JPS6021499A - Device for melting and treating granular body - Google Patents
Device for melting and treating granular bodyInfo
- Publication number
- JPS6021499A JPS6021499A JP58129982A JP12998283A JPS6021499A JP S6021499 A JPS6021499 A JP S6021499A JP 58129982 A JP58129982 A JP 58129982A JP 12998283 A JP12998283 A JP 12998283A JP S6021499 A JPS6021499 A JP S6021499A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- cylindrical
- container
- melting
- section
- 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
Landscapes
- Furnace Details (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
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り−
る粉状体溶融処]!l!装置に関し、更に詳しくは、汚
染性の焼月1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りる。DETAILED DESCRIPTION OF THE INVENTION The present invention uses microwaves to melt and solidify powder.
Powder melting process]! l! More specifically, the present invention relates to a powder melting apparatus that can safely melt powder such as contaminating ash.
マイクロ波を用いる粉状体の溶融処理方法は、加熱が粉
状体を構成づる物質自体の分子運動にVづく誘電損失に
にって行われるため、処理粉状体を内部から均一に■つ
効率よく加熱溶+Mりることができるので従来の電熱加
熱や幅用加熱による方法に比較して原理的に格段に(受
れτいる。このため、多くの産業分野において様々な[
1的に利用されているが、特に最近これを産呆廃史物処
理に応用し、各種産業施設A5原子力施設から1)1出
される廃棄物をマイク[1被照則にJ5り加熱溶融し、
廃棄物中に含まれる二酸化珪素ににり刀ラス化し固化り
る方法が注目されつつある。In the method of melting powder using microwaves, heating is performed by dielectric loss caused by the molecular motion of the substance itself that makes up the powder, so the processed powder can be uniformly melted from the inside. Since it is possible to efficiently heat melt + M, it is theoretically much more popular than conventional electric heating or width heating methods.For this reason, various [
Recently, it has been applied to the treatment of industrial waste and historical materials, and the waste generated from various industrial facilities and A5 nuclear facilities is heated and melted using a microphone [1]. ,
A method of turning silicon dioxide contained in waste into a lath and solidifying it is attracting attention.
このための溶融処理装置とし−(各種の乙のが考えられ
ている。例えば、その一つとし゛(、マイクロ波空胴共
振器を構成づる円筒容器から成るわ)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 melting processing equipment have been considered for this purpose. BACKGROUND OF THE INVENTION Solid body melt processing apparatuses are known.
この種の粉状体溶融処理装置にd3 +プる粉状溶融部
の概略構成は第1図で示づことができる。即ち、粉状体
溶融部1は、フランジ市合部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4h)ら成る円筒容器5
の上部に、発振器6が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ど、共振時のマツチングをと
るマッヂング機構33と、粉状体9を導入する粉状体導
入管10とを連結覆ることにより構成され、マイクロ波
を導入したとぎ、円筒容器5の内部が最も強い電界を生
り”るモードで共振りるマイクロ波空胴共振器を形成づ
るようになっている。The schematic structure of the powder melting section of this type of powder melting processing apparatus can be shown in FIG. That is, the powder melting section 1 includes a cylindrical container 5 consisting of metal cylinders 3 and 4h) with high conductivity that are joined or separated at the flange meeting section 2.
A microwave waveguide 7 that guides the microwave emitted from the oscillator 6 into the cylindrical container 5, a matching mechanism 33 that performs matching during resonance, and a powder introduction pipe 10 that introduces the powder 9 are installed on the top of the oscillator 6. When microwaves are introduced, a microwave cavity resonator is formed which resonates in a mode in which the inside of the cylindrical container 5 generates the strongest electric field.
