JPH0441319B2 - - Google Patents

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Publication number
JPH0441319B2
JPH0441319B2 JP58129983A JP12998383A JPH0441319B2 JP H0441319 B2 JPH0441319 B2 JP H0441319B2 JP 58129983 A JP58129983 A JP 58129983A JP 12998383 A JP12998383 A JP 12998383A JP H0441319 B2 JPH0441319 B2 JP H0441319B2
Authority
JP
Japan
Prior art keywords
powder
cylindrical container
partition wall
melting processing
pipe
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
Application number
JP58129983A
Other languages
Japanese (ja)
Other versions
JPS6021500A (en
Inventor
Yasuaki Kataoka
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP58129983A priority Critical patent/JPS6021500A/en
Publication of JPS6021500A publication Critical patent/JPS6021500A/en
Publication of JPH0441319B2 publication Critical patent/JPH0441319B2/ja
Granted legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Furnace Details (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】 本発明は、マイクロ波を用いて粉状体を溶融し
固化する粉状体溶融処理装置に関し、更に詳しく
は、汚染性の焼却灰等の粉状体を安全に溶融処理
できる粉状体溶融処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a powder melting device that uses microwaves to melt and solidify powder, and more specifically, to a powder melting device that uses microwaves to melt and solidify powder. The present invention relates to a powder melting processing device that can process powdered materials.

マイクロ波の用いる粉状体の溶融処理方法は、
加熱が粉状体を構成する物質自体の分子運動に基
づく誘電損失によつて行われるため、処理粉状体
を内部から均一に且つ効率よく加熱溶融すること
ができるので従来の電熱加熱や輻射加熱による方
法に比較して原理的に格段に優れている。このた
め、多くの産業分野において様々な目的に利用さ
れているが、特に最近これを産業廃棄物処理に応
用し、各種産業施設や原子力施設から排出される
廃棄物をマイクロ波照射により加熱溶融し、廃棄
物中に含まれる二酸化珪素によりガラス化し固化
する方法が注目されつつある。
The method for melting powder using microwaves is
Because heating is performed by dielectric loss based on the molecular motion of the substance that makes up the powder, the treated powder can be heated and melted from the inside evenly and efficiently, making it easier to heat and melt the powder than conventional electric heating or radiation heating. In principle, this method is much superior to that of the previous method. For this reason, it is used for various purposes in many industrial fields, but recently it has been applied to industrial waste treatment, where waste discharged from various industrial facilities and nuclear facilities is heated and melted by microwave irradiation. , a method of vitrifying and solidifying waste using silicon dioxide contained in waste is attracting attention.

このための溶融処理装置として各種のものが考
えられている。例えば、その一つとして、マイク
ロ波空胴共振器を構成する円筒容器から成る粉状
体溶融部を備えた粉状体溶融処理装置が知られて
いる。
Various types of melt processing equipment have been considered for this purpose. For example, as one such apparatus, a powder melting processing apparatus is known which includes a powder melting section consisting of a cylindrical container constituting a microwave cavity resonator.

この種の粉状体溶融処理装置における主要部の
概略構成は第1図で示すことができる。即ち、マ
イクロ波空洞共振器を形成する円筒容器1は、フ
ランジ重合部2にて結合又は分離される導電率の
高い金属製円筒3及び4から成り、該円筒容器1
の上部には、発振器6から出るマイクロ波を円筒
容器1内に導くマイクロ波導波管7と、共振時の
マツチングをとるマツチング機構8と、粉状体9
を導入する粉状体導入管10とが連結されてい
る。そして、発振器6からマイクロ波を照射した
とき、円筒容器1の内部が最も強い電界を生ずる
モードで共振するようになつている。
A schematic configuration of the main parts of this type of powder melting processing apparatus can be shown in FIG. That is, a cylindrical container 1 forming a microwave cavity resonator is composed of metal cylinders 3 and 4 with high conductivity that are joined or separated at a flange overlapping portion 2, and the cylindrical container 1
A microwave waveguide 7 that guides the microwave emitted from the oscillator 6 into the cylindrical container 1, a matching mechanism 8 that performs matching during resonance, and a powder material 9 are disposed on the top of the oscillator 6.
It is connected to a powder introduction pipe 10 that introduces powder. When microwaves are irradiated from the oscillator 6, the interior of the cylindrical container 1 resonates in a mode that produces the strongest electric field.

