JPS62153620A - Structure of combustible discharged gas incinerator device using microwave - Google Patents

Structure of combustible discharged gas incinerator device using microwave

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Publication number
JPS62153620A
JPS62153620A JP29219885A JP29219885A JPS62153620A JP S62153620 A JPS62153620 A JP S62153620A JP 29219885 A JP29219885 A JP 29219885A JP 29219885 A JP29219885 A JP 29219885A JP S62153620 A JPS62153620 A JP S62153620A
Authority
JP
Japan
Prior art keywords
microwave
furnace
incineration
chamber
exhaust gas
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
JP29219885A
Other languages
Japanese (ja)
Inventor
Mitsuhiko Nomi
能見 光彦
Junichi Yamaji
山路 順一
Toyoji Mizushima
水島 豊史
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP29219885A priority Critical patent/JPS62153620A/en
Publication of JPS62153620A publication Critical patent/JPS62153620A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To enable microwave to be effectively supplied to a microwave absorbing material at a bottom part of an incineration chamber by a method wherein a port of radiation of microwave arranged at a top part of the incineration device is made as a funnel shape and a metallic plate is fixed to an upper furnace wall of a hot incineration furnace chamber. CONSTITUTION:A port 20 for radiation of microwave is made as a funnel shape and a microwave is efficiently supplied to a hot temperature incineration furnace chamber 18 through a microwave transmitting furnace material 17. A metallic plate 21 having a nature of reflecting the microwave is fixed to the upper incineration furnace wall of a hot temperature incineration furnace, the microwave is not absorbed at the upper part of the incineration chamber of hot incineration furnace and the microwave can effectively be supplied to the microwave absorption ceramics furnace material 15 and the furnace bottom plate 16. Therefore, since the bottom part of the hot temperature incineration device is heated to a hot temperature, the processing gas supplied from the bottom part of the incineration furnace starts to ignite at the bottom part, the upper part of the furnace is heated with the combustion heat, so as entire incineration chamber 18 can uniformly be heated up to a hot temperature and the processing gas can be processed better.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、マイクロ波エネルギを利用して、可燃性排ガ
ス又は有害成分含有排ガスを酸化燃焼または分解処理す
るだめの焼却炉に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an incinerator that uses microwave energy to oxidize, burn, or decompose combustible exhaust gas or exhaust gas containing harmful components.

〔従来の技術及びその問題点〕[Conventional technology and its problems]

従来、例えば、高分子プラスチック材等からなる廃棄物
を焼却する場合、炉内で多量の可燃性ガス、タール分、
油煙及び/又は有害ガスが発生する。これらは、同一の
焼却炉内で完全に燃焼させることは難かしく、また完全
に燃焼させるためには、炉の大きさを処理量に対し大容
量の炉とし、炉内温度を常に高温に保つようにする必要
があり、このような炬を用いて焼却するのは効率的な方
法であるとは言い難い。
Conventionally, when incinerating waste made of polymeric plastic materials, for example, a large amount of flammable gas, tar, etc.
Oil smoke and/or harmful gases are generated. It is difficult to completely burn these in the same incinerator, and in order to burn them completely, the size of the furnace should be large enough to handle the amount of waste, and the temperature inside the furnace should always be kept high. It is difficult to say that incineration using such a torch is an efficient method.

・この対策として、通常の焼却炉においては、その焼却
排ガスの出口の部分に、高温に加熱できる二次燃焼炉を
設け、この炉中で朱紫分を完全に燃焼させる方法を採用
しており、この方法は有効ではあるが二次燃焼炉は高温
に保つ必要があシ、その為補助燃料供給バーナーの設置
等炉の構造が複雑となり、またその制御が繁雑となる等
の問題点があった。
・As a countermeasure for this, in ordinary incinerators, a secondary combustion furnace that can be heated to a high temperature is installed at the outlet of the incineration exhaust gas, and a method is adopted in which the vermilion is completely combusted in this furnace. Although this method is effective, it is necessary to maintain the secondary combustion furnace at a high temperature, which makes the furnace structure complicated, such as installing an auxiliary fuel supply burner, and its control becomes complicated. Ta.