この粉状体溶融処理装置におい(、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tttl 1173りると、わ)状体9は加熱溶R
11シ、その後/1文冷状態にd3 <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ff6東物の場合)にJ−っで1粉状体9はカラ
ス化又は岩石化して固化づる。この固化した粉状体S)
は、円筒4と共に金属製円筒3がら分離され、廃棄処理
されることになる。In this powder melting processing apparatus, after introducing a predetermined amount of powder 9 into the cylindrical container 5, the powder 9 is irradiated with microwaves at tttl 1173, and the powder 9 is heated. Molten R
11 shi, then / 1 sentence in the cold state d3 < and the ingredients contained in the powder 9, such as silicon dioxide (if the powder 9 is ff6 Tomono from a nuclear facility), J-de 1 powder 9 becomes crow or rocks and solidifies. This solidified powder S)
will be separated from the metal cylinder 3 together with the cylinder 4 and disposed of.
この装置は一時に多用の粉状体の処理が可能である等の
点で、実用−[、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、1扇子力発電所、核燃11
31処理’Jl場、ラジΔアイソト−プを1吏用づる/
71!r設等におtJる廃棄物を焼却しU UPだ放射
性焼却灰等の放射性の粉状体を、−、l=記溶融処理装
置で溶r1!処理しようと覆ると、次の如き大きな問題
が生じる。This apparatus is considered to be the most excellent as a practical waste treatment apparatus in that it is capable of processing a large number of powdered materials at once. However, 1 fan power plant, 11 nuclear
31 Processing 'Jl field, using one radial delta isotope/
71! Radioactive powder such as radioactive incineration ash is incinerated in a facility, etc., and radioactive powder such as radioactive incineration ash is melted in a melting processing device where −, l= is used. If you try to deal with it, the following big problems will arise.
まず、従来の粉状体溶融処理装置i9tで(,1、オ多
)状体9を円筒容器5内に導入し1.:後、ンイクロ波
をjji、7則すると、マイクロ波照射中に発イ1りる
副二Lガスによって円筒容器5が加圧状態とく【す、粉
状体9が円筒3と4のフランジ部2ヤ)マイクしI波力
人艙7及び粉状体導入管10の接続部から飛1)(シた
り吹き出したりして周囲を汚染りることがある。このよ
うな粉状体9が外部に出ることは、わ)状体9が原子力
/II段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, a (, 1, Ota) shaped body 9 is introduced into a cylindrical container 5 using a conventional powder melting processing apparatus i9t. : After that, the cylindrical container 5 is put into a pressurized state by the secondary gas emitted during microwave irradiation. 2) The microphone may fly out from the connection between the I-wave power cabin 7 and the powder introduction pipe 10. 1) (It may spill or blow out, contaminating the surrounding area. Such powder 9 may be exposed to the outside. If the W)-shaped body 9 is a waste from a nuclear power/II stage, it is extremely dangerous and poses a major safety problem.
又、/J5L !JJ性粉状体(焼却灰)の場合はでの
粒径が小さく容易に浮遊乃至飛fil(Jる。従って、
かかる危険な故剣性粉状体を焼u1揚から溶融処理賛同
まて、周囲に灰を飛散さVずに輸送することもかなり困
5!11なことCある。Also, /J5L! In the case of JJ powder (incineration ash), the particle size is small and it easily floats or flies away. Therefore,
It is quite difficult to transport such dangerous powdered materials from incineration to melting without scattering the 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、イq
月−1的は、粉状体のマイクにll熱照射中J3りる粉
状体の溶融処理装置外への飛ii!や吹き出しをなくし
、にり安全性を高めた粉状体溶融処理装置を提(Jtり
ることにある。The present invention has been made in view of these points, and has the following advantages:
Month-1 target is J3 powder flying out of the melting processing equipment during heat irradiation to the powder microphone! Our goal is to provide a powder melting processing device that eliminates blow-outs and improves safety.
