JPH0441318B2 - - Google Patents
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- Publication number
- JPH0441318B2 JPH0441318B2 JP58129982A JP12998283A JPH0441318B2 JP H0441318 B2 JPH0441318 B2 JP H0441318B2 JP 58129982 A JP58129982 A JP 58129982A JP 12998283 A JP12998283 A JP 12998283A JP H0441318 B2 JPH0441318 B2 JP H0441318B2
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- Prior art keywords
- powder
- cylindrical
- section
- melting
- container
- Prior art date
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- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Vertical, Hearth, Or Arc Furnaces (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.
マイクロ波を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 as follows:
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粉状溶融
部の概略構成は第1図で示すことができる。即
ち、粉状体溶融部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から成る円筒容器5の上部に、発振器6から出
るマイクロ波を円筒容器5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
とを連結することにより構成され、マイクロ波を
導入したとき、円筒容器5の内部が最も強い電界
を生ずるモードで共振するマイクロ波空胴共振器
を形成するようになつている。 The schematic structure of the powder melting section in this type of powder melting processing apparatus can be shown in FIG. That is, the powder melting section 1 transmits microwaves emitted from an oscillator 6 to the upper part of the cylindrical container 5, which is made up of metal cylinders 3 and 4 with high conductivity, which are joined or separated at the flange polymerization section 2. A microwave waveguide 7 that guides the inside, a matching mechanism 8 that performs matching during resonance, and a powder introduction pipe 10 that introduces the powder 9.
When microwaves are introduced, a microwave cavity resonator is formed which resonates in a mode that produces the strongest electric field inside the cylindrical container 5.
この粉状体溶融処理装置において、円筒容器5
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, the cylindrical container 5
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れる。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5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5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 5 and then irradiated with microwaves, the cylindrical container 5 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において、円筒形胴
部及び漏斗形底部から成り該漏斗形底部が前記粉
状体溶融部と連通する円筒円錐形容器を設け、該
円筒円錐形容器の円筒形胴部の周壁に、粉状体導
入管を接続方向に接続すると共に、該円筒円錐形
容器の円筒形胴部の頂部に、一端が排気装置に接
続された排気管を貫設することにより粉状体捕集
部を形成し、該粉状体捕集部を負圧状態にして粉
状体貯留部から粉状体を前記粉状体捕集部に旋回
気流として導入し、該粉状体捕集部の容器の周壁
に沿つて沈降させ前記粉状体溶融部に落下させる
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 equipped with a powder melting section consisting of a cylindrical container constituting a microwave cavity resonator. A cylindrical-conical container is provided, the bottom of which communicates with the powder melting section, a powder introduction pipe is connected to the peripheral wall of the cylindrical body of the cylindrical-conical container in the connecting direction, and the cylindrical-conical container A powder collection section is formed by penetrating the top of the cylindrical body of the vessel with an exhaust pipe connected to an exhaust device at one end, and the powder collection section is brought into a negative pressure state to remove the powder. The powder is introduced from the powder storage section into the powder collection section as a swirling airflow, and is caused to settle along the peripheral wall of the container of the powder collection section and fall into the powder melting section. 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図の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、1は粉状体溶融部であり、円筒3,4をフ
ランジ重合部2で着脱可能に結合した円筒容器5
と、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と、マツチング機構9とで構成され
ている。11は粉状体捕集部であり、管路14を
介して粉状体溶融部1と連通する円筒円錐形容器
15と、一端が円筒円錐形容器15の円筒形胴部
12の周壁に接線方向に接続され、他端が粉状体
貯留部18に配置される粉状体導入管19と、一
端側が円筒円錐容器15の円筒形胴部12の頂部
を貫通して設置され、他端側がターボフアン、ブ
レードフアン等の排気装置22に接続される排気
管23とで構成されている。粉状体捕集部11の
排気側、即ち、排気装置22の排気口は、管路2
0を介して集塵器24に接続され、該集塵器24
でもつて排気に同伴した少量の粉状体を完全に捕
集し、管路25を介して粉状体貯留部18に戻す
構成となつている。 Figures 2 and 3 (A-A sectional view in Figure 2)
1 is an explanatory diagram showing an embodiment of the present invention, in which, like FIG. 1, 1 is a powder melting section, and a cylindrical container 5 in which cylinders 3 and 4 are removably connected at a flange overlapping section 2.
