JP2002214391A - Calcined body breaking method of molten glass liquid surface - Google Patents

Calcined body breaking method of molten glass liquid surface

Info

Publication number
JP2002214391A
JP2002214391A JP2001013427A JP2001013427A JP2002214391A JP 2002214391 A JP2002214391 A JP 2002214391A JP 2001013427 A JP2001013427 A JP 2001013427A JP 2001013427 A JP2001013427 A JP 2001013427A JP 2002214391 A JP2002214391 A JP 2002214391A
Authority
JP
Japan
Prior art keywords
glass
molten glass
supply pipe
liquid surface
calcined body
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
Application number
JP2001013427A
Other languages
Japanese (ja)
Other versions
JP4449222B2 (en
Inventor
Toshihiro Yamanaka
智弘 山中
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.)
IHI Corp
Original Assignee
IHI 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 IHI Corp filed Critical IHI Corp
Priority to JP2001013427A priority Critical patent/JP4449222B2/en
Publication of JP2002214391A publication Critical patent/JP2002214391A/en
Application granted granted Critical
Publication of JP4449222B2 publication Critical patent/JP4449222B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B3/00Charging the melting furnaces

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Melting And Manufacturing (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a new calcined body breaking method of a molten glass liquid surface capable of certainly and speedily breaking and removing a calcined body produced on the molten glass liquid surface. SOLUTION: A purge line 16 is connected to a glass bead supply pipe 13, and glass beads B are supplied from the glass bead supply pipe 13 into a glass melting furnace 1 and simultaneously compressed air is blown from the purge line 16 to strongly collide the glass beads B against the molten glass G liquid surface. Thus, the calcined body S on the molten glass G liquid surface can be certainly and speedily broken and removed, and inconvenience such as degradation of fluidity due to abnormal temperature rising of the molten glass G can be avoided.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、高レベル放射性廃
液をガラス固化する際に用いられるガラス溶融炉に係
り、特にそのガラス溶融炉の溶融ガラス液面に形成され
る仮焼体を破壊・除去できる仮焼体破壊方法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a glass melting furnace used for vitrifying high-level radioactive liquid waste, and more particularly to breaking and removing a calcined body formed on a liquid glass surface of the glass melting furnace. The present invention relates to a method for destroying a calcined body.

【0002】[0002]

【従来の技術】使用済み核燃料の再処理後に生ずる高レ
ベル放射性廃液は、極めて高い放射線と崩壊熱を有して
おり、液体のままでは処分が困難であることから、図2
に示すような構造をしたガラス溶融炉1内に送られ、こ
こでほう珪酸ガラス等からなるガラス原料(ガラスビー
ズ,ガラスカートリッジ等)と共に高温で溶かし合わさ
れながらキャニスタcと称される耐食性のステンレス容
器内に詰め込まれてガラス固化体として安定化された
後、一定期間自然冷却されてから地中深く地層処分する
ことが計画されている。
2. Description of the Related Art High-level radioactive liquid waste generated after reprocessing of spent nuclear fuel has extremely high radiation and decay heat, and is difficult to dispose of as a liquid.
Is melted together with a glass material (glass beads, glass cartridge, etc.) made of borosilicate glass or the like at a high temperature and is a corrosion-resistant stainless steel container called a canister c. It is planned to stabilize it as a vitrified body after being packed inside, and then cool it naturally for a certain period of time before disposing of it deep underground.

【0003】このようなガラス固化に用いられるガラス
溶融炉1は、図示するように耐火煉瓦からなる炉本体2
の底部にその内部の溶融ガラスGを流下する流下孔3を
有する底部電極4を備えると共にその側壁に一対の主電
極5,5と補助電極6,6とを備えた構造となってい
る。
[0003] A glass melting furnace 1 used for such vitrification includes a furnace main body 2 made of a refractory brick as shown in the figure.
And a pair of main electrodes 5 and 5 and auxiliary electrodes 6 and 6 on the side walls.

