JP2007271492A - Method and system for managing molten metal level - Google Patents

Method and system for managing molten metal level Download PDF

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JP2007271492A
JP2007271492A JP2006098507A JP2006098507A JP2007271492A JP 2007271492 A JP2007271492 A JP 2007271492A JP 2006098507 A JP2006098507 A JP 2006098507A JP 2006098507 A JP2006098507 A JP 2006098507A JP 2007271492 A JP2007271492 A JP 2007271492A
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molten metal
level
melting furnace
melting
metal level
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JP4726678B2 (en
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Hiroyuki Fukada
博之 深田
Tsuneo Sato
常雄 佐藤
Yoshio Izumi
芳生 和泉
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Chugoku Electric Power Co Inc
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

<P>PROBLEM TO BE SOLVED: To enable the efficient melting management of miscellaneous solid waste which takes metal power and the like into consideration. <P>SOLUTION: A method for managing the molten metal level in facilities for a volume reduction of low-level radioactive waste is characterized in that the weight ratio of borax to silica sand is set at 1:1 when the borax and the silica sand are poured into the molten metal in a melting furnace included in the volume-reduction facilities so as to restrain the molten metal level from rising. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、溶湯レベル管理方法、および溶湯レベル管理システムに関する。   The present invention relates to a molten metal level management method and a molten metal level management system.

原子力発電所で発生する低レベル放射性廃棄物のうち、例えば雑固体廃棄物は、ドラム缶に詰められた上でモルタル等の充填を受け、このドラム缶ごと所定の埋設場に埋設処分される。なお、埋設場の広さには限りがあるので、雑固体廃棄物を減容し、埋設されるドラム缶の数を少なくすることが好ましい。   Of the low-level radioactive waste generated at nuclear power plants, for example, miscellaneous solid waste is packed in drums and then filled with mortar, and the drums are disposed of in a predetermined burial site. Since the burial area is limited, it is preferable to reduce the volume of miscellaneous solid waste and reduce the number of drum cans to be buried.

そこで、雑固体廃棄物の減容技術として、高周波誘導加熱方式による溶融減容設備が提案されている。この設備においては、溶融炉内にセットしたキャニスタ内で溶融対象物たる雑固体廃棄物を溶融して減容し固化させた後、キャニスタごとドラム缶に詰める。そして、モルタル等の固型化材料を前記ドラム缶に充填して廃棄体とすることとなる。   Therefore, as a technique for reducing the volume of miscellaneous solid waste, a melting volume reduction facility using a high frequency induction heating method has been proposed. In this facility, miscellaneous solid waste, which is an object to be melted, is melted and reduced and solidified in a canister set in a melting furnace, and then packed together with the canister in a drum can. Then, the drum can is filled with a solidified material such as mortar to form a waste body.

こうした溶融設備における、溶融炉の制御手法に関して、例えば、廃棄物を黒鉛含有坩堝に収容し、前記黒鉛含有坩堝の外周に配設された誘導コイルによって前記廃棄物を誘導加熱してスラグ層と金属層に分離溶融する廃棄物溶融方法であって、前記黒鉛含有坩堝内の上部に位置するスラグ層が、前記黒鉛含有坩堝内の下部に位置する金属層よりも高温になるように前記誘導コイルの出力を制御して誘導加熱を行い、前記スラグ層の表面張力が小さくなるようにして溶融する廃棄物溶融方法(特許文献1参照)などが提案されている。   Regarding the control method of the melting furnace in such a melting facility, for example, waste is accommodated in a graphite-containing crucible, and the waste is induction-heated by an induction coil disposed on the outer periphery of the graphite-containing crucible, so that a slag layer and a metal A waste melting method of separating and melting into layers, wherein the induction coil has a higher temperature than a metal layer located in a lower part of the graphite-containing crucible in a slag layer located in the upper part of the graphite-containing crucible. A waste melting method (see Patent Document 1) that performs induction heating by controlling the output and melts the slag layer so as to reduce the surface tension has been proposed.

また、廃棄物溶融炉の炉下部側壁に複数段の監視口を設け、それぞれの監視口から、撮像器、輝度計、色彩計測器、赤外線センサーのうちの何れかにより炉内を監視し、画像の平均輝度、輝度、色度数、赤外線量、放射率のうちの何れかに基づいて、各段の監視口のレベルが廃棄物堆積層のレベルであるか、空間のレベルであるかを判定することにより、層高レベルを求めることを特徴とする廃棄物溶融炉内の層高レベル測定方法(特許文献2参照)なども提案されている。
特開2002−30354号公報 特開2003−121243号公報
In addition, a multi-stage monitoring port is provided on the bottom wall of the waste melting furnace, and the inside of the furnace is monitored from any of the monitoring ports by any one of an imager, luminance meter, color measuring device, and infrared sensor. Based on one of the average brightness, brightness, chromaticity, infrared amount, and emissivity of each, it is determined whether the level of the monitoring port of each stage is the level of the waste accumulation layer or the level of the space Thus, a method for measuring a layer height level in a waste melting furnace (see Patent Document 2) characterized by obtaining a layer height level has also been proposed.
JP 2002-30354 A JP 2003-121243 A

ところで溶融炉においては、溶融炉内の高周波誘導コイルに電圧を印加することにより磁界およびこれに起因するジュール熱を発生させてキャニスタ内の昇温を実現し、溶融対象物の溶融を行っている。この溶融は、予めキャニスタ内に投入された溶融対象物に対するものと、この溶融対象物の減容がなされた後に追加投入された溶融対象物に対するものとがある。   By the way, in a melting furnace, a voltage is applied to a high-frequency induction coil in the melting furnace to generate a magnetic field and Joule heat resulting from the magnetic field, thereby increasing the temperature in the canister and melting an object to be melted. . This melting includes a melting target object that has been input into the canister in advance and a melting target object that is additionally input after the volume of the melting target is reduced.