, a microwave waveguide 7 that introduces the microwave from the oscillator 6, and a matching mechanism 9. Reference numeral 11 denotes a powder collecting section, which includes a cylindrical-conical container 15 that communicates with the powder melting section 1 via a conduit 14, and one end of which is tangential to the peripheral wall of the cylindrical body 12 of the cylindrical-conical container 15. A powder introduction pipe 19 is connected to the powder material introduction pipe 19 whose other end is arranged in the powder storage section 18, and whose one end is installed passing through the top of the cylindrical body 12 of the cylindrical-conical container 15, and whose other end is arranged in the powder storage section 18. The exhaust pipe 23 is connected to an exhaust device 22 such as a turbo fan or a blade fan. The exhaust side of the powder collecting section 11, that is, the exhaust port of the exhaust device 22 is connected to the pipe line 2.
0 to the dust collector 24, and the dust collector 24
Thus, a small amount of powder accompanying the exhaust gas is completely collected and returned to the powder storage section 18 via the pipe 25.
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、粉状体捕集部11の排
気装置22を始動すると、排気管23、円筒円錐
形容器15、粉状体導入管19等で構成される系
内は負圧状態となり、粉状体導入管19を介して
粉状体貯留部18の粉状体9が円筒円錐形容器1
5内に吸引される。粉状体導入管19の一端が円
筒形胴部12の周壁に接線方向で接続されている
ため、円筒形胴部12に吸引導入される粉状体9
は、旋回気流となつて円筒形胴部12を流れ、遠
心力の作用を受けて円筒形胴部12の周壁に沿つ
て下降(沈降)し、漏斗形底部13、管路14を
介して粉状体溶融部1の円筒容器5に落下する。
粉状体溶融部1の円筒容器5に所定量の粉状体9
が沈積した状態において、排気装置22を稼動の
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5の内部に強い電界が生じる。この電界によ
つて円筒容器5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の一部が粉状体
捕集部11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円錐形容器15
の周壁に沿つて沈降し円筒容器5に落下すること
になる。予め定めた時間、円筒容器5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5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。 In this processing apparatus, when the exhaust device 22 of the powder collection section 11 is started, the inside of the system consisting of the exhaust pipe 23, the cylindrical-conical container 15, the powder introduction pipe 19, etc. becomes a negative pressure state, and the powder The powder 9 in the powder storage section 18 is transferred to the cylindrical-conical container 1 through the powder introduction pipe 19.
5. Since one end of the powder introduction pipe 19 is tangentially connected to the peripheral wall of the cylindrical body 12, the powder 9 is sucked and introduced into the cylindrical body 12.
The powder flows through the cylindrical body 12 as a swirling air current, descends (settles) along the circumferential wall of the cylindrical body 12 under the action of centrifugal force, and passes through the funnel-shaped bottom 13 and the pipe 14 to become powder. The shaped body falls into the cylindrical container 5 of the melting section 1.
A predetermined amount of powder 9 is placed in the cylindrical container 5 of the powder melting section 1.
When microwaves are introduced from the microwave waveguide 7 and resonated together with the matching mechanism 8 while the exhaust device 22 is kept in operation in a state where the gas is deposited, a strong electric field is generated inside the cylindrical container 5. The powder 9 in the cylindrical container 5 is heated and melted by this electric field. At this time, dusting occurs due to disturbances such as generation of by-product gas, and even if some of the powder 9 returns to the powder collecting section 11, it will be captured by the swirling airflow and due to the action of centrifugal force. Cylindrical-conical container 15 again
The liquid sinks along the peripheral wall of the cylinder and falls into the cylindrical container 5. When the powder 9 in the cylindrical container 5 is irradiated with microwaves for a predetermined time and then left to cool, the powder 9 (molten material) in the cylindrical container 5 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、粉状体捕集部11の排気管23を介して排
気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24で捕集され、再び粉状体貯留部18に戻さ
れ、上記の処理工程に再度かけられる。 It should be noted that the airflow exhausted through the exhaust pipe 23 of the powder collecting section 11 hardly contains any powder 9, but even if it does, it will be collected by the dust collector 24. The powder is collected, returned to the powder storage section 18, and subjected to the above-mentioned processing steps again.