【0004】そして、先ず、この炉本体2の天井壁に設
けられた投入口7から高レベル放射性廃液とガラス原料
を所定の比率で投入した後、主電極5,5間に電流を流
してジュール熱を発生させることで投入されたガラス原
料を高温に加熱して高レベル放射性廃液とガラス原料と
がその炉内で十分に溶かし合わされて溶融ガラスGとな
る。次いで、この炉内の溶融ガラスGが所定量となった
ならば、その下部に位置する補助電極6,6間と底部電
極4及び主電極5,5間に電気を流して下層部のガラス
原料を溶融すると共に、流下孔3から延びる流下ノズル
8をその周囲の電熱コイル9で加熱して内部の溶融ガラ
スGを結合装置10で結合された下部のキャニスタc内
に連続的に流下させてガラス固化体として収容するよう
になっている。
[0004] First, a high-level radioactive waste liquid and a glass raw material are charged at a predetermined ratio from a charging port 7 provided on the ceiling wall of the furnace main body 2, and an electric current is applied between the main electrodes 5 and 5 to cause a joule. By generating heat, the charged glass material is heated to a high temperature, and the high-level radioactive liquid waste and the glass material are sufficiently melted in the furnace to form a molten glass G. Next, when the amount of the molten glass G in the furnace reaches a predetermined amount, electricity flows between the auxiliary electrodes 6 and 6 located under the furnace and between the bottom electrode 4 and the main electrodes 5 and 5 to lower the glass material in the lower layer. Is melted, and the falling nozzle 8 extending from the falling hole 3 is heated by the surrounding electric heating coil 9 to continuously flow the molten glass G inside into the lower canister c joined by the joining device 10 to reduce the glass. It is designed to be housed as a solid.

【0005】尚、この溶融炉1内で発生したガスはオフ
ガスとして排気口11から排気され、図示しないHEP
Aフィルター等で放射性物質が完全に捕集除去されて無
害化された後、大気中に放出されるようになっている。
The gas generated in the melting furnace 1 is exhausted from the exhaust port 11 as off-gas,
The radioactive material is completely collected and removed by an A filter or the like, rendered harmless, and then released into the atmosphere.

【0006】[0006]

【発明が解決しようとする課題】ところで、このように
溶融ガラスGを順次流下させることで炉内の溶融ガラス
Gが減少したならば、その流下を一時停止し、再度減少
した分だけその投入口7から新たなガラス原料と廃液を
つぎ足し、加熱・溶融するようになるが、この新たに廃
液やガラス原料を投下した際に、溶融ガラスGの表層部
が急激に冷やされてその液面に薄い膜状の仮焼体Sが形
成されることがある。
If the molten glass G in the furnace is reduced by sequentially flowing the molten glass G in this way, the flow is temporarily stopped, and the inlet is reduced by the reduced amount. 7, a new glass raw material and waste liquid are added and heated and melted. When the new waste liquid and glass raw material are dropped, the surface layer of the molten glass G is rapidly cooled and the liquid surface becomes thin. A film-like calcined body S may be formed.

【0007】この仮焼体Sの発生メカニズム及びその成
分等の詳細については現在のところ不明であり、今後さ
らなる実験・研究が必要となるが、少なくともこのよう
な仮焼体Sが溶融ガラスGの液面に生成されると、炉内
の溶融ガラスGの熱がプレナム(気相)P側に逃げ難く
なって炉内の溶融ガラスG、特にその液面付近の温度が
急激に上昇して溶融ガラスGの流動性が悪化するといっ
た不都合が発生する。
The mechanism of generation of the calcined body S and the details of its components are unknown at present, and further experiments and studies will be required in the future. When generated on the liquid surface, the heat of the molten glass G in the furnace hardly escapes to the plenum (gas phase) P side, and the temperature of the molten glass G in the furnace, particularly near the liquid level, rises sharply and melts. The disadvantage that the fluidity of the glass G is deteriorated occurs.

【0008】すなわち、この溶融ガラスGの温度は複数
の温度センサーによって常時監視され、その温度センサ
からの信号に応じて制御装置が電極5,5の電流値をコ
ントロールするようになっているが、このような仮焼体
Sが発生して溶融ガラスGから熱が逃げ難くなってその
温度が必要以上に上昇すると、温度センサーが誤作動
し、電極5,5の電流値を必要以上に減少して溶融ガラ
スGの粘度が上昇し、ガラス流下性が著しく悪化してし
まうことがある。
That is, the temperature of the molten glass G is constantly monitored by a plurality of temperature sensors, and a control device controls the current values of the electrodes 5 and 5 in accordance with signals from the temperature sensors. When the calcined body S is generated and the heat hardly escapes from the molten glass G and the temperature rises more than necessary, the temperature sensor malfunctions, and the current values of the electrodes 5 and 5 decrease more than necessary. As a result, the viscosity of the molten glass G increases, and the glass flowability may be significantly deteriorated.