本発明者らは、このような問題点を解決する手段として
さきに、炉中のマイクロ波を吸収する性質を有する材料
にマイクロ波を照射することにより高温に保持されてい
る炉に、可燃性排ガス或いは有害成分含有排ガスを通し
、可燃性成分或いは有害成分を酸化或いは分解する方法
並びに該方法を実施するための焼却炉を提案した(特願
昭59−272067号、実願昭59−195298号
、実願昭59−195300号)。
As a means to solve these problems, the present inventors first developed a material that absorbs microwaves in the furnace by irradiating microwaves to a material that absorbs microwaves. We proposed a method of oxidizing or decomposing flammable or harmful components through exhaust gas or exhaust gas containing harmful components, and an incinerator for carrying out the method (Japanese Patent Application No. 59-272067, Utility Application No. 59-195298) , Utility Application No. 59-195300).

この方法は、マイクロ波を吸収する性質を有する材料に
マイクロ波を照射することにより高温に保持された炉中
に可燃性排ガス或いは有害成分含有排ガスを通すことに
より、即ち該炉を二次燃焼炉として用いることによシ、
簡単な装置で未燃分を完全に燃焼せしめ、捷た有害成分
を完全に分解せしめるものである。
This method involves passing flammable exhaust gas or exhaust gas containing harmful components through a furnace that is maintained at a high temperature by irradiating microwaves onto a material that absorbs microwaves, that is, converting the furnace into a secondary combustion furnace. It can be used as
This is a simple device that completely burns unburned substances and completely decomposes the hazardous components that have been broken down.

つぎに、この以前に提案した焼却炉及びその運転方法を
第2図及び第5図に基いて説明する。
Next, the previously proposed incinerator and its operating method will be explained with reference to FIGS. 2 and 5.

@2図は焼却炉の一例を示すもので、その断面概略図を
示し、符号1は可燃性排ガス或いは有害成分含有排ガス
の入口部、2は処理された排ガスの出口部、3はマイク
ロ波導入口、4は断熱材層、5はマイクロ波を吸収する
性質を有する粒状、板状又は塊状の材料からなる充填層
、6は高温炉室、7は上部炉室、8は排ガスの通過する
多数の穴を有する充填材支持板(炉底板)を示す。
Figure @2 shows an example of an incinerator, and shows a schematic cross-sectional view of the incinerator, where 1 is an inlet for flammable exhaust gas or exhaust gas containing harmful components, 2 is an outlet for treated exhaust gas, and 3 is a microwave inlet. , 4 is a heat insulating material layer, 5 is a packed layer made of granular, plate-like or block-like material having the property of absorbing microwaves, 6 is a high-temperature furnace chamber, 7 is an upper furnace chamber, and 8 is a large number of holes through which exhaust gas passes. A filler support plate (furnace bottom plate) with holes is shown.

マイクロ波導入口3から印加されたマイクロ波はマイク
ロ波を吸収する性質を有する粒状、板状又は塊状の材料
からなる充填層5に吸収され、該充填層は高温に加熱さ
れる。可燃性排ガス入口部1から導入される可燃性排ガ
スは、該高温に加熱された充填材と接触して高温に加熱
され高温炉室6中で、ガス中の可燃分をほぼ完全に燃焼
させることができる。また、マイクロ波出力を制御する
ことにより充填層を900℃またはそれ以上の温度に容
易に加熱することができるので、プラスチック廃棄物等
の焼却排ガス中に含有されているタール分も容易に燃焼
させることが可能であり、また該焼却排ガス中に含まれ
ているアンモニア或いはシアン等も容易に分解すること
ができる。
Microwaves applied from the microwave inlet 3 are absorbed by the packed bed 5 made of a granular, plate-like, or block-like material that has the property of absorbing microwaves, and the packed bed is heated to a high temperature. The combustible exhaust gas introduced from the combustible exhaust gas inlet 1 comes into contact with the heated filling material and is heated to a high temperature to almost completely burn the combustible content in the gas in the high temperature furnace chamber 6. I can do it. In addition, by controlling the microwave output, the packed bed can be easily heated to a temperature of 900°C or higher, making it easy to burn tar contained in the exhaust gas from incineration of plastic waste, etc. Furthermore, ammonia, cyanide, etc. contained in the incineration exhaust gas can be easily decomposed.