第4図は本発明の他の実施例の説明図で、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。この実施例の特徴は、粉状体捕集部11
と粉状体溶融部1とを連通する管路14に弁26
を設けた点にある。弁26は円筒容器5内の粉状
体9にマイクロ波を照射中は閉成されるようにな
つている。このため、粉状体9にマイクロ波照射
中に副生ガスによるダステイングが生じても粉状
体は粉状体捕集部11に戻ることはない。 FIG. 4 is an explanatory diagram of another embodiment of the present invention.
The same reference numerals are used for the same parts as those in the figures, and the explanation thereof will be omitted. The feature of this embodiment is that the powder collecting section 11
A valve 26 is provided in the pipe line 14 that communicates the powder melting section 1 with the
The point is that it has been established. The valve 26 is closed while the powder 9 in the cylindrical container 5 is being irradiated with microwaves. Therefore, even if the powder 9 is dusted by by-product gas during microwave irradiation, the powder does not return to the powder collecting section 11.
第5図及び第6図(第5図のB−B断面図)は
本発明の更に他の実施例の説明図で、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。この実施例の特徴は、粉状体捕集部11を構
成する円筒円錐形容器15と粉状体溶融部1を構
成する円筒容器5とを一体化し、それぞれの容器
を連通する管路(第2図における管路14)を省
略した点にある。このような構成によれば、粉状
体溶融部1と粉状体捕集部11が一体となつてい
るため、コンパクトな粉状体溶融処理装置を実現
することができる。 5 and 6 (BB sectional view of FIG. 5) are explanatory diagrams of still another embodiment of the present invention, and the same parts as in FIG. . The feature of this embodiment is that the cylindrical-conical container 15 constituting the powder collecting section 11 and the cylindrical container 5 constituting the powder melting section 1 are integrated, and a conduit (pipe line) connecting each container This is because the pipe line 14) in Figure 2 has been omitted. According to such a configuration, since the powder melting section 1 and the powder collecting section 11 are integrated, it is possible to realize a compact powder melting processing apparatus.
尚、上記各実施例において、排気装置22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、排気管23を排出先に集塵器24を備え
ることを要件とするものではなく、排気管23の
排気先が大気或いは廃棄物を焼却する焼却炉の中
であつてもよい。更に、本発明は粉状体捕集部1
1を構成する円筒円錐形容器15の材質を限定す
るものではないが、一般的には金属で構成され
る。又、溶融処理後の粉状体9を排出するため、
円筒容器5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 22 (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. Furthermore, the present invention does not require that the exhaust pipe 23 be provided with a dust collector 24 at the exhaust destination, and even if the exhaust destination of the exhaust pipe 23 is in the atmosphere or in an incinerator that incinerates waste. good. Furthermore, the present invention provides a powder collecting section 1.
Although the material of the cylindrical-conical container 15 constituting the container 1 is not limited, it is generally made of metal. In addition, in order to discharge the powder 9 after the melting process,
A discharge valve may be provided at the bottom of the cylindrical container 5.
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、円筒形胴部及び漏斗形底部を有
し、該漏斗形底部が粉状体溶融部と連通する粉状
体捕集部を負圧状態にして粉状体を旋回気流とし
て前記円筒形胴部に吸引導入し、該円筒形胴部の
周壁に沿つて沈降捕集し、粉状体溶融部に落下さ
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貯留部から移送することは勿
論のこと、粉状体にマイクロ波照射中に副生ガス
が発生し、ダステイングによつて粉状体の一部が
粉状体捕集部に戻つても、旋回気流に捕捉され再
び粉状体溶融部に戻り、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 described above in detail, the powder melting processing apparatus of the present invention has a cylindrical body and a funnel-shaped bottom, and the funnel-shaped bottom has a powder collecting section that communicates with the powder melting section. The structure is such that the powder is brought into a negative pressure state as a swirling airflow and sucked into the cylindrical body, where it settles and is collected along the peripheral wall of the cylindrical body and falls into the powder melting section. . For this reason, it is not only possible to transfer the powder from the storage section without scattering the powder to the outside, but also by-product gas is generated during the microwave irradiation of the powder, and part of the powder is removed by dusting. Even if the powder returns to the powder collecting section, it is captured by the swirling airflow and returns to the powder melting section, and is not scattered to the outside. Therefore, it can be said to be extremely safe without contaminating the surrounding area.