【0009】そこで、本発明はこのような課題を有効に
解決するために案出されたものであり、その目的はこの
ような不都合を招く仮焼体が発生してもこれを確実かつ
迅速に破壊・除去することができる新規な溶融ガラス液
面の仮焼体破壊方法を提供するものである。
Accordingly, the present invention has been devised to effectively solve such a problem, and its object is to ensure that even if a calcined body causing such inconvenience occurs, it can be reliably and promptly made. An object of the present invention is to provide a novel method for destroying a calcined body of a liquid surface of a molten glass which can be destroyed and removed.

【0010】[0010]

【課題を解決するための手段】上記課題を解決するため
に本発明は、請求項1に示すように、ガラス溶融炉内の
溶融ガラス液面に生成する仮焼体の破壊方法において、
上記ガラス溶融炉の原料供給口に設けられるガラスビー
ズ供給管にパージラインを接続し、そのガラスビーズ供
給管からガラス溶融炉内にガラスビーズを供給すると同
時に上記パージラインから圧縮空気を吹き込んでそのガ
ラスビーズを溶融ガラス液面に勢い良く衝突させながら
供給するようにしたものである。
According to the present invention, there is provided a method for destroying a calcined body formed on a liquid surface of a molten glass in a glass melting furnace.
A purge line is connected to a glass bead supply pipe provided at a raw material supply port of the glass melting furnace, and glass beads are supplied from the glass bead supply pipe into the glass melting furnace while compressed air is blown from the purge line. The beads are supplied while vigorously colliding with the liquid surface of the molten glass.

【0011】これによって、ガラスビーズの供給と同時
に溶融ガラス液面に形成された仮焼体を確実に破壊・除
去することができるため、溶融ガラス中に熱が溜まるこ
となく、良好なガラス溶融処理を実施することができ
る。
[0011] With this, the calcined body formed on the liquid surface of the molten glass can be reliably destroyed and removed at the same time as the supply of the glass beads. Can be implemented.

【0012】また、請求項2に示すように、上記ガラス
ビーズ供給管の下端部を上記溶融ガラスの液面付近まで
延出させると共に、そのパージライン接続部から下端ま
でを直線状に形成すれば、ガラスビーズを溶融ガラス液
面側にダイレクトに送り出すことができるため、より効
果的に仮焼体に衝突させ、これを破壊・除去することが
できる
According to a second aspect of the present invention, the lower end of the glass bead supply pipe extends to near the liquid surface of the molten glass, and a straight line is formed from the connection part of the purge line to the lower end. Since the glass beads can be sent directly to the liquid side of the molten glass, the glass beads can be more effectively collided with the calcined body, which can be destroyed and removed.

【0013】[0013]

【発明の実施の形態】次に、本発明を実施する好適一形
態を添付図面を参照しながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, a preferred embodiment of the present invention will be described with reference to the accompanying drawings.

【0014】図1は、本発明方法に係るガラス溶融炉1
上部の原料供給管12付近の実施の一形態を示したもの
である。
FIG. 1 shows a glass melting furnace 1 according to the method of the present invention.
1 shows an embodiment in the vicinity of an upper raw material supply pipe 12.

【0015】図示するように、この原料供給管12は、
炉本体2の天井壁に形成された投入口7のフランジ7a
に、これを垂直に貫通するように取り付けられたもので
あり、溶融ガラスとなるガラス原料と高レベル放射性廃
液とをその上方から投下させて炉本体2内に供給するよ
うになっている。
As shown, the raw material supply pipe 12 is
Flange 7a of inlet 7 formed on the ceiling wall of furnace body 2
The glass raw material to be molten glass and the high-level radioactive liquid waste are dropped from above and supplied into the furnace main body 2.