この粉状体溶融処理装置において、円筒容器1
に所定量の粉状体9を導入した後、粉状体9への
マイクロ波の照射を開始すると、粉状体9は加熱
溶融し、その後放冷状態におくと、粉状体9に含
まれる成分例えば二酸化珪素(粉状体9が原子力
施設からの廃棄物の場合)によつて、粉状体9は
ガラス化又は岩石化して固化する。この固化した
粉状体9は、円筒4と共に金属製円筒3から分離
され、廃棄処理されることになる。
In this powder melting processing apparatus, a cylindrical container 1
After introducing a predetermined amount of the powder 9 into the powder 9, when microwave irradiation to the powder 9 is started, the powder 9 is heated and melted, and when it is left to cool, the particles contained in the powder 9 are melted. Depending on the components contained in the powder, such as silicon dioxide (if the powder 9 is waste from a nuclear facility), the powder 9 becomes vitrified or petrified and solidifies. This solidified powder 9 is separated from the metal cylinder 3 together with the cylinder 4, and is disposed of.

この装置は一時に多量の粉状体の処理が可能で
ある等の点で、実用上、廃棄物処理用装置として
は最も優れていると考えらえる。しかし、原子力
発電所、核燃料処理工場、ラジオアイソトープを
使用する施設等における廃棄物を焼却して得た放
射性焼却灰等の放射性の粉状体を、上記溶融処理
装置で溶融処理しようとすると、次の如き大きな
問題が生じる。
This device is considered to be the most excellent waste treatment device in terms of its ability to process a large amount of powder at one time. However, when trying to melt radioactive powder such as radioactive incineration ash obtained by incinerating waste at nuclear power plants, nuclear fuel processing plants, facilities that use radioisotopes, etc. using the above melting processing equipment, the following occurs. A big problem arises.

まず、従来の粉状体溶融処理装置では、粉状体
9を円筒容器1内に導入した後、マイクロ波を照
射すると、マイクロ波照射中に発生する副生ガス
によつて円筒容器1が加圧状態となり、粉状体9
が円筒3と4のフランジ部2やマイクロ波導入管
7及び粉状体導入管10の接続部から飛散したり
吹き出したりして周囲を汚染することがある。こ
のような粉状体9が外部に出ることは、粉状体9
が原子力施設からの廃棄物である場合、非常に危
険であり安全性の面から大きな問題となる。
First, in the conventional powder melting processing apparatus, when the powder 9 is introduced into the cylindrical container 1 and then irradiated with microwaves, the cylindrical container 1 is heated by the by-product gas generated during the microwave irradiation. It becomes a pressure state and the powder 9
may be scattered or blown out from the flange portions 2 of the cylinders 3 and 4 or the connecting portions of the microwave introduction tube 7 and the powder introduction tube 10, contaminating the surrounding area. The fact that such powdery material 9 comes out is that the powdery material 9
If it is waste from a nuclear facility, it is extremely dangerous and poses a major safety problem.

又、放射性粉状体(焼却灰)の場合はその粒径
が小さく容易に浮遊乃至飛散する。従つて、かか
る危険な放射性粉状体を焼却場から溶融処理装置
まで、周囲に灰を飛散させずに輸送することもか
なり困難なことである。
Furthermore, in the case of radioactive powder (incineration ash), its particle size is small and it easily floats or scatters. Therefore, it is quite difficult to transport such dangerous radioactive powder from the incinerator to the melting processing equipment without scattering ash into the surrounding area.

本発明は、このような点に鑑みてなされたもの
で、その目的は、粉状体のマイクロ波照射中にお
ける粉状体の溶融処理装置外への飛散や吹き出し
をなくし、より安全性を高めた粉状体溶融処理装
置を提供することにある。
The present invention has been made in view of these points, and its purpose is to eliminate the scattering and blowing out of the powder material outside the melting processing equipment during microwave irradiation of the powder material, and to further improve safety. An object of the present invention is to provide a powder melting processing apparatus.