しかしながら、このようにキャニスタ内に投入される溶融対象物たる雑固体廃棄物が、所定量以上の金属粉または金属片などを含む場合、溶融過程において問題が生じやすかった。その問題とは、前記金属粉等の投入に起因してキャニスタ内に多量の酸化鉄が生成され、この多量の酸化鉄が一酸化炭素を発生させることに起因している。ここで発生した一酸化炭素は、キャニスタ内の溶湯中を液面つまり大気中に向かって上昇し、これに伴って溶湯レベル自体の急激な上昇を招来する惧れがあった。したがって、この溶湯レベルの上昇がキャニスタからの溶湯のふきこぼれにつながって、溶融炉の自動停止やその後の煩雑な復旧措置を余儀なくされていた。これにより雑固体廃棄物の減容処理効率が低下し、処理コストや手間の悪化を招くこととなっていた。   However, when the miscellaneous solid waste, which is an object to be melted, put into the canister in this way contains a predetermined amount or more of metal powder or metal pieces, problems are likely to occur in the melting process. The problem is caused by the fact that a large amount of iron oxide is generated in the canister due to the introduction of the metal powder and the like, and this large amount of iron oxide generates carbon monoxide. The carbon monoxide generated here rises in the molten metal in the canister toward the liquid surface, that is, in the atmosphere, and there is a concern that the molten metal itself may be rapidly increased. Therefore, this rise in the molten metal level led to the spilling of molten metal from the canister, which forced the automatic shutdown of the melting furnace and subsequent complicated recovery measures. As a result, the volume reduction processing efficiency of miscellaneous solid waste is reduced, leading to deterioration in processing costs and labor.

そこで本発明は上記課題を鑑みてなされたものであり、金属粉等に配慮した、雑固体廃棄物の効率よい溶融管理を可能とする、溶湯レベル管理方法および溶湯レベル管理システムを提供することを主たる目的とする。   Accordingly, the present invention has been made in view of the above problems, and provides a molten metal level management method and a molten metal level management system that enables efficient melting management of miscellaneous solid waste in consideration of metal powder and the like. Main purpose.

上記課題を解決する本発明の溶湯レベル管理方法は、低レベル放射性廃棄物の減容設備における溶湯レベルの管理方法であって、溶湯レベルの上昇抑制用のホウ砂を、珪砂の投入量より多く、前記減容設備が備える溶融炉内の溶湯に投入することを特徴とする(第1の発明)。   The molten metal level management method of the present invention that solves the above problems is a molten metal level management method in a low-level radioactive waste volume reduction facility, wherein the amount of borax for suppressing an increase in molten metal level is greater than the amount of silica sand input. The molten metal is introduced into the molten metal in the melting furnace provided in the volume reduction equipment (first invention).

第2の発明は、第1の発明において、低レベル放射性廃棄物の減容設備における溶湯レベルの管理方法であって、前記減容設備が備える溶融炉内の溶湯に投入する、溶湯レベルの上昇抑制用のホウ砂および珪砂の重量比を1:1とすることを特徴とする。   A second invention is a method for managing a melt level in a volume reduction facility for low-level radioactive waste according to the first invention, wherein the rise in the melt level is charged into a melt in a melting furnace provided in the volume reduction facility. The weight ratio of borax and quartz sand for suppression is 1: 1.

第3の発明は、第1または第2の発明において、溶融炉毎の前記ホウ砂の投入重量を1kgとし、溶融炉毎の前記珪砂の投入重量を1kgとすることを特徴とする。   A third invention is characterized in that, in the first or second invention, an input weight of the borax for each melting furnace is 1 kg, and an input weight of the silica sand for each melting furnace is 1 kg.

第4の発明は、第1〜第3のいずれかの発明において、前記減容設備が備える溶融炉内における溶湯レベルを検知する溶湯レベル検知手順と、前記検知した溶湯レベルが所定範囲以上に上昇しているか判定するレベル判定手順と、前記判定により前記溶湯レベルが所定範囲以上に上昇していると判定された場合に前記ホウ砂および珪砂を溶融炉内の溶湯へ投入する添加剤投入手順と、を含むことを特徴とする。   According to a fourth invention, in any one of the first to third inventions, a molten metal level detection procedure for detecting a molten metal level in a melting furnace provided in the volume reduction facility, and the detected molten metal level rises to a predetermined range or more. A level determination procedure for determining whether the molten metal level has risen to a predetermined range or more by the determination, and an additive charging procedure for charging the borax and quartz sand into the molten metal in the melting furnace. , Including.

第5の発明は、第1〜第4のいずれかの発明において、低レベル放射性廃棄物中より所定量以上の金属粉または金属片を選別し、この金属粉または金属片を前記溶融炉における溶融対象から除外する、金属粉等除外手順を含むことを特徴とする。   According to a fifth invention, in any one of the first to fourth inventions, a predetermined amount or more of metal powder or metal pieces is selected from low-level radioactive waste, and the metal powder or metal pieces are melted in the melting furnace. It includes a procedure for excluding metal powder, etc., which is excluded from the target.