【0016】すなわち、この原料供給管12には、図示
しないガラス原料供給部から延びるガラスビーズ供給管
13と、廃液タンクから延びる廃液供給管14とがそれ
ぞれ貫通して設けられており、ガラスビーズ供給管13
からガラス原料となる粒径が数mmのガラスビーズB
が、また、廃液供給管14から高レベル放射性廃液がそ
れぞれ独立して供給されるようになっている。
That is, the raw material supply pipe 12 is provided with a glass bead supply pipe 13 extending from a glass raw material supply section (not shown) and a waste liquid supply pipe 14 extending from a waste liquid tank. Tube 13
Glass beads B with a particle size of a few mm
However, the high-level radioactive waste liquid is supplied independently from the waste liquid supply pipe 14.

【0017】また、この原料供給管12には、同じくガ
ラス原料となるガラスカートリッジCを供給するための
ガラスカートリッジ供給管15も接続されており、ガラ
ス繊維からなるガラスカートリッジCを原料供給管12
側に送り込みながらそのガラスカートリッジC中に高レ
ベル放射性廃液を染み込ませてその廃液と共に炉本体2
内へ順次落下・供給するようになっている。
A glass cartridge supply pipe 15 for supplying a glass cartridge C, which is also a glass raw material, is also connected to the raw material supply pipe 12.
The high level radioactive waste liquid is impregnated into the glass cartridge C while being sent to the side of the furnace body 2 together with the waste liquid.
It is designed to fall and supply sequentially inside.

【0018】ここで、本発明にあっては、ガラスビーズ
Bを供給するガラスビーズ供給管13が、図示するよう
に原料供給管12の側面を斜め下方に貫通すると共に、
その下端部が原料供給管12の下端のさらに下方で溶融
ガラスGの液面付近まで延出した直線状態となってお
り、ガラスビーズBを溶融ガラスGの液面側まで真っ直
ぐに案内して供給するようになっている。
Here, in the present invention, the glass bead supply pipe 13 for supplying the glass beads B penetrates the side of the raw material supply pipe 12 obliquely downward as shown in FIG.
The lower end portion is in a linear state extending further below the lower end of the raw material supply pipe 12 to near the liquid surface of the molten glass G, and guides the glass beads B straight to the liquid surface side of the molten glass G to supply the glass beads B. It is supposed to.

【0019】さらに、このガラスビーズ供給管13に
は、パージライン16が接続されており、パージ用のエ
ア、すなわち高圧の圧縮空気を任意にガラスビーズ供給
管13内に吹き込んでその内部を自重落下するガラスビ
ーズBをさらに加速して溶融ガラスGの液面上に衝突さ
せるようになっている。
Further, a purge line 16 is connected to the glass bead supply pipe 13, and air for purging, that is, high-pressure compressed air is arbitrarily blown into the glass bead supply pipe 13 to drop its own weight under its own weight. The glass beads B are further accelerated to collide with the liquid surface of the molten glass G.

【0020】従って、前述したようにガラス固化体を製
造することによって溶融ガラスGの容量が減少した炉本
体2内に、再度、新たな廃液と共に、このガラスビーズ
供給管13からガラスビーズBをパージエアーによって
溶融ガラスGの液面に対して勢い良く吹き付ければ、そ
の溶融ガラスGの液面上に形成された仮焼体Sがこのガ
ラスビーズBの衝突による衝撃によって直ちに破壊さ
れ、その溶融ガラスGと混ぜ合わされて消滅するように
なるため、溶融ガラスGの熱が溜まることなく液面上の
プレナムP側へ確実に、すなわち、初期の設計通りに逃
がすことができる。
Therefore, the glass beads B are again purged from the glass bead supply pipe 13 together with the new waste liquid into the furnace main body 2 in which the volume of the molten glass G is reduced by manufacturing the vitrified body as described above. If the liquid surface of the molten glass G is vigorously sprayed with the air, the calcined body S formed on the liquid surface of the molten glass G is immediately destroyed by the impact of the collision of the glass beads B, and the molten glass Since the molten glass G disappears after being mixed with G, the heat of the molten glass G can be reliably released to the plenum P side on the liquid surface without accumulating, that is, as originally designed.