なお、第2図に示す例において、充填層として用いるマ
イクロ波吸収材の粒径は5sm〜10調程度の大きさの
ものでよく、また100++m〜300簡の厚さに充填
すれば十分である。
In the example shown in FIG. 2, the particle size of the microwave absorbing material used as the packed layer may be about 5 sm to 10 sm, and it is sufficient to fill it to a thickness of 100 ++ m to 300 sm. .

また、マイクロ波の排ガス入口部からの漏洩を防止する
ため、炉底板8もマイクロ波吸収材で製造するのが好ま
しい。
Furthermore, in order to prevent microwaves from leaking from the exhaust gas inlet, the furnace bottom plate 8 is also preferably made of a microwave absorbing material.

マイクロ波吸収材としては、SiC,TiO2、Al2
O2、イルメナイト、Fe2O3、S ic+s i3
N4 、ZrO2、CaO砂等マイクロ波を吸収すると
共に耐熱性を有する<)のが用いられるが、マイクロ波
の吸収特性等から、SiC,TiO2、イルメナイト、
BaTiO3又はF e203、特に5iC1Ti02
が好ましい。
As microwave absorbing materials, SiC, TiO2, Al2
O2, ilmenite, Fe2O3, S ic+s i3
N4, ZrO2, CaO sand, etc. that absorb microwaves and have heat resistance are used; however, due to their microwave absorption characteristics, SiC, TiO2, ilmenite,
BaTiO3 or Fe203, especially 5iC1Ti02
is preferred.

つぎに第2図に示したものとは異なる型の焼却炉を第3
図に示す。
Next, we installed a third incinerator of a different type than the one shown in Figure 2.
As shown in the figure.

第3図において、符号11は可燃性排ガス又は有毒成分
含有排ガス入口部、12は処理された排ガス排出口、1
3はマイクロ波尋人管、14は断熱材、15はマイクロ
波吸収材よシなる炉壁、16はマイクロ波吸収材よシな
る排ガス通路を設けた炉底板、17は燃焼ガス通路を設
けたマイクロ波透過性耐熱材よりなる多孔板、18は高
温炉室、19は上部炉室を示す。
In FIG. 3, reference numeral 11 indicates an inlet of flammable exhaust gas or an exhaust gas containing toxic components, 12 indicates a treated exhaust gas outlet, and 1
3 is a microwave pipe, 14 is a heat insulating material, 15 is a furnace wall made of a microwave absorbing material, 16 is a furnace bottom plate with an exhaust gas passage made of a microwave absorbing material, and 17 is a combustion gas passage. A perforated plate made of a microwave permeable heat resistant material, 18 is a high temperature furnace chamber, and 19 is an upper furnace chamber.

マイクロ波導入’f11sから印加されたマイクロ波は
、マイクロ波透過性耐熱材多孔板17を透過し、高温炉
室18内のマイクロ波吸収材よりなる壁15及び炉底板
16に吸収され、その結果該壁及び炉底板が高温に加熱
されるので、その輻射熱によυ高温炉室6中は高温とな
る。
The microwave applied from the microwave introduction 'f11s passes through the microwave-transparent heat-resistant material porous plate 17 and is absorbed by the wall 15 and the furnace bottom plate 16 made of microwave absorbing material in the high-temperature furnace chamber 18. As a result, Since the walls and the furnace bottom plate are heated to a high temperature, the inside of the high-temperature furnace chamber 6 becomes high temperature due to the radiant heat.

そして可燃性排ガス入口部から導入される可燃性ガスは
、前記輻射熱により高温に加熱され、排ガス中に含まれ
ている酸素により排ガス中の可燃物は燃焼せしめられた
後上部炉室19を経て排出口12より徘呂される。
The combustible gas introduced from the combustible exhaust gas inlet is heated to a high temperature by the radiant heat, and the combustibles in the exhaust gas are combusted by the oxygen contained in the exhaust gas, after which it is discharged through the upper furnace chamber 19. He wandered through exit 12.