第6の発明は、低レベル放射性廃棄物の減容設備における溶湯レベルの管理システムであって、前記減容設備が備える溶融炉内における溶湯レベルを検知する溶湯レベル検知手段と、前記検知した溶湯レベルが所定範囲以上に上昇しているか判定するレベル判定手段と、前記判定により前記溶湯レベルが所定範囲以上に上昇していると判定された場合に前記ホウ砂および珪砂を溶融炉内の溶湯へ投入する添加剤投入手段と、を含むことを特徴とする。   A sixth aspect of the invention is a molten metal level management system in a low-level radioactive waste volume reduction facility, wherein the molten metal level detection means detects the level of the molten metal in the melting furnace provided in the volume reduction facility, and the detected molten metal. Level determining means for determining whether the level has risen above a predetermined range, and when the determination determines that the molten metal level has risen above a predetermined range, the borax and quartz sand are transferred to the molten metal in the melting furnace. And an additive charging means to be charged.

第7の発明は、第6の発明において、低レベル放射性廃棄物中より所定量以上の金属粉または金属片を選別し、この金属粉または金属片を前記溶融炉における溶融対象から除外する、金属粉等除外手段を含むことを特徴とする。   A seventh invention is the metal according to the sixth invention, wherein a metal powder or a metal piece of a predetermined amount or more is selected from the low-level radioactive waste, and the metal powder or the metal piece is excluded from the melting object in the melting furnace. It includes an exclusion means such as powder.

その他、本願が開示する課題、及びその解決方法は、発明の実施の形態の欄、及び図面により明らかにされる。   In addition, the problems disclosed by the present application and the solutions thereof will be clarified by the embodiments of the present invention and the drawings.

本発明によれば、金属粉等に配慮した、雑固体廃棄物の効率よい溶融管理が可能となる。   According to the present invention, efficient melting management of miscellaneous solid waste in consideration of metal powder and the like becomes possible.

以下に本発明の実施形態について図面を用いて詳細に説明する。図1は本発明が適用される放射性廃棄物処理設備の全体構成を示す説明図である。先に本出願人は、図1に示す雑固体廃棄物の減容設備300を開発し、現在実用に供している。本実施形態においては、この雑固体廃棄物の減容設備300において本発明の雑固体廃棄物の溶湯レベル管理システムを実現すると同時に、雑固体廃棄物の溶湯レベル管理方法を行う状況を想定する。   Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is an explanatory diagram showing the overall configuration of a radioactive waste treatment facility to which the present invention is applied. Previously, the present applicant has developed a volume reduction facility 300 for miscellaneous solid waste shown in FIG. In the present embodiment, it is assumed that the miscellaneous solid waste volume reduction system 300 implements the miscellaneous solid waste melt level management system of the present invention and at the same time performs the miscellaneous solid waste melt level management method.

この雑固体廃棄物の減容設備300は、雑固体廃棄物を仕分する前処理設備1と、仕分された雑固体廃棄物のうち溶融可能な廃棄物を溶融するための溶融設備2と、溶融終了後の溶融廃棄物を収納したドラム缶に、モルタルを充填して充填固化体とするモルタル固化設備3と、充填固化体を一時保管する保管設備4とからなる。   The miscellaneous solid waste volume reduction facility 300 includes a pretreatment facility 1 for sorting miscellaneous solid waste, a melting facility 2 for melting fusible waste among the sorted miscellaneous solid waste, It consists of a mortar solidification facility 3 in which a drum can containing molten waste after completion is filled with mortar to obtain a solidified solid body, and a storage facility 4 for temporarily storing the solidified solidified body.

前処理設備1は、原子力発電施設にて発生する、性状(材質、寸法、形状等)の異なる雑固体廃棄物5を、処理対象外廃棄物6、直接充填物7、溶融対象物8に分別する仕分け台9を備える。   The pretreatment facility 1 separates miscellaneous solid wastes 5 having different properties (materials, dimensions, shapes, etc.) generated at nuclear power generation facilities into wastes 6 not to be treated, direct fillers 7 and melted objects 8 A sorting table 9 is provided.

また、溶融対象物8を溶融し易い大きさに切断する切断機10と、溶融対象物8を投入容器11、キャニスタ12のそれぞれに収納する収納手段13と、投入容器11及びキャニスタ12を溶融設備2に搬出する搬出手段14と、直接充填物7が充填されたドラム缶15をモルタル固化設備3に搬出する搬出手段16とを備える。   Moreover, the cutting machine 10 which cut | disconnects the to-be-melted object 8 in the magnitude | size which is easy to fuse | melt, the storage means 13 which accommodates the to-be-melted object 8 in the charging container 11 and the canister 12, respectively, and the charging container 11 and the canister 12 are melting equipment. 2 and an unloading means 16 for unloading the drum 15 filled directly with the filler 7 to the mortar solidification facility 3.

前記仕分け台9は、原子力発電施設から送られてくる雑固体廃棄物5を受けつけて回転するターンテーブル等の回転部17と、回転部17を支持する固定部18とを備える。この仕分け台9における雑固体廃棄物5の分別作業は、前記回転部17を囲むように配置された複数人員の手作業により実施するとしてもよい。雑固体廃棄物5を例えば、処理対象外廃棄物6、直接充填物7、溶融対象物8の3区分に分別することとなる。   The sorting table 9 includes a rotating unit 17 such as a turntable that receives and rotates the miscellaneous solid waste 5 sent from the nuclear power generation facility, and a fixed unit 18 that supports the rotating unit 17. The sorting work of the miscellaneous solid waste 5 in the sorting table 9 may be performed by manual work of a plurality of personnel arranged so as to surround the rotating unit 17. The miscellaneous solid waste 5 is classified into, for example, three categories of non-processing target waste 6, direct filling 7, and melting target 8.