この目的を達成する本発明は、マイクロ波空胴共振器を
構成り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−C1円筒形胸部及び漏斗形底部か
ら成り該11i13+形底部が前記粉状体溶融部と連通
づる円筒円錐形容器を設け、該円旧1円811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l、:排気管をd設J゛ること
にに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+iQ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
壁に治って沈降させ前記わ)状1木溶81(部に落1;
させるJ、うに構成したことをR徴どりるしの(ある。To achieve this object, the present invention provides 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 whose 11i13+-shaped bottom communicates with the powder melting section is provided, and a powder introduction pipe is tangentially connected to the peripheral wall of the cylindrical body of the 1-yen 811-shaped container, A powder collecting section is formed by installing an exhaust pipe at the top of the cylindrical body of the cylindrical-conical container, one end of which is connected to an exhaust device, and The collection section is brought into a negative pressure state, and the powder is introduced from the powder storage section into the +iQ powder collection section as a swirling airflow, and is allowed to settle and settle on the peripheral wall of the container of the powder collection section. Said wa) shape 1 wood melt 81 (part dropped 1;
J, the sea urchin is composed of R sign (there is).
以下、図面を参照し本光明の実施例を詳細に説明り゛る
。Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
第2図及び第3図(第2図のΔ−Δ10j面図)は、本
発明の一実施例を承り説明図で、第1図と同様、1は粉
状体溶融部Cあり、円筒3./lをフランジ市合部2で
谷II;(可能に結合し!、二円筒容器5)と、5C振
器6からのマイクロ波を導入りるマイクロ波導波管7と
、マップング1914ie 9とて構成されζいる。Figures 2 and 3 (Δ-Δ10j plane view in Figure 2) are explanatory diagrams of an embodiment of the present invention.Same as Figure 1, 1 has a powder melting part C, and a cylinder 3 .. /l at the flange joint part 2; (possibly combined!, two cylindrical containers 5), a microwave waveguide 7 introducing the microwave from the 5C shaker 6, and a mapping 1914ie 9. It is composed of ζ.
11は粉状体捕集部であり、↑′τ路17′Iを介しく
粉状体溶rA1!部1と連通りる円1;1円鉗形容器1
;5と、一端が円筒円錐形容器15の円筒形1111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に開門される粉状体導入τへ1<−)と、 端側か
円f1M円♀1を形容器15の円筒形胴部12の1cJ
部をC1通して’AQ if!iされ、他端:側がター
ボフッ・ン、ブ゛レードファン等の排気装置22に接続
される排気筑23とで構成されている。粉状体捕集部1
1の排気側、即ち、排気装@22の排気口は、管路20
を介して集廂器24に接続され、該集廂器24でもって
排気に同伴した少量の粉状体を完全に補集し、管路25
を介して粉状体貯留部18に戻づ構成となっている。Reference numeral 11 denotes a powder collecting section, which collects powder dissolved rA1 through the ↑'τ path 17'I! Circle 1 connected to part 1; 1-yen hook-shaped container 1
5, and one end is tangentially connected to the peripheral wall of the cylindrical 1111 part 12 of the cylindrical-conical container 15, and the other end is opened to the powder storage section 18 (1<-). , 1cJ of the cylindrical body 12 of the container 15 in the shape of a circle f1M circle ♀1 on the end side
'AQ if!' through C1. 1, and an exhaust box 23 whose other end is connected to an exhaust device 22 such as a turbo fan or blade fan. Powder collection part 1
The exhaust side of No. 1, that is, the exhaust port of the exhaust system @ 22, is connected to the pipe 20.
It is connected to the collector 24 via the collector 24, and the collector 24 completely collects a small amount of powder accompanying the exhaust gas, and the pipe 25
The powder is returned to the powder storage section 18 via the.
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2
2を始動づると、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゜乏j内に吸引される。粉状体導入
管19の一端が円ぬ形胴部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、旋回気流どなって円筒形胴部12を流れ、遠心
力の作用を受GJて円筒形胴部12の周壁に沿って下降
(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。In this processing apparatus, the exhaust device 2 of the powder collecting section 11
2 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 in a negative pressure state,
Powder 9 in powder storage section 18 via powder introduction pipe 19
is sucked into a cylindrical-conical container 1°. Since one end of the powder introduction pipe 19 is tangentially connected to the circumferential wall of the circular body 12, the powder 9 sucked and introduced into the cylindrical body 12 becomes cylindrical due to the swirling airflow. It flows through the body part 12, receives the action of centrifugal force, descends (settles) along the circumferential wall of the cylindrical body part 12, and flows through the funnel-shaped bottom part 13 and the pipe line 14 to the cylindrical container of the powder melting part 1. Fall to 5.