【0021】すなわち、従来、このガラスビーズBは、
廃液と同様に主にその自重によってガラスビーズ供給管
13内を転げ落ちるようにして供給されるため、仮焼体
Sを破壊するような衝撃を発生することはなかったが、
このようにガラスビーズ供給管13の下端部を液面側に
向けて直線状にし、さらにそのガラスビーズBをパージ
エアーによって加速させて勢い良く衝突させながら供給
することでガラス原料の供給と同時に仮焼体Sを効果的
に破壊・除去することが可能となる。
That is, conventionally, the glass beads B
Like the waste liquid, it is supplied so as to roll down the glass bead supply pipe 13 mainly due to its own weight, so that there is no impact that destroys the calcined body S.
In this way, the lower end of the glass bead supply pipe 13 is made linear toward the liquid surface side, and the glass beads B are accelerated by the purge air and supplied while being vigorously collided, so that the glass raw material is supplied simultaneously with the supply of the glass raw material. The fired body S can be effectively destroyed and removed.

【0022】この結果、炉本体2内の溶融ガラスGの温
度が異常に上昇することがなくなるため、前述したよう
な温度センサの誤作動に伴う粘度上昇による流下不良等
といった不都合を確実に回避することができ、良好なガ
ラス固化処理運転を行うことができる。
As a result, the temperature of the molten glass G in the furnace main body 2 does not rise abnormally, so that inconveniences such as the above-mentioned inferior flow due to an increase in viscosity due to the malfunction of the temperature sensor are reliably avoided. And a good vitrification operation can be performed.

【0023】尚、上述したように原料供給方法として
は、ガラスビーズ供給管13及び廃液供給管14から供
給する方法の他に、ガラスカートリッジ供給管15から
供給する方法及び両者を併用する方法があるが、いずれ
の方法でも原料供給時にこのガラスビーズ供給管13か
らガラスビーズBを勢い良く溶融ガラスGの液面側に吹
き付けるようにすることで本発明の目的を確実に達成す
ることができる。
As described above, as a raw material supply method, in addition to a method of supplying from the glass bead supply pipe 13 and the waste liquid supply pipe 14, a method of supplying from the glass cartridge supply pipe 15 and a method of using both are used. However, in any of the methods, the object of the present invention can be reliably achieved by vigorously spraying the glass beads B from the glass bead supply pipe 13 onto the liquid surface side of the molten glass G at the time of supplying the raw material.

【0024】また、図中17は、水供給管であり、必要
に応じて炉本体2内に水を供給し、その炉本体2内の廃
液を任意に希釈するものである。
In the figure, reference numeral 17 denotes a water supply pipe for supplying water into the furnace main body 2 as required, and arbitrarily diluting the waste liquid in the furnace main body 2.

【0025】[0025]

【発明の効果】以上要するに本発明によれば、ガラス原
料の供給と同時に溶融ガラスの液面に生成した仮焼体を
確実に破壊・除去することができるため、溶融ガラス温
度の異常上昇による流動性の悪化等の不都合を未然に回
避することができる等といった優れた効果を発揮するこ
とができる。
In summary, according to the present invention, since the calcined body generated on the liquid surface of the molten glass can be reliably destroyed and removed simultaneously with the supply of the glass raw material, the flow caused by the abnormal rise of the molten glass temperature Excellent effects such as inconvenience such as deterioration of the properties can be avoided beforehand.

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

【図1】本発明に係る溶融ガラス液面の仮焼体破壊方法
の実施の一形態を示す説明図である。
FIG. 1 is an explanatory view showing one embodiment of a method for breaking a calcined body of a molten glass liquid surface according to the present invention.

【図2】従来のガラス溶融炉の構造を示す説明図であ
る。
FIG. 2 is an explanatory view showing the structure of a conventional glass melting furnace.

【符号の説明】[Explanation of symbols]

1 ガラス溶融炉 2 炉本体 12 原料供給管 13 ガラスビーズ供給管 14 廃液供給管 15 ガラスカートリッジ供給管 16 パージライン B ガラスビーズ C ガラスカートリッジ G 溶融ガラス S 仮焼体 DESCRIPTION OF SYMBOLS 1 Glass melting furnace 2 Furnace main body 12 Raw material supply pipe 13 Glass bead supply pipe 14 Waste liquid supply pipe 15 Glass cartridge supply pipe 16 Purge line B Glass beads C Glass cartridge G Molten glass S Calcined body