この仕分け台9は、本発明における、低レベル放射性廃棄物中より所定量以上の金属粉または金属片を選別し、この金属粉または金属片を前記溶融炉21における溶融対象から除外する金属粉除外手段となる。そのため、例えば、所定量以上の金属粉または金属片に特有の性状や形態を識別する適宜なセンサや機構を備えて、前記雑固体廃棄物中より、所定量以上の金属粉または金属片を含む雑固体廃棄物を選別・除外するものとすれば好適である。   The sorting table 9 selects a predetermined amount or more of metal powder or metal pieces from the low-level radioactive waste in the present invention, and excludes the metal powder or metal pieces from the melting object in the melting furnace 21. It becomes a means. Therefore, for example, an appropriate sensor or mechanism for identifying a characteristic or form peculiar to a predetermined amount or more of metal powder or metal piece is provided, and the predetermined amount or more of metal powder or metal piece is included in the miscellaneous solid waste. It is preferable to sort and exclude miscellaneous solid waste.

前記処理対象外廃棄物6は、例えば、鉛等の有害物及び可燃物であり、有害物は貯蔵所に搬出され、可燃物は別途焼却施設にて焼却処理される。   The non-processable waste 6 is, for example, harmful substances such as lead and flammable substances. The toxic substances are carried out to a storage, and the flammable substances are incinerated separately in an incineration facility.

一方、直接充填物7は、溶融することにより溶融設備2に好ましくない影響を与える、例えば、塩化ビニル類、ゴム類等の難燃性の廃棄物及び真鍮等の非鉄金属類である。この直接充填物8は、例えば手作業にてそのままドラム缶15に充填され、移動台車又はクレーン等の搬出手段16にてモルタル固化設備3に搬出される。   On the other hand, the direct filler 7 is a non-ferrous metal such as brass and flame retardant waste such as vinyl chlorides and rubbers, which adversely affect the melting equipment 2 by melting. The direct filling 8 is filled in the drum can 15 as it is, for example, manually, and is carried out to the mortar solidification facility 3 by the carrying-out means 16 such as a movable carriage or a crane.

また、溶融対象物8は、溶融により減容化がはかれる、例えば、炭素鋼、ステンレス等の金属類、コンクリート、保温材、ガラスの無機物類の不燃物である。この溶融対象物8のうち、大型の雑固体廃棄物や異形の雑固体廃棄物は、投入容器11又はキャニスタ12に入る大きさに切断機10にて切断される。こられの溶融対象物8は、手作業又はコンベア等の収納手段13により投入容器11又はキャニスタ12に収納され、クレーン又はコンベア等の搬出手段14により溶融設備2へ搬出される。   Further, the object to be melted 8 is an incombustible material such as metals such as carbon steel and stainless steel, concrete, heat insulating material, and glass inorganic materials whose volume can be reduced by melting. Of the melted object 8, large miscellaneous solid waste or irregularly shaped miscellaneous solid waste is cut by the cutting machine 10 into a size that can enter the input container 11 or the canister 12. These melting objects 8 are stored in the charging container 11 or the canister 12 by storage means 13 such as a manual operation or a conveyor, and are transported to the melting facility 2 by the transporting means 14 such as a crane or a conveyor.

他方、前記溶融設備2は、略円筒形状であって、内側表面の下部に高周波誘導コイル20が螺旋状に巻回されている溶融炉21を有する。また、この溶融炉21の下部側から初期装荷として予め溶融対象物8を詰め込んだキャニスタ12を上昇させて高周波誘導コイル20の内側に装填し、溶融終了後はキャニスタ12を下降させ、冷却装置22まで移動させる移動装置23を備える。   On the other hand, the melting equipment 2 has a substantially cylindrical shape, and has a melting furnace 21 around which a high-frequency induction coil 20 is spirally wound. Further, from the lower side of the melting furnace 21, the canister 12 previously packed with the object 8 to be melted is lifted and loaded inside the high-frequency induction coil 20. After the melting is finished, the canister 12 is lowered and the cooling device 22. A moving device 23 is provided.

更に、前記溶融設備2は、初期装荷した溶融対象物8が溶融し減容することで生じたキャニスタ12内の余裕空間に、溶融炉21の上部側から投入容器11を降下させ、当該投入容器11下部のゲートを開けることでキャニスタ12内に溶融対象物8を投入する投入装置24を備える。   Further, the melting facility 2 lowers the charging container 11 from the upper side of the melting furnace 21 into a marginal space in the canister 12 generated by melting and reducing the volume of the initially loaded melting target object 8. 11 is provided with a charging device 24 for charging the melted object 8 into the canister 12 by opening the gate at the bottom.

また、キャニスタ12内部の溶融状況を常時監視する監視カメラ25と、溶融炉21から発生する排気を排出する煙道26と、排気中の粉塵を濾過するフィルター27と、排気を吸引する排ガスブロワと、排ガスブロワにより吸引した排気を無害化する排気処理装置29とを備える。なお、前記監視カメラ25は、本発明における、前記溶融炉21内における溶湯レベルを検知する溶湯レベル検知手段となる。   In addition, a monitoring camera 25 that constantly monitors the melting state inside the canister 12, a flue 26 that discharges the exhaust generated from the melting furnace 21, a filter 27 that filters dust in the exhaust, and an exhaust gas blower that sucks the exhaust And an exhaust treatment device 29 for detoxifying the exhaust sucked by the exhaust gas blower. The monitoring camera 25 serves as a molten metal level detecting means for detecting the molten metal level in the melting furnace 21 in the present invention.