高温炉室18の上部に設けたマイクロ波透過性耐熱材よ
りなる多孔板17は、高温炉室内における輻射熱による
加熱効果を向上させるためのものであって、この多孔板
17は無くてもよい。多孔板17の材質としては、石英
、窒化ケイ素等を使用でき、またマイクロ波を多少吸収
する性質を有するもの、例えばアルミナを素材とするも
のを用いてもよい。
A perforated plate 17 made of a microwave-transparent heat-resistant material provided in the upper part of the high-temperature furnace chamber 18 is for improving the heating effect of radiant heat in the high-temperature furnace chamber, and the perforated plate 17 may be omitted. As the material of the perforated plate 17, quartz, silicon nitride, etc. can be used, and a material having a property of absorbing microwaves to some extent, such as a material made of alumina, may also be used.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

上記マイクロ波エネルギーを利用した焼却炉においては
、 ■ 炉頂部に直接マイクロ波導波管を取り付けているた
め、マイクロ波が効率良く炉内へ導入されにくく、また ■ 高温炉室に照射されたマイクロ波は炉室上部でその
大部分が吸収されるため、炉室内の温度分布は下部が低
(上部が高い状態となり、炉室内で処理ガスを効率良く
処理できないという欠点があった。
In the above-mentioned incinerator that uses microwave energy, ■ Because the microwave waveguide is directly attached to the top of the furnace, it is difficult for microwaves to be efficiently introduced into the furnace, and ■ Microwaves irradiated into the high-temperature furnace chamber are Most of the gas is absorbed in the upper part of the furnace chamber, so the temperature distribution inside the furnace chamber is low at the bottom (high at the top), which has the disadvantage that the process gas cannot be processed efficiently in the furnace chamber.

〔問題点を解決するだめの手段〕[Failure to solve the problem]

本発明は前記欠点を除去するためになされたものであっ
て、炉中のマイクロ波を吸収する性質を有する材料にマ
イクロ波を照射することにより高温に保持されている炉
に、可燃性ガス或いは有害成分含有ガスを通して可燃性
成分或いは有害成分を酸化燃焼或いは分解せしめる炉に
おいて、炉頂部に設けたマイクロ波照射口部をラッパ状
形状とすることによりマイクロ波を一室全域に均一に導
入できるようにしたものであり、また、炉頂部に設けた
マイクロ波照射口部をラッパ状形状とすると共に、高温
炉室上部炉壁に金属板を取りつけることによりマイクロ
波を炉室底部のマイクロ波吸収材に有効に供給できるよ
うにしだものであって、マイクロ数を効率よく利用でき
るようにしたものである。
The present invention has been made in order to eliminate the above-mentioned drawbacks, and the present invention has been made to remove flammable gas or In a furnace that oxidizes, burns, or decomposes combustible or harmful components through gas containing harmful components, the microwave irradiation port provided at the top of the furnace is shaped like a trumpet so that microwaves can be uniformly introduced throughout the room. In addition, the microwave irradiation port provided at the top of the furnace has a trumpet-like shape, and a metal plate is attached to the upper furnace wall of the high-temperature furnace chamber, so that microwaves are transmitted through the microwave absorbing material at the bottom of the furnace chamber. It is designed to be able to effectively supply microorganisms, and to make efficient use of micro-numbers.

以下、第1図に基いて本発明の詳細な説明する。Hereinafter, the present invention will be explained in detail based on FIG.

第1図は、第5図に示す焼却炉に本発明を適用したもの
で、第3図の符号と同じ符号は第3図について説明した
ものと同じ意味を有し、符号20はラッパ状形状とした
マイクロ波照射口部を示し、該部分は上部炉室19を兼
ねているものであり、21は高温炉室18の上部壁に取
り付けた金属板を示す。第1図に示す焼却炉においては
、マイクロ波を吸収するセラミックス炉材は高温炉室の
下部のみに設けているが、金属板21を取りつけない場
合には、第3図に示す焼却炉と同様高温炉室の上部壁面
にも設けてよいことは当然である。
FIG. 1 shows an incinerator in which the present invention is applied to the incinerator shown in FIG. 5. The same reference numerals as those in FIG. This portion also serves as the upper furnace chamber 19, and 21 indicates a metal plate attached to the upper wall of the high temperature furnace chamber 18. In the incinerator shown in Fig. 1, the ceramic furnace material that absorbs microwaves is provided only in the lower part of the high-temperature furnace chamber, but if the metal plate 21 is not attached, it is similar to the incinerator shown in Fig. 3. It goes without saying that it may also be provided on the upper wall surface of the high temperature furnace chamber.