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、排気装置音22を稼動のまま、マイ
クロ波導波管7からマイク11波を導入し、マツチング
機桶8と共に共振さVるど、円筒容器5の内部に強い電
界が生じる。この電界によって円筒容器5内の粉状体9
は加熱され溶融りる。With a predetermined amount of powder 9 deposited in the cylindrical container 5 of the powder melting section 1, the microphone 11 waves are introduced from the microwave waveguide 7 while the exhaust system sound 22 is still operating, and the matching machine tub 8 is heated. At the same time, due to the resonance V, a strong electric field is generated inside the cylindrical container 5. This electric field causes the powder 9 inside the cylindrical container 5 to
is heated and melted.
このとぎ、副生ガスが発生する等の外乱のためダスティ
ングが生じ、粉状体9の一部が粉状体捕集部11に戻っ
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の周壁に沿って沈降し円筒容器
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q1シた後、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
状又は岩石状となって固化する。固化した粉状体9は、
円筒3から分前される円筒4と共に排気又は保管処理さ
れる。At this point, 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 will be affected by the centrifugal force. As a result, it sinks again along the peripheral wall of the cylindrical-conical container 15 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. It solidifies. The solidified powder 9 is
The cylinder 3 is evacuated or stored together with the cylinder 4.
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、はとんど粉状体9は含まれていないが、
たとえ含まれ(いたと1)(°も集l!y!:冴24で
捕集され、再び粉状体貯留部18に戻され、上記の処理
I fJi!に再度かけられる。Although the airflow exhausted through the exhaust pipe 23 of the powder collecting section 11 does not contain the powder 9 for the most part,
Even if it is contained, it is collected by the powder 24, returned to the powder storage section 18, and subjected to the above-mentioned processing IfJi! 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。こめ実
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G″Jた点にある。弁2
6は円筒容器5内の粉状体9にマイクロ波を照射中は開
成されるようになっている。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ィングが生じても
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, in which the same parts as in FIG. 2 are denoted by the same reference numerals, and the explanation thereof will be omitted. The feature of this embodiment is that a valve 26 is provided in the pipe line 14 that communicates the powder collecting section 11 and the powder melting section 1.Valve 2
6 is opened while the powder 9 in the cylindrical container 5 is being irradiated with microwaves. Therefore, even if dusting occurs on the powder 9 due to by-product gas during microwave irradiation, the powder does not return to the powder collection section 11.
第5図及び第6図(第5図の13−B断面図)は木鋒明
の史に他の実施例のd1明図で、第2図とlf:il一
部分には同一符号を用い、イの説明は省略りる。Figures 5 and 6 (13-B sectional view in Figure 5) are d1 diagrams of other embodiments in the history of Mok Feng Ming, and the same reference numerals are used for the lf:il part as in Figure 2, The explanation of A is omitted.
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ど粉状体溶融部1を椙成りる円1n容器
5とを一体化し、それぞれの容器を連通りる管路(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
体どなっているため、]ンバクト・な粉状体溶融処理装
置を実現することができる。The feature of this embodiment is that the cylindrical-conical container 15 constituting the powder collecting section 11 and the circular container 5 forming the powder melting section 1 are integrated, and a pipe is connected to each container. Road (2nd
This is because the pipe line 14) in the figure is 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 an efficient powder melting processing apparatus.