また、キャニスタ12の炉内への装荷や炉外への取り出し等、キャニスタ12のハンドリングを容易にするため、また、キャニスタ12の外表面温度の測定のため、溶融炉21の内壁とキャニスタ12との間には空隙を持たせている。   Further, in order to facilitate handling of the canister 12 such as loading the canister 12 into the furnace and taking it out of the furnace, and for measuring the outer surface temperature of the canister 12, the inner wall of the melting furnace 21 and the canister 12 There is a gap between them.

このような溶融設備2においては、溶融炉21内の高周波誘導コイル20に電圧を印加することにより磁界が発生し、ジュール熱を生ずることでキャニスタ12の内部を1500℃程度に昇温させ、溶融対象物8を溶融させる。そして、キャニスタ内に余裕ができると投入容器11内の溶融対象物8を順次キャニスタ12内に追加投入しながら溶融させ、所定の溶湯レベルに至るまで追加投入を継続する。溶湯レベル及び溶融状態は、キャニスタ12内部が見渡せる溶融炉21の上部付近に設けられた前記監視カメラ25によって常時監視されている。   In such a melting facility 2, a magnetic field is generated by applying a voltage to the high-frequency induction coil 20 in the melting furnace 21, and Joule heat is generated to raise the temperature inside the canister 12 to about 1500 ° C. The object 8 is melted. When there is room in the canister, the melting object 8 in the charging container 11 is melted while being sequentially added into the canister 12, and the additional charging is continued until a predetermined molten metal level is reached. The molten metal level and the molten state are constantly monitored by the monitoring camera 25 provided near the upper portion of the melting furnace 21 overlooking the inside of the canister 12.

さらに、溶融炉21の上部付近には、排気排出用の煙道26が開口されており、この煙道26には煙道配管30が接続されている。また、この煙道配管30はフィルタ27を介して排気処理装置29に接続されている。排ガスブロアの吸引動作により溶融炉内は負圧に常時保たれ、排気の外部拡散を防止している。また、排気については、フィルタ27で濾過を行って排気中の粉塵を除去した後、排気処理装置29を通過させて無害化し、大気中に放出される。   Further, a flue 26 for exhaust discharge is opened near the upper portion of the melting furnace 21, and a flue pipe 30 is connected to the flue 26. The flue pipe 30 is connected to an exhaust treatment device 29 through a filter 27. Due to the suction operation of the exhaust gas blower, the inside of the melting furnace is always kept at a negative pressure to prevent external diffusion of the exhaust gas. Further, the exhaust gas is filtered by the filter 27 to remove dust in the exhaust gas, and then passed through the exhaust treatment device 29 to be harmless and discharged into the atmosphere.

キャニスタ12において溶融終了後の溶融廃棄物31は、キャニスタ移動装置23にてキャニスタ12ごと溶融炉21から取り出され、冷却装置22まで搬送される。また、この冷却装置22にて外気等で所定温度まで冷却された溶融廃棄物31は、キャニスタ12ごとドラム缶32内に収容されることとなる。   The molten waste 31 after the end of melting in the canister 12 is taken out of the melting furnace 21 together with the canister 12 by the canister moving device 23, and is conveyed to the cooling device 22. Further, the molten waste 31 cooled to the predetermined temperature by the outside air or the like in the cooling device 22 is accommodated in the drum can 32 together with the canister 12.

図2は本実施形態における雑固体廃棄物の溶湯レベル管理システムを含む溶融設備概要図である。本実施形態における前記溶融設備2は、図2に示すように、前記減容設備300が備える溶融炉21内における溶湯レベルを検知する溶湯レベル検知手段25(例:監視カメラ)と、前記検知した溶湯レベルが所定範囲以上に上昇しているか判定するレベル判定手段201と、前記判定により前記溶湯レベルが所定範囲以上に上昇していると判定された場合にホウ砂および珪砂を溶融炉内の溶湯へ投入する添加剤投入手段202とからなる溶湯レベル管理システム200を備える。   FIG. 2 is a schematic diagram of a melting facility including a melt level management system for miscellaneous solid waste in the present embodiment. As shown in FIG. 2, the melting facility 2 in the present embodiment includes a molten metal level detection means 25 (e.g., a monitoring camera) that detects a molten metal level in the melting furnace 21 provided in the volume reduction facility 300, and the detection. Level determination means 201 for determining whether or not the molten metal level has risen above a predetermined range, and when it is determined by the determination that the molten metal level has risen above the predetermined range, borax and quartz sand are removed from the molten metal in the melting furnace. A molten metal level management system 200 comprising an additive charging means 202 for charging into the battery is provided.