、 第1図に示す焼却炉の運転方法は、第3図について
説明したのと全く同様であるが、第1図に示す焼却炉に
おいては、マイクロ波照射口部をラッパ状形状としたた
め、マイクロ波がマイクロ波透過炉材17を通して効率
よく高温炉室へ供給され、高温炉室上部炉壁にマイクロ
波を反射する性質のある金属板を取シ付けてちるため、
マイクロ波が高温炉室上部で吸収されることなく、高温
炉室の下部炉壁を構成するマイクロ波吸収セラミックス
炉材及びマイクロ波吸収セラミックス製の炉底板に有効
に供給できるの工 で、高温へ底部が高温に加熱されるため、・炉底部より
供給された処理ガスは、底部に警いて燃焼を開始し、こ
の燃焼熱により炉の上部が加熱されるようになるため、
高温炉室全体をほぼ均一な高温状態とすることができる
ため、処理ガスを良好に処理できるものである。
The operating method of the incinerator shown in Fig. 1 is exactly the same as that explained with reference to Fig. 3, but in the incinerator shown in Fig. 1, the microwave irradiation port is shaped like a trumpet, so that the microwave Waves are efficiently supplied to the high-temperature furnace chamber through the microwave transmission furnace material 17, and a metal plate that reflects microwaves is attached to the upper furnace wall of the high-temperature furnace chamber.
This technology allows microwaves to be effectively supplied to the microwave-absorbing ceramic furnace material and the microwave-absorbing ceramic furnace bottom plate that make up the lower wall of the high-temperature furnace chamber without being absorbed in the upper part of the high-temperature furnace chamber. Because the bottom is heated to a high temperature, the processing gas supplied from the bottom of the furnace starts burning at the bottom, and this combustion heat heats the top of the furnace.
Since the entire high-temperature furnace chamber can be brought into a substantially uniform high-temperature state, the processing gas can be processed satisfactorily.

実施例1 直径(内径)200m+、高さ320mの高温炉室の上
部炉壁の内周部に巾90簡のステンレススチーμ板をは
りつけ、且つ上部に高さ350−のラッパ状マイクロ波
照射口部を設けた、第1図に示す構造のパイロット試験
炉を用い、マイクロ波発生装置からのマイクロ波出力を
3 kWとしマイクロ波を照射して炉芹部を約900℃
に加熱した後、Co I)M)某2000 ppm以上
で過剰空気率2.0の被処理ガスをo、s7m/秒の速
度で通じたところ、燃焼ガス出口部における排出ガスの
Co含有量は50 ppm以下となった。
Example 1 A stainless steel μ plate with a width of 90 strips is attached to the inner periphery of the upper furnace wall of a high temperature furnace chamber with a diameter (inner diameter) of 200 m + and a height of 320 m, and a trumpet-shaped microwave irradiation port with a height of 350 m is attached at the top. Using a pilot test furnace with the structure shown in Figure 1, the microwave output from the microwave generator was set to 3 kW, and microwaves were irradiated to heat the core of the furnace to approximately 900°C.
After heating it to It became 50 ppm or less.

該焼却炉においては、・、−入射マイクロ波の95チ以
上を高温炉室へ供給できたが、第3図に示す炉において
は、炉入射マイクロ波の80%程度しか高温炉室へ供給
できず、しかも高温炉室の上部が加熱されるため、上記
と同じ燃焼効率を得るためには、マイクロ波発生装置の
マイク口波出力を約5 kWとする必要があった。
In this incinerator, 95 or more of the incident microwaves could be supplied to the high-temperature furnace chamber, but in the furnace shown in Figure 3, only about 80% of the incident microwaves could be supplied to the high-temperature furnace chamber. Moreover, since the upper part of the high-temperature furnace chamber is heated, in order to obtain the same combustion efficiency as above, it was necessary to set the microphone mouth wave output of the microwave generator to about 5 kW.