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図、第3図
は第2図のA−A断面図、第4図は本発明の他の
実施例を示す図、第5図は本発明の更に他の実施
例を示す図、第6図は第5図のB−B断面図であ
る。
1……粉状体溶融部、2……フランジ部、3,
4……円筒、5……円筒容器、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、11……粉状体捕集部、12……
円筒形胴部、13……漏斗形底部、14……管
路、15……円筒円錐形容器、18……粉状体貯
留部、19……粉状体導入管、22……排気装
置、23……排気管、24……集塵器。
FIG. 1 is a conceptual explanatory diagram of a known powder melting processing apparatus, FIG. 2 is a diagram showing an embodiment of the present invention, FIG. 3 is a sectional view taken along line A-A in FIG. 2, and FIG. FIG. 5 is a diagram showing still another embodiment of the invention, and FIG. 6 is a sectional view taken along line BB in FIG. 5. 1...Powder melting part, 2...Flange part, 3,
4... Cylinder, 5... Cylindrical container, 6... Oscillator, 7
...Microwave waveguide, 8...Matching mechanism,
9... Powder, 11... Powder collection section, 12...
Cylindrical body, 13...funnel-shaped bottom, 14...pipe line, 15...cylindrical-conical container, 18...powder storage section, 19...powder introduction pipe, 22...exhaust device, 23...exhaust pipe, 24...dust collector.
Claims (1)
ら成る粉状体溶融部を備えた粉状体溶融処理装置
において、円筒形胴部及び漏斗形底部から成り該
漏斗形底部が前記粉状体溶融部と連通する円筒円
錐形容器を設け、該円筒円錐形容器の円筒形胴部
の周壁に、粉状体導入管を接線方向に接続すると
共に、該円筒円錐形容器の円筒形胴部の頂部に、
一端が排気装置に接続された排気管を貫設するこ
とにより粉状体捕集部を形成し、該粉状体捕集部
を負圧状態にして粉状体貯留部から粉状体を前記
粉状体捕集部に旋回気流として導入し、該粉状体
捕集部の容器の周壁に沿つて沈降させ前記粉状体
溶融部に落下させ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 equipped with a powder melting section consisting of a cylindrical container constituting a microwave cavity resonator, the powder melting section is composed of a cylindrical body and a funnel-shaped bottom, and the funnel-shaped bottom is used for melting the powder. A cylindrical-conical container is provided which communicates with the cylindrical-conical container, and a powder introduction tube is tangentially connected to the peripheral wall of the cylindrical body of the cylindrical-conical container, and the top of the cylindrical trunk of the cylindrical-conical container is To,
A powder collection section is formed by penetrating an exhaust pipe whose one end is connected to an exhaust device, and the powder collection section is brought into a negative pressure state to remove the powder from the powder storage section. Powder material is introduced into a powder collecting section as a swirling airflow, settling along a peripheral wall of a container of the powder collecting section, and falling into the powder melting section. Melting processing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58129982A JPS6021499A (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 |
|---|---|---|---|
| JP58129982A JPS6021499A (en) | 1983-07-15 | 1983-07-15 | Device for melting and treating granular body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6021499A JPS6021499A (en) | 1985-02-02 |
| JPH0441318B2 true JPH0441318B2 (en) | 1992-07-07 |
Family
ID=15023230
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58129982A Granted JPS6021499A (en) | 1983-07-15 | 1983-07-15 | Device for melting and treating granular body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6021499A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2566163B2 (en) * | 1989-05-23 | 1996-12-25 | 株式会社荏原製作所 | Waste melting furnace |
-
1983
- 1983-07-15 JP JP58129982A patent/JPS6021499A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6021499A (en) | 1985-02-02 |
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