溶湯レベル管理システム200は、溶融設備2に備わるコンピュータであり、前記溶湯レベル検知手段25からの溶湯レベル情報を取得する一方で、この溶湯レベル情報と自身が備えるメモリに格納された溶湯レベルの許容上昇範囲とを比較する。この比較により、現在の溶融炉21つまりキャニスタ12における溶湯レベルが所定範囲以上に上昇しているか否か判定することとなる。この判定結果が前記所定範囲以上との旨であれば、ホウ砂および珪砂の溶湯投入指示を生成し、これを前記添加剤投入手段202に通知するのである。   The molten metal level management system 200 is a computer provided in the melting facility 2 and acquires molten metal level information from the molten metal level detecting means 25. On the other hand, the molten metal level information and the allowance of the molten metal level stored in its own memory are obtained. Compare with rising range. From this comparison, it is determined whether or not the melt level in the current melting furnace 21, that is, the canister 12, has risen above a predetermined range. If the determination result is equal to or greater than the predetermined range, an instruction for adding molten borax and silica sand is generated and notified to the additive charging means 202.

ここで、前記ホウ砂は、溶湯内にあって溶湯自体の粘性を抑制することで溶湯レベルの流動性を確保することが可能なものである。一方、珪砂は、溶湯内にあって生成された前記酸化鉄に起因する一酸化炭素発生を抑制可能なものである。したがって本発明は、ホウ砂により溶湯の粘性を抑制して流動性を高めると共に、溶湯内を液面つまり大気に向かって上昇して溶湯自体のレベル上昇を招来する一酸化炭素の発生を珪素により抑制し、溶湯の粘性および一酸化炭素の両面から溶湯レベル上昇という課題にアプローチしたものである。   Here, the borax is in the molten metal, and it is possible to ensure fluidity at the molten metal level by suppressing the viscosity of the molten metal itself. On the other hand, the silica sand can suppress the generation of carbon monoxide due to the iron oxide generated in the molten metal. Accordingly, the present invention suppresses the viscosity of the molten metal with borax to improve the fluidity, and also causes the generation of carbon monoxide that rises in the molten metal toward the liquid surface, that is, the atmosphere and causes the molten metal itself to increase in level. This is an approach to the problem of increasing the melt level from both sides of the viscosity and carbon monoxide.

また、前記溶融炉21内の溶湯に投入する、溶湯レベルの上昇抑制用のホウ砂および珪砂の重量比は、1:1とすることが好適である。或いは、溶融炉21(のキャニスタ12)毎の前記ホウ砂の投入重量を1kgとし、溶融炉21(のキャニスタ12)毎の前記珪砂の投入重量を1kgとすることとしてもよい。いずれにしても、従来は投入するホウ砂および珪砂の重量比が0.6:1であったから、ホウ砂の投入量を珪砂に比して従来より増大させ、溶湯の粘性により配慮したものとも言える。   Moreover, it is preferable that the weight ratio of the borax and the silica sand for suppressing the rise of the melt level to be introduced into the melt in the melting furnace 21 is 1: 1. Alternatively, the input weight of the borax for each melting furnace 21 (the canister 12) may be 1 kg, and the input weight of the silica sand for each melting furnace 21 (the canister 12) may be 1 kg. In any case, the weight ratio of borax and silica sand to be introduced was 0.6: 1 in the past, so the amount of borax input was increased compared to that of silica sand and the viscosity of the molten metal was considered. I can say that.

また、前記ホウ砂および珪砂としては、一例として、ホウ砂:Na2↓B4↓O7↓10H2↓、珪砂:フェロシリコン、を想定できるが、その他の成分構成のホウ砂、珪砂であっても適用可能である。   As the borax and silica sand, for example, borax: Na2 ↓ B4 ↓ O7 ↓ 10H2 ↓ and quartz sand: ferrosilicon can be assumed, but borax and silica sand with other components are also applicable. It is.

なお、前記溶湯レベル検知手段25は、上述した監視カメラ25の例だけでなく、他の種々のレベル検知手段を採用することが可能である。また、前記添加剤投入手段202についても、キャニスタ12内の溶湯へホウ砂および珪砂を投入可能な装置であれば、キャニスタ12や溶融炉21の形態や構造などに応じて適宜採用するものとできる。   The molten metal level detection means 25 can adopt not only the example of the monitoring camera 25 described above but also various other level detection means. Also, the additive charging means 202 can be appropriately employed according to the form and structure of the canister 12 and the melting furnace 21 as long as it is an apparatus capable of charging borax and silica sand into the molten metal in the canister 12. .

図3は本実施形態における雑固体廃棄物の溶湯レベル管理方法の処理手順を示すフロー図である。次に、雑固体廃棄物の溶湯レベル管理方法の処理手順について説明する。まず、金属粉等除外手段たる仕分け台9において、低レベル放射性廃棄物中より所定量以上の金属粉または金属片について選別および除去を実行する(s1000)。ここで選別・除去された所定量以上の金属粉または金属片は、直接充填物7としてドラム缶15に充填され、搬出手段16によりモルタル固化設備3に搬出される。   FIG. 3 is a flowchart showing the processing procedure of the miscellaneous solid waste molten metal level management method in the present embodiment. Next, the processing procedure of the molten metal level management method for miscellaneous solid waste will be described. First, sorting and removal of a predetermined amount or more of metal powder or metal pieces from the low-level radioactive waste is performed in the sorting table 9 as a means for excluding metal powder or the like (s1000). A predetermined amount or more of the metal powder or metal piece selected and removed here is directly filled into the drum can 15 as the filling material 7 and is carried out to the mortar solidification facility 3 by the carrying-out means 16.