この目的を達成する本発明は、マイクロ波空胴
共振器として円筒容器を用いる粉状体溶融処理装
置において、前記円筒容器の周壁に粉状体導入管
を接線方向に接続し、頂部には一端が排気装置に
接続された排気管を貫設すると共に、前記円筒容
器の中部に略漏斗状の隔壁を配設し、前記円筒容
器内を負圧状態にすることにより、粉状体を粉状
体貯留部から前記円筒容器内に旋回気流として導
入し、前記円筒容器の周壁及び前記隔壁上面に沿
つて沈降させ、沈積した粉状体に負圧下でマイク
ロ波を照射して溶融処理するように構成したこと
を特徴とするものである。
The present invention achieves this object in a powder melting processing apparatus using a cylindrical container as a microwave cavity resonator, in which a powder introduction pipe is tangentially connected to the peripheral wall of the cylindrical container, and one end is connected to the top of the cylindrical container. An exhaust pipe connected to an exhaust device is installed through the cylindrical container, and a substantially funnel-shaped partition wall is provided in the middle of the cylindrical container to create a negative pressure state inside the cylindrical container. The powder is introduced as a swirling airflow into the cylindrical container from the body storage part, and is allowed to settle along the peripheral wall of the cylindrical container and the upper surface of the partition wall, and the deposited powder is irradiated with microwaves under negative pressure to melt it. It is characterized by the following structure.

以下、図面を参照し本発明の実施例を詳細に説
明する。
Embodiments of the present invention will be described in detail below with reference to the drawings.

第2図及び第3図(第2図A−A断面図)は、
本発明の一実施例を示す説明図で、第1図と同
様、円筒容器1は、円筒3,4をフランジ重合部
2で着脱可能に結合することにより構成される。
又、円筒容器1の上部には、第1図と同様、発振
器6からのマイクロ波を導入するマイクロ波導波
管7が連結されている。
Figures 2 and 3 (sectional view taken along line A-A in Figure 2) are
This is an explanatory diagram showing one embodiment of the present invention. Similar to FIG. 1, a cylindrical container 1 is constructed by removably connecting cylinders 3 and 4 at a flange overlapping portion 2. FIG.
Further, a microwave waveguide 7 for introducing microwaves from an oscillator 6 is connected to the upper part of the cylindrical container 1, as in FIG. 1.

一方、粉状体導入管10の一端は、円筒容器1
の上部の周壁に接線方向に接続され、他端は粉状
体貯留部11内に配置されている。更に、円筒容
器1の中部には、略漏斗状の隔壁12が配設さ
れ、この下部にマツチング機構8が取り付けられ
ている。又、円筒容器1の頂部を貫通して排気管
13が設置され、該排気管13の他端側は、ター
ボフアン、ブレードフアン等の排気装置14に接
続されている。この排気装置14の排気口は、管
路15を介して集塵器16に接続され、該集塵器
16でもつて排気に同伴した少量の粉状体を完全
に補集し、管路17を介して粉状体貯留部11に
戻す構成となつている。
On the other hand, one end of the powder introduction pipe 10 is connected to the cylindrical container 1
is tangentially connected to the upper peripheral wall of the powder storage section 11, and the other end thereof is disposed within the powder storage section 11. Further, a substantially funnel-shaped partition wall 12 is provided in the middle of the cylindrical container 1, and a matching mechanism 8 is attached to the lower part of the partition wall 12. Further, an exhaust pipe 13 is installed passing through the top of the cylindrical container 1, and the other end side of the exhaust pipe 13 is connected to an exhaust device 14 such as a turbo fan or a blade fan. The exhaust port of this exhaust device 14 is connected to a dust collector 16 via a pipe 15, and the dust collector 16 completely collects a small amount of powder accompanying the exhaust air. The powder is returned to the powder storage section 11 via the powder storage section 11.

次に、上記構成の粉状体溶融処理装置の作動に
ついて説明する。
Next, the operation of the powder melting processing apparatus having the above configuration will be explained.