尚、上記各実施例において、υl気装同22として(第
4図及び第5図にあってはこれらは省略されている)、
ターボファン、ブレードファン等を用いているが、本発
明はこれに限定づるものではなく、多翼ファン、プロペ
ラファン等のファン(通風機)、ターボブ[1ワー、ル
ーツブ1」ワー等のブロワ−(送風機)、水1ジエクタ
、スヂームエジエクタ簀のニジ〕ニクタであってもにい
3.又、本発明は、排気管23の排出先に集塵器24を
備えることを要イシ1とJるちのではなく、排気管23
の排気光が人気或いは廃棄物を焼IJjりる焼月1炉の
中であってもよい。更に、本発明は粉状体捕集部11を
構成りる円筒円錐形容器1 bの44 ′ii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を排出りるため、円筒容器5の底
部にfJl出用弁を設りてもJ:い、。In each of the above embodiments, the υl air chamber 22 (these are omitted in FIGS. 4 and 5),
Although a turbo fan, a blade fan, etc. are used, the present invention is not limited to these. Fans (ventilators) such as multi-blade fans and propeller fans, and blowers such as turbo fans [1-WER and Roots-Blow 1-WER] are used. (Blower), 1 tank of water, 1 tank of water, 3. In addition, the present invention requires that the dust collector 24 be provided at the discharge end of the exhaust pipe 23, but not in the exhaust pipe 23.
The exhaust light may be in the furnace where the waste is burned or burned. Furthermore, although the present invention does not limit the cylindrical-conical container 1b 44'ii constituting the powder collecting section 11, it is generally made of metal. or,
In order to discharge the powder 9 after the melting process, a fJl outlet valve may be provided at the bottom of the cylindrical container 5.
以上詳しく説明しノこように、本発明の粉状体溶融処理
装置(よ、円筒形胴部及び漏斗形底部を右し、該漏斗形
底部が粉状体溶融部と連通りる粉状体捕東部を負圧状態
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って沈降捕集し、粉状体
溶融部に落下させる構成となっている。このため、粉状
体を外部に飛散づ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、ダスティングによって粉状体の一部が粉状体捕集
部に戻っても、旋回気流に捕捉され再び粉状体溶融部に
戻り、外部に飛散覆ることはない。As explained above in detail, the powder melting processing apparatus of the present invention (with a cylindrical body and a funnel-shaped bottom, the funnel-shaped bottom communicates with the powder melting section) The powder is drawn into the cylindrical body part as a swirling airflow by setting the trapping part under negative pressure, and is collected by sedimentation along the peripheral wall of the cylindrical body part, and is caused to fall into the powder melting part. Therefore, it is not only possible to transfer the powder from the storage part without scattering it to the outside, but also by-product gas is generated during the microwave irradiation of the powder, and the powder is removed by dusting. Even if some of 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 outside.
従って、周囲を汚染することらなく、極めて安全性が高
いと8える。Therefore, it is considered 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1図、第3図は第2図のA−
A断面図、第4図は本発明の伯の実施例を示す図、第5
図は本発明の史に曲の実施例を承り図、第6図は第5図
のB −r、’= VIi面図C′ある。
1・・・粉状体溶融部 2・・・フランジ部3.4・・
・円v:I 5・・・円筒容器6・・・発撮器 7・・
・マイク1−1波う9波貸8・・・マツチング機4苫
9・・・¥5)状(本11・・・粉状体111)東部
12・・・円筒形胴部13・・・漏斗形底部 14・・
・管路15・・・円筒内It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・・・州@器
特9′[出願人 三1[東圧化学株式会社代理人 弁理
士 1゛[島 藤 治Fig. 1 is a conceptual explanatory diagram of a known powder melting processing device;
The figures show an embodiment of the present invention.
A sectional view, FIG. 4 is a diagram showing an embodiment of the present invention, and FIG.
The figure shows an embodiment of the song in the history of the present invention, and FIG. 6 is a view of B-r,'=VIi plane C' of FIG. 1... Powder melting part 2... Flange part 3.4...
・Circle v: I 5... Cylindrical container 6... Shooting device 7...
・Microphone 1-1 Wave 9 Wave Rental 8...Matching machine 4 Toma
9...¥5) (Book 11...Powder 111) Eastern part
12...Cylindrical body 13...Funnel-shaped bottom 14...