一方、前記溶融炉21内(のキャニスタ12)における溶湯レベルを、前記監視カメラ25などの溶湯レベル検知手段により検知する(s1001)。前記レベル判定手段201は、前記検知した溶湯レベルを所定の許容上昇範囲(所定範囲レベル)と比較し(s1002)、所定範囲以上であるか否か判定する(s1003)。この判定により、溶湯レベルが所定の範囲以下であった場合(s1003:NO)、処理をステップs1001に戻し、通常操業の状態を維持する。   On the other hand, the molten metal level in the melting furnace 21 (canister 12) is detected by a molten metal level detecting means such as the monitoring camera 25 (s1001). The level determination unit 201 compares the detected molten metal level with a predetermined allowable increase range (predetermined range level) (s1002), and determines whether or not it is greater than or equal to a predetermined range (s1003). If it is determined that the molten metal level is below the predetermined range (s1003: NO), the process returns to step s1001, and the normal operation state is maintained.

他方、前記溶湯レベルが所定範囲以上であると判定された場合に(s1003:YES)、前記レベル判定手段201より添加剤投入手段202に対し、前記ホウ砂および珪砂の溶湯へ投入処理の指示を行う。これを受けた添加剤投入手段202は、例えばキャニスタ12の溶湯液面に対向する位置に備えた開閉扉203を所定時間開放するなどして自身の添加剤格納容器204より所定量(例:ホウ砂と珪砂の重量比1:1、またはホウ砂1kg:珪砂1kg)のホウ砂および珪砂の投入処理を実行し(s1004)、本フローは終了する。このホウ砂および珪砂の溶湯投入処理によって、ホウ砂により溶湯の粘性を抑制して流動性を高めると共に、溶湯内を液面つまり大気に向かって上昇して溶湯自体のレベル上昇を招来する一酸化炭素の発生を珪素により抑制することとなる。   On the other hand, when it is determined that the molten metal level is equal to or higher than a predetermined range (s1003: YES), the level determining unit 201 instructs the additive charging unit 202 to perform a charging process on the molten borax and quartz sand. Do. In response to this, the additive charging means 202 opens a predetermined amount of the additive storage container 204 (e.g., hoof) by opening the open / close door 203 provided at a position facing the molten metal surface of the canister 12 for a predetermined time. The borax and silica sand are introduced at a weight ratio of 1: 1 sand to silica sand, or 1 kg of borax: 1 kg of silicate sand (s1004), and this flow ends. This borax and quartz sand molten metal charging process increases the fluidity by suppressing the viscosity of the molten metal with borax, and also raises the level of the molten metal itself by rising toward the liquid surface, that is, the atmosphere. The generation of carbon is suppressed by silicon.

本発明によれば、金属粉等に配慮した、雑固体廃棄物の効率よい溶融管理が可能となる。   According to the present invention, efficient melting management of miscellaneous solid waste in consideration of metal powder and the like becomes possible.

以上、本発明の実施の形態について、その実施の形態に基づき具体的に説明したが、これに限定されるものではなく、その要旨を逸脱しない範囲で種々変更可能である。   As mentioned above, although embodiment of this invention was described concretely based on the embodiment, it is not limited to this and can be variously changed in the range which does not deviate from the summary.

本発明が適用される放射性廃棄物処理設備の全体構成を示す説明図である。It is explanatory drawing which shows the whole structure of the radioactive waste processing equipment to which this invention is applied. 本実施形態における雑固体廃棄物の溶湯レベル管理システムを含む溶融設備概要図である。It is a melting facility schematic diagram including the molten metal level management system for miscellaneous solid waste in this embodiment. 本実施形態における溶湯レベル管理方法の処理手順を示すフロー図である。It is a flowchart which shows the process sequence of the molten metal level management method in this embodiment.

符号の説明Explanation of symbols

1 前処理設備 2 溶融設備
3 モルタル固化設備 4 保管設備
5 雑固体廃棄物 6 処理対象外廃棄物
7 直接充填物 8 溶融対象物
9 仕分け台、金属粉除外手段 10 切断機
11 投入容器 12 キャニスタ
13 収納手段 14、16 搬出手段
15、32 ドラム缶 17 回転部
18 固定部 20 高周波誘導コイル
21 溶融炉 22 冷却装置
23 移動装置 24 投入装置
25 監視カメラ、溶湯レベル検知手段 26 煙道
27 フィルター 29 排気処理装置
30 煙道配管 31 溶融廃棄物
33 固形化材サイロ 34 固形化材投入機
35 練り混ぜ機 36 ホッパ
37 充填固化体
200 溶湯レベル管理システム 201 レベル判定手段
202 添加剤投入手段 203 開閉扉
204 添加剤格納容器 300 雑固体廃棄物溶融設備
DESCRIPTION OF SYMBOLS 1 Pretreatment equipment 2 Melting equipment 3 Mortar solidification equipment 4 Storage equipment 5 Miscellaneous solid waste 6 Unprocessed waste 7 Direct filling 8 Melting object 9 Sorting table, metal powder exclusion means 10 Cutting machine 11 Input container 12 Canister 13 Storage means 14, 16 Unloading means 15, 32 Drum can 17 Rotating part 18 Fixed part 20 High-frequency induction coil 21 Melting furnace 22 Cooling device 23 Moving device 24 Input device 25 Monitoring camera, molten metal level detecting means 26 Flue 27 Filter 29 Exhaust treatment device 30 Flue pipe 31 Molten waste 33 Solidified material silo 34 Solidified material charging machine 35 Kneader 36 Hopper 37 Filled solidified body 200 Molten metal level control system 201 Level judgment means 202 Additive charging means 203 Opening / closing door 204 Additive storage Container 300 Miscellaneous solid waste melting equipment