この処理装置において、排気装置14を始動す
ると、排気管13、円筒容器1、粉状体導入管1
0等で構成される系内は負圧状態となり、粉状体
導入管10を介して粉状体貯留部11内の粉状体
9が円筒容器1内に吸引される。粉状体導入管1
0の一端が円筒容器1の周壁に接線方向で接続さ
れているため、円筒容器1に吸引導入される粉状
体9は、旋回気流となつて内部を流れ、且つ遠心
力の作用を受けて円筒容器1の上部周壁及び漏斗
状隔壁12の上面に沿つて下降(沈降)し、漏斗
状隔壁12の開口部を介して円筒容器1の下部に
落下する。円筒容器1に所定量の粉状体9が沈積
した状態において、排気装置14を稼働のまま、
マイクロ波導波管7からマイクロ波を導入し、マ
ツチング機構8と共に共振させると、円筒容器1
の内部に強い電界が生じる。この電界によつて円
筒容器1内の粉状体9は加熱され溶融する。この
とき、副生ガスが発生する等の外乱のためダステ
イングが生じ、粉状体9の一部が漏斗状隔壁12
の上側に戻つたとしても、旋回気流に捕捉され、
遠心力の作用により再び円筒容器1の周壁及び隔
壁12の上面に沿つて沈降し円筒容器1の下部に
落下することになる。
In this processing device, when the exhaust device 14 is started, the exhaust pipe 13, the cylindrical container 1, the powder introduction pipe 1
The inside of the system composed of 0, etc. becomes a negative pressure state, and the powder 9 in the powder storage section 11 is sucked into the cylindrical container 1 through the powder introduction pipe 10. Powder introduction pipe 1
Since one end of the powder 9 is connected to the peripheral wall of the cylindrical container 1 in a tangential direction, the powder 9 sucked into the cylindrical container 1 flows inside as a swirling air current and is subjected to the action of centrifugal force. It descends (sinks) along the upper peripheral wall of the cylindrical container 1 and the upper surface of the funnel-shaped partition wall 12, and falls to the lower part of the cylindrical container 1 through the opening of the funnel-shaped partition wall 12. With the predetermined amount of powder 9 deposited in the cylindrical container 1, the exhaust device 14 is left in operation,
When microwaves are introduced from the microwave waveguide 7 and resonated together with the matching mechanism 8, the cylindrical container 1
A strong electric field is generated inside the The powder 9 in the cylindrical container 1 is heated and melted by this electric field. At this time, dusting occurs due to disturbances such as generation of by-product gas, and a part of the powder 9 is transferred to the funnel-shaped partition wall 12.
Even if it returns to the upper side, it will be caught in the swirling air current,
Due to the action of the centrifugal force, it sinks again along the peripheral wall of the cylindrical container 1 and the upper surface of the partition wall 12 and falls to the lower part of the cylindrical container 1.

予め定めた時間、円筒容器1内の粉状体9にマ
イクロ波を照射した後、放冷状態におくと、円筒
容器1内の粉状体9(溶融物)はガラス状又は岩
石状となつて固化する。固化した粉状体9は、円
筒3から分離される円筒4と共に廃棄又は保管処
理される。
When the powder 9 in the cylindrical container 1 is irradiated with microwaves for a predetermined time and then left to cool, the powder 9 (molten material) in the cylindrical container 1 becomes glass-like or rock-like. and solidify. The solidified powder 9 is disposed of or stored together with the cylinder 4 that is separated from the cylinder 3.

尚、排気管13を介して廃棄される気流の中に
は、ほとんど粉状体9は含まれていないが、たと
え含まれていたとしても集塵器16で捕集され、
再び粉状体貯留部11に戻され、上記の処理工程
に再度かけられる。又、粉状体導入管10により
粉状体9を吸入する過程において、粉状体9中に
含まれる大形金属片等の好ましからざる重量物は
選択的に排除される効果も期待できる。この場
合、残つた大形金属片等は他の処理方法で処理さ
れることになる。
It should be noted that the airflow discarded through the exhaust pipe 13 hardly contains any powder 9, but even if it does, it will be collected by the dust collector 16.
The powder is returned to the powder storage section 11 and subjected to the above-mentioned processing steps again. Further, in the process of sucking the powder 9 through the powder introduction pipe 10, it can be expected that undesirable heavy objects such as large metal pieces contained in the powder 9 will be selectively removed. In this case, the remaining large metal pieces etc. will be treated by another treatment method.