なお、第2図に示す如き焼却炉において高温炉室の炉壁
に金属板をはりつけ、且つ上部にラッパ状マイクロ波照
射口部を設けた場合にも同様の結果が得られる。
Similar results can be obtained when a metal plate is attached to the wall of the high-temperature furnace chamber in an incinerator as shown in FIG. 2, and a trumpet-shaped microwave irradiation port is provided at the top.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、マイクロ波を効率良く焼却炉に供給す
ることが可能である。
According to the present invention, it is possible to efficiently supply microwaves to an incinerator.

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

第1図は本発明の一実施例を説明するだめの焼却炉の断
面概略図、第2図及び第3図は従来の焼却炉の断面概略
図を示す。 1.11・・・被処理排ガス入口部、2.12・・・処
理された排ガス出口管、3,13・・・マイクロ波導入
管、4,14・・・断熱材、5・・・充填層、6・・・
高温炉室、8,16・・・炉底板、15・・・炉壁、1
8・・・高温炉室、20−・・ラッパ状形状のマイクロ
波照射口、21・・・金属板 第1図 第2図 ■ 第3図
FIG. 1 is a schematic cross-sectional view of a secondary incinerator illustrating an embodiment of the present invention, and FIGS. 2 and 3 are schematic cross-sectional views of a conventional incinerator. 1.11... Inlet of exhaust gas to be treated, 2.12... Outlet pipe of treated exhaust gas, 3, 13... Microwave introduction pipe, 4, 14... Insulating material, 5... Filling Layer, 6...
High temperature furnace chamber, 8, 16... Furnace bottom plate, 15... Furnace wall, 1
8...High temperature furnace chamber, 20-...Trumpet-shaped microwave irradiation port, 21...Metal plate Fig. 1 Fig. 2■ Fig. 3

Claims (1)

【特許請求の範囲】 1、炉中のマイクロ波を吸収する性質を有する材料にマ
イクロ波を照射することにより高温に保持されている炉
に、可燃性ガス或いは有害成分含有排ガスを通し、可燃
性成分或いは有害成分を酸化燃焼或いは分解せしめる炉
において、炉頂部にあるマイクロ波照射口部をラツパ状
形状としたことを特徴とするマイクロ波による可燃性排
ガス焼却炉。 2、炉内のマイクロ波吸収材上部の炉材表面を金属板で
被覆した特許請求の範囲第1項記載の焼却炉。
[Claims] 1. Combustible gas or exhaust gas containing harmful components is passed through a furnace that is maintained at a high temperature by irradiating microwaves to a material that absorbs microwaves in the furnace. A microwave combustible exhaust gas incinerator for oxidative combustion or decomposition of components or harmful components, characterized in that a microwave irradiation port at the top of the furnace is shaped like a flap. 2. The incinerator according to claim 1, wherein the surface of the furnace material above the microwave absorbing material in the furnace is covered with a metal plate.
JP29219885A 1985-12-26 1985-12-26 Structure of combustible discharged gas incinerator device using microwave Pending JPS62153620A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29219885A JPS62153620A (en) 1985-12-26 1985-12-26 Structure of combustible discharged gas incinerator device using microwave

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29219885A JPS62153620A (en) 1985-12-26 1985-12-26 Structure of combustible discharged gas incinerator device using microwave

Publications (1)

Publication Number Publication Date
JPS62153620A true JPS62153620A (en) 1987-07-08

Family

ID=17778799

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29219885A Pending JPS62153620A (en) 1985-12-26 1985-12-26 Structure of combustible discharged gas incinerator device using microwave

Country Status (1)

Country Link
JP (1) JPS62153620A (en)

Cited By (2)

* 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
US6891140B2 (en) 2000-10-19 2005-05-10 Gifu Prefecture Sintering furnace, method of manufacturing sintered objects, and sintered objects

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4867204A (en) * 1971-12-17 1973-09-13
JPS5416745A (en) * 1977-07-07 1979-02-07 Mitsubishi Electric Corp Microwave irradiation device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4867204A (en) * 1971-12-17 1973-09-13
JPS5416745A (en) * 1977-07-07 1979-02-07 Mitsubishi Electric Corp Microwave irradiation device

Cited By (2)

* 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
US6891140B2 (en) 2000-10-19 2005-05-10 Gifu Prefecture Sintering furnace, method of manufacturing sintered objects, and sintered objects

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