Claims (7)

低レベル放射性廃棄物の減容設備における溶湯レベルの管理方法であって、溶湯レベルの上昇抑制用のホウ砂を、珪砂の投入量より多く、前記減容設備が備える溶融炉内の溶湯に投入することを特徴とする溶湯レベル管理方法。   A method for managing the level of molten metal in a volume reduction facility for low-level radioactive waste, wherein the amount of borax for suppressing the rise in the level of molten metal is greater than the amount of silica sand, and is introduced into the molten metal in the melting furnace provided in the volume reduction facility. A molten metal level management method characterized by: 請求項1において、低レベル放射性廃棄物の減容設備における溶湯レベルの管理方法であって、前記減容設備が備える溶融炉内の溶湯に投入する、溶湯レベルの上昇抑制用のホウ砂および珪砂の重量比を1:1とすることを特徴とする溶湯レベル管理方法。   2. The method for managing a molten metal level in a low-volume radioactive waste volume reduction facility according to claim 1, wherein the borax and silica sand are used to suppress an increase in the molten metal level and are introduced into the molten metal in the melting furnace provided in the volume reduction facility. The molten metal level management method, wherein the weight ratio is 1: 1. 請求項1または2において、溶融炉毎の前記ホウ砂の投入重量を1kgとし、溶融炉毎の前記珪砂の投入重量を1kgとすることを特徴とする溶湯レベル管理方法。   The molten metal level management method according to claim 1 or 2, wherein an input weight of the borax for each melting furnace is 1 kg, and an input weight of the silica sand for each melting furnace is 1 kg. 請求項1〜3のいずれかにおいて、前記減容設備が備える溶融炉内における溶湯レベルを検知する溶湯レベル検知手順と、前記検知した溶湯レベルが所定範囲以上に上昇しているか判定するレベル判定手順と、前記判定により前記溶湯レベルが所定範囲以上に上昇していると判定された場合に前記ホウ砂および珪砂を溶融炉内の溶湯へ投入する添加剤投入手順と、を含むことを特徴とする溶湯レベル管理方法。   In any one of Claims 1-3, the molten metal level detection procedure which detects the molten metal level in the melting furnace with which the said volume reduction equipment is provided, and the level determination procedure which determines whether the detected molten metal level is rising beyond the predetermined range And an additive charging procedure for charging the borax and silica sand into the molten metal in the melting furnace when it is determined by the determination that the molten metal level has risen above a predetermined range. Melt level management method. 請求項1〜4のいずれかにおいて、低レベル放射性廃棄物中より所定量以上の金属粉または金属片を選別し、この金属粉または金属片を前記溶融炉における溶融対象から除外する、金属粉等除外手順を含むことを特徴とする溶湯レベル管理方法。   In any one of Claims 1-4, the metal powder etc. which sort out the metal powder or metal piece more than predetermined amount from the low level radioactive waste, and exclude this metal powder or metal piece from the melting object in the said melting furnace A molten metal level management method comprising an exclusion procedure. 低レベル放射性廃棄物の減容設備における溶湯レベルの管理システムであって、前記減容設備が備える溶融炉内における溶湯レベルを検知する溶湯レベル検知手段と、前記検知した溶湯レベルが所定範囲以上に上昇しているか判定するレベル判定手段と、前記判定により前記溶湯レベルが所定範囲以上に上昇していると判定された場合に前記ホウ砂および珪砂を溶融炉内の溶湯へ投入する添加剤投入手段と、を含むことを特徴とする溶湯レベル管理システム。   A melt level management system in a low-level radioactive waste volume reduction facility, wherein the melt level detection means detects a melt level in a melting furnace provided in the volume reduction facility, and the detected melt level exceeds a predetermined range. Level determining means for determining whether or not it has risen, and additive charging means for charging the borax and silica sand into the molten metal in the melting furnace when it is determined by the determination that the molten metal level has risen above a predetermined range And a molten metal level management system. 請求項6において、低レベル放射性廃棄物中より所定量以上の金属粉または金属片を選別し、この金属粉または金属片を前記溶融炉における溶融対象から除外する、金属粉等除外手段を含むことを特徴とする溶湯レベル管理システム。
The metal powder or the like is excluded from the melting object in the melting furnace according to claim 6, including a predetermined amount or more of the metal powder or the metal piece from the low-level radioactive waste. A molten metal level management system.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010179239A (en) * 2009-02-05 2010-08-19 Nippon Steel Engineering Co Ltd Pretreatment method and pretreatment equipment in plasma melting decomposition treatment of material to be treated
US8983561B2 (en) 2010-09-14 2015-03-17 Denso Corporation In-vehicle apparatus

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JPS61178699A (en) * 1985-02-05 1986-08-11 明星工業株式会社 Volune reducing method of radioactive waste
JP2004294308A (en) * 2003-03-27 2004-10-21 Ngk Insulators Ltd Melting processing method of miscellaneous solid waste

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61178699A (en) * 1985-02-05 1986-08-11 明星工業株式会社 Volune reducing method of radioactive waste
JP2004294308A (en) * 2003-03-27 2004-10-21 Ngk Insulators Ltd Melting processing method of miscellaneous solid waste

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010179239A (en) * 2009-02-05 2010-08-19 Nippon Steel Engineering Co Ltd Pretreatment method and pretreatment equipment in plasma melting decomposition treatment of material to be treated
US8983561B2 (en) 2010-09-14 2015-03-17 Denso Corporation In-vehicle apparatus

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