第4図及び第5図はそれぞれ本発明の他の実施
例の概略説明図で、第2図と同一部分には同一符
号を用い、その説明は省略する。これらの実施例
の特徴は、円筒3を異なる直径の円筒3a,3b
から構成し、円筒3aの下部に隔壁12を固着
し、該隔壁12を円筒3bの上部に固着した点に
ある。このような構成によれば、円筒3の内周面
への隔壁12の取付作業が容易になる。
4 and 5 are schematic explanatory diagrams of other embodiments of the present invention, and the same parts as in FIG. 2 are denoted by the same reference numerals, and the explanation thereof will be omitted. The feature of these embodiments is that the cylinder 3 is made of cylinders 3a and 3b having different diameters.
A partition wall 12 is fixed to the lower part of the cylinder 3a, and the partition wall 12 is fixed to the upper part of the cylinder 3b. According to such a configuration, the work of attaching the partition wall 12 to the inner circumferential surface of the cylinder 3 becomes easy.

尚、上記各実施例において、排気装置14とし
て(第4図及び第5図にあつてはこれらは省略さ
れている)、ターボフアン、ブレードフアン等を
用いているが、本発明はこれに限定するものでは
なく、多翼フアン、プロペラフアン等のフアン
(通風機)、ターボブロワー、ルーツブロワー等の
ブロワー(送風機)、水エジエクタ、スチームエ
ジエクタ等のエジエクタであつてもよい。又、本
発明は、集塵器16を備えることを要件とするも
のではなく、排気管13を介して得られる排気ガ
スを直接大気中或いは廃棄物を焼却する焼却炉内
に吹き出すようにしてもよい。更に、溶融処理後
の粉状体9を排出するため、円筒容器1の底部に
排出用弁を設けてもよい。
In each of the above embodiments, a turbo fan, a blade fan, etc. are used as the exhaust device 14 (these are omitted in FIGS. 4 and 5), but the present invention is not limited to this. Instead, it may be a fan such as a multi-blade fan or a propeller fan, a blower such as a turbo blower or a roots blower, or an ejector such as a water ejector or a steam ejector. Further, the present invention does not require the provision of the dust collector 16, and the exhaust gas obtained through the exhaust pipe 13 may be blown directly into the atmosphere or into an incinerator for incinerating waste. good. Further, a discharge valve may be provided at the bottom of the cylindrical container 1 in order to discharge the powder 9 after the melting process.

以上詳しく説明したように、本発明の粉状体溶
融処理装置は、漏斗状隔壁が配設された円筒容器
の内部を負圧状態にすることにより、粉状体を旋
回気流として吸引導入し、該円筒容器の周壁及び
漏斗状隔壁の上面に沿つて沈降捕集し、円筒容器
の下部に落下させる構成となつている。このた
め、粉状体を外部に飛散することなく粉状体貯留
部から移送できることは勿論のこと、マイクロ波
を照射中に副生ガスが発生し、ダステイングによ
つて粉状体の一部が漏斗状隔壁の上方に戻つて
も、旋回気流に捕捉され再び円筒容器の下部に戻
り、外部に飛散することはない。従つて、周囲を
汚染することもなく、極めて安全性が高いと言え
る。
As explained in detail above, the powder melting processing apparatus of the present invention suctions and introduces the powder as a swirling airflow by creating a negative pressure inside the cylindrical container in which the funnel-shaped partition wall is provided. The liquid is collected by sedimentation along the peripheral wall of the cylindrical container and the upper surface of the funnel-shaped partition wall, and is allowed to fall to the lower part of the cylindrical container. For this reason, it is possible to transfer the powder from the powder storage section without scattering the powder to the outside, but also by-product gas is generated during microwave irradiation, and part of the powder is removed by dusting. Even if it returns above the funnel-shaped partition, it is captured by the swirling airflow and returns to the lower part of the cylindrical container, and is not scattered to the outside. Therefore, it can be said to be extremely safe without contaminating the surrounding area.