・Pipe line 15...Cylindrical It type container 18...Powder storage section 19...Powder introduction pipe 22
... Exhaust device 23 ... Exhaust pipe 24 ... State @Kitoku 9' [Applicant 31 [Toatsu Chemical Co., Ltd. agent Patent attorney 1] [Osamu Shimafuji
Claims (1)
体溶融部を備えた粉状体溶融処理装置において、円筒形
胴部及び漏夕]形底部がら成り該漏斗形底部が前記粉状
体溶融部と連通づる円筒円錐形容器を段【ノ、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
向に接続づると共に、該円筒円夕1[形容器の円筒形胴
部の頂部に、一端が排気′iA首に接続された排気管を
門設すること(JJ、り粉状体捕集部を形成し、該粉状
体捕集部を(1圧状態にして扮状体貯留部から粉状体を
前記粉状体捕集部に施回気流としく導入し、該粉状体捕
集部の容器の周壁に沿っ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りる粉状体温A
lt処理!!装置。[Scope of Claim] A powder melting processing apparatus equipped with a powder melting section consisting of a cylindrical container constituting a microwave cavity resonator, the funnel-shaped body comprising a cylindrical body and a funnel-shaped bottom. A cylindrical-conical container whose bottom communicates with the powder melting section is connected to the circumferential wall of the cylindrical body of the cylindrical-conical container in a tangential direction, and E.1 [Providing an exhaust pipe with one end connected to the exhaust neck at the top of the cylindrical body of the container (JJ, forming a powder collection section and The collecting part is brought into a state of 1 pressure, and the powder is introduced from the dressing part into the powder collecting part as a circulating air stream, and it settles along the peripheral wall of the container of the powder collecting part. Powder body temperature A characterized by being configured such that the powder body is allowed to fall into the powder melting section.
lt processing! ! Device.
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 true JPS6021499A (en) | 1985-02-02 |
| JPH0441318B2 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) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02309188A (en) * | 1989-05-23 | 1990-12-25 | Ebara Corp | Heating and melting furnace for disposal or the like |
-
1983
- 1983-07-15 JP JP58129982A patent/JPS6021499A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02309188A (en) * | 1989-05-23 | 1990-12-25 | Ebara Corp | Heating and melting furnace for disposal or the like |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0441318B2 (en) | 1992-07-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4777192A (en) | Apparatus and method for radiation processing of materials | |
| KR102540803B1 (en) | Lithium ion battery positive electrode materials recovery system and lithium ion battery positive electrode materials recovery method using thereof | |
| CN114505470A (en) | But tail gas purification casting is with multiple cooling of exempting from contact device of turning over case | |
| US4748005A (en) | Apparatus and method for radiation processing of materials | |
| KR102152406B1 (en) | Treatment system and method of paraffin solidified waste | |
| JPH0441319B2 (en) | ||
| JPH0348624B2 (en) | ||
| CN105944479A (en) | Purifying device for lead-containing sulfur-containing flue gas | |
| JPS6111141A (en) | Fusion-treating apparatus for powdery material | |
| JPH0441318B2 (en) | ||
| JP3436502B2 (en) | Wet crusher | |
| JPH1099819A (en) | Waste plastic processing separation equipment | |
| JPS58223434A (en) | Melting treatment device for powder material | |
| CN205949013U (en) | Adopt broken mechanical disintegration grader of microwave -assisted | |
| JP2002320947A (en) | Suspended organism treatment method and apparatus | |
| JP3354720B2 (en) | Method and apparatus for treating explosives and explosives | |
| EP0339111A1 (en) | Method for radiation processing of materials | |
| JPH0452438B2 (en) | ||
| CN221294850U (en) | Medical waste processor | |
| JPH06339745A (en) | Method and apparatus for reprocessing loose material | |
| US4230672A (en) | Apparatus for recovering nuclear fuel from scrap material | |
| JP2005350504A (en) | Polymer resin decomposition treatment method and decomposition treatment apparatus | |
| CN220269878U (en) | Drying and cooling the bio-organic fertilizer screening integrated production line | |
| JPS5888084A (en) | Apparatus for heat-treating waste matter | |
| JPH031103Y2 (en) |