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ガラス溶融炉内の溶融ガラス液面に生成
する仮焼体を破壊する方法において、上記ガラス溶融炉
の原料供給口に設けられるガラスビーズ供給管にパージ
ラインを接続し、そのガラスビーズ供給管からガラス溶
融炉内にガラスビーズを供給すると同時に上記パージラ
インから圧縮空気を吹き込んでそのガラスビーズを溶融
ガラス液面に勢い良く衝突させるようにしたことを特徴
とする溶融ガラス液面の仮焼体破壊方法。
In a method for destroying a calcined body formed on a liquid level of a molten glass in a glass melting furnace, a purge line is connected to a glass bead supply pipe provided at a raw material supply port of the glass melting furnace. The glass beads are supplied from the bead supply pipe into the glass melting furnace at the same time as the compressed air is blown from the purge line so that the glass beads vigorously collide with the molten glass liquid level. Method of destroying the calcined body.
【請求項2】 上記ガラスビーズ供給管の下端部を上記
溶融ガラスの液面付近まで延出させると共に、上記パー
ジライン接続部から下流側を直線状に形成するようにし
たことを特徴とする請求項1に記載の溶融ガラス液面の
仮焼体破壊方法。
2. The method according to claim 1, wherein a lower end portion of the glass bead supply pipe extends to near a liquid level of the molten glass, and a downstream side from the purge line connection portion is formed linearly. Item 4. The method for destroying a calcined body of a liquid surface of a molten glass according to Item 1.
JP2001013427A 2001-01-22 2001-01-22 Method for destroying calcined body of molten glass liquid surface Expired - Fee Related JP4449222B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001013427A JP4449222B2 (en) 2001-01-22 2001-01-22 Method for destroying calcined body of molten glass liquid surface

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001013427A JP4449222B2 (en) 2001-01-22 2001-01-22 Method for destroying calcined body of molten glass liquid surface

Publications (2)

Publication Number Publication Date
JP2002214391A true JP2002214391A (en) 2002-07-31
JP4449222B2 JP4449222B2 (en) 2010-04-14

Family

ID=18880282

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001013427A Expired - Fee Related JP4449222B2 (en) 2001-01-22 2001-01-22 Method for destroying calcined body of molten glass liquid surface

Country Status (1)

Country Link
JP (1) JP4449222B2 (en)

Also Published As

Publication number Publication date
JP4449222B2 (en) 2010-04-14

Similar Documents

Publication Publication Date Title
US6532768B1 (en) Process for the vitrification of a pulverulent material and apparatus for implementing the process
JP5261038B2 (en) In-furnace monitoring apparatus, in-furnace monitoring method, and furnace operation control method using the same
JPWO2011004851A1 (en) Glass melting furnace, molten glass manufacturing method, glass product manufacturing apparatus, and glass product manufacturing method
JP2002214391A (en) Calcined body breaking method of molten glass liquid surface
JP5216283B2 (en) Waste asbestos melting furnace
KR20130103383A (en) Titanium powder production apparatus and method
JP3173599B2 (en) Incineration method of waste graphite containing radionuclides
JP2008078031A (en) Droplet recovery system and its method
JP3236885B2 (en) Waste treatment equipment
JP4449223B2 (en) Method for destroying calcined body of molten glass liquid surface
JP2002181994A (en) Volume reduction equipment for radioactive waste and its operation method
JP4547809B2 (en) Method for destroying calcined body of molten glass
KR20120055778A (en) Plasma melting system using steam plasma torch and driving method thereof
KR20040020459A (en) Waste feeding and off-gas exhausting apparatus in the plasma melting system and waste management method thereof
JP3941526B2 (en) Waste powder melting method and melting equipment used therefor
JP4258953B2 (en) Glass melting furnace for high-level radioactive liquid waste
CN220648261U (en) Plasma gasification melting furnace with arched grate
JP3904379B2 (en) Dust discharge device for secondary combustion chamber
TWI776499B (en) blast furnace operation method
JP2000292594A (en) Radioactive waste melting processor and processing method
JP2008298306A (en) Portable deformed 12-phase ac plasma discharging device for waste disposal treatment and furnace
JP2003120924A (en) Tapping device of fusion furnace
JP2992257B2 (en) Plasma melting method and apparatus
JP3702033B2 (en) Cooling structure of furnace body in melting furnace
KR100456776B1 (en) apparatus of treating radioactive Dry Active Solid Waste(DAW) and treatment system for destroying by burning up and vitrificating radioactive waste in use with the apparatus

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20071129

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20091216

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100105

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100118

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130205

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130205

Year of fee payment: 3

LAPS Cancellation because of no payment of annual fees