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

第1図は公知の粉状体溶融処理装置の概念説明
図、第2図は本発明の一実施例を示す説明図、第
3図は第2図のA−A断面図、第4図及び第5図
はそれぞれ本発明の他の実施例の概略を示す説明
図である。 1……円筒容器、2……フランジ部、3,4…
…円筒、6……発振器、7……マイクロ波導波
管、8……マツチング機構、9……粉状体、10
……粉状体導入管、11……粉状体貯留部、12
……漏斗状隔壁、13……排気管、14……排気
装置、16……集塵器。
Fig. 1 is a conceptual explanatory diagram of a known powder melting processing apparatus, Fig. 2 is an explanatory diagram showing an embodiment of the present invention, Fig. 3 is a sectional view taken along line AA in Fig. 2, Fig. 4, and FIG. 5 is an explanatory diagram showing the outline of other embodiments of the present invention. 1... Cylindrical container, 2... Flange portion, 3, 4...
... Cylinder, 6 ... Oscillator, 7 ... Microwave waveguide, 8 ... Matching mechanism, 9 ... Powder, 10
... Powder introduction pipe, 11 ... Powder storage section, 12
... Funnel-shaped bulkhead, 13 ... Exhaust pipe, 14 ... Exhaust device, 16 ... Dust collector.

Claims (1)

【特許請求の範囲】[Claims] 1 マイクロ波空胴共振器として円筒容器を用い
る粉状体溶融処理装置において、前記円筒容器の
周壁に粉状体導入管を接線方向に接続し、頂部に
は一端が排気装置に接続された排気管を貫設する
と共に、前記円筒容器の中部に略漏斗状の隔壁を
配設し、前記円筒容器内を負圧状態にすることに
より、粉状体を粉状体貯留部から前記円筒容器内
に施回気流として導入し、前記円筒容器の周壁及
び前記隔壁上面に沿つて沈降させ、沈積した粉状
体に負圧下でマイクロ波を照射して溶融処理する
ように構成したことを特徴とする粉状体溶融処理
装置。
1. In a powder melting processing apparatus using a cylindrical container as a microwave cavity resonator, a powder introduction pipe is tangentially connected to the peripheral wall of the cylindrical container, and an exhaust pipe is connected to the top with one end connected to an exhaust device. A pipe is inserted through the cylindrical container, and a substantially funnel-shaped partition is provided in the middle of the cylindrical container to create a negative pressure inside the cylindrical container, thereby transferring the powder from the powder storage section into the cylindrical container. The powder is introduced as an airflow into the cylindrical container, is allowed to settle along the peripheral wall of the cylindrical container and the upper surface of the partition wall, and is melted by irradiating the deposited powder with microwaves under negative pressure. Powder melting processing equipment.
JP58129983A 1983-07-15 1983-07-15 Device for melting and treating granular body Granted JPS6021500A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58129983A JPS6021500A (en) 1983-07-15 1983-07-15 Device for melting and treating granular body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58129983A JPS6021500A (en) 1983-07-15 1983-07-15 Device for melting and treating granular body

Publications (2)

Publication Number Publication Date
JPS6021500A JPS6021500A (en) 1985-02-02
JPH0441319B2 true JPH0441319B2 (en) 1992-07-07

Family

ID=15023257

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58129983A Granted JPS6021500A (en) 1983-07-15 1983-07-15 Device for melting and treating granular body

Country Status (1)

Country Link
JP (1) JPS6021500A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0642000B2 (en) * 1985-12-12 1994-06-01 三機工業株式会社 Equipment for supplying radioactive waste in the furnace
US5041798A (en) * 1990-06-12 1991-08-20 International Business Machines Corporation Time reference with proportional steering
JPH0570797A (en) * 1991-09-17 1993-03-23 Tama Kagaku Kogyo Kk Detergent composition

Also Published As

Publication number Publication date
JPS6021500A (en) 1985-02-02

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