Brother Ind Ltd Treating device of waste

Also Published As

Publication number Publication date
JPS62218711A (en) 1987-09-26

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