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JP3839121B2 - Cleaning and dismantling method for alkali metal contaminants - Google Patents
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JP3839121B2 - Cleaning and dismantling method for alkali metal contaminants - Google Patents

Cleaning and dismantling method for alkali metal contaminants Download PDF

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Publication number
JP3839121B2
JP3839121B2 JP05834397A JP5834397A JP3839121B2 JP 3839121 B2 JP3839121 B2 JP 3839121B2 JP 05834397 A JP05834397 A JP 05834397A JP 5834397 A JP5834397 A JP 5834397A JP 3839121 B2 JP3839121 B2 JP 3839121B2
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Prior art keywords
alkali metal
air
cleaning
gas
container
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JPH10238141A (en
Inventor
稔 佐藤
六男 坂本
文男 金箱
昇三 藤岡
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東興機械工業株式会社
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Description

【0001】
【発明の属する技術分野】
本発明はアルカリ金属汚染体、特にナトリウムが内部に付着残留したタンク、容器、機器の廃棄処分に先立っての洗浄解体方法に関する。
【0002】
【従来の技術】
従来、上記したアルカリ金属汚染容器、機器の洗浄、解体方法としては図2として示す水蒸気による洗浄や図3として示すアルコールによる洗浄が一般的に知られている。
【0003】
アルカリ金属は化学的活性度が高く、水やアルコール等の洗浄剤と反応し、水素ガスを放出して化学的に不活性化される。即ち、ナトリウムの場合、水と反応して水酸化ナトリウムとなり、アルコールと反応してエトキシル化する。この場合に、処理せんとする容器、機器内が空気で満たされていると、前記した放出された水素ガスと、特に空気中の酸素が反応して爆発を生ずる危険性を有している。
【0004】
図2として示す水蒸気による洗浄方法を説明すると、この図2にあって、1は内部にナトリウムNが付着残留している容器である。この容器1内に窒素ガス等の不活性ガスをガスタンク2より送り込んで内部を置換して満たし、水蒸気発生機3から水蒸気を注入することでナトリウムNを水酸化ナトリウムN´に変えることで、そのナトリウムNの不活性化を図るものとしている。なお、図2にあって4は排水タンク、5は途中にフレームアレスター(逆火防止装置)6を介在させた排気系である。
【0005】
また、図3として示すのはアルコールによる洗浄方法であり、図2と共通する部分は同一の符号を付して詳しい説明は省略する。この場合、ガスタンク2から窒素ガス等の不活性ガスを容器1内に満たし、アルコールタンク7からポンプ8を介して容器1内にアルコール8を注入する。そして、このアルコール8は循環ポンプ9によって循環される。
【0006】
このようにしてアルカリ金属(ナトリウムN)を不活性化して、水素ガスの発生がなくなった後、ガス切断法等の機械的手段によって、この容器1を解体し、廃棄するものとされていた。
【0007】
【発明が解決しようとする課題】
しかしながら、上記した従来の方法によれば、水素ガスやアルコール、蒸気に起因する爆発の危険性を除去するために常時不活性ガスを注入する必要があること、不活性ガスの連続注入装置、水蒸気やアルコール等の洗浄剤の注入装置等々多くの附帯的な装置が必要となり、操作も煩雑なものとなり、作業実施コストを含めて要する費用も嵩んでしまうものとなっている。
【0008】
【発明の目的】
そこで、本発明は係る従来の技術の実情、問題点に着目して、かかる問題点を解消して、より一層確実な安全性が得られ、かつ、設備や作業に要する費用を節減して低廉なもので済むこととしたアルカリ金属汚染体の洗浄解体方法を提供することを目的としている。
【0009】
【課題を解決するための手段】
この目的を達成するために、本発明に係るアルカリ金属汚染体の洗浄解体方法は存在するアルカリ金属の少なくとも表面を砂層で覆い、次いで含湿空気を導入して換気を行ない、水素濃度を薄めるとともに前記アルカリ金属を反応させて不活性化し、その不活性化が完了して水素の発生がなくなった時点で空気雰囲気において機械的解体作業をなすことを特徴とし、前記した含湿空気の湿分が少ない場合、補助的に微量の水を注入することを特徴とし、水素濃度が顕著な値となった場合、前記した含湿空気の導入を止め、アルゴンガス、窒素ガス等の不活性ガスを注入しつつ排気し、水素濃度を低下させることを特徴とし、作業時間の終了に伴い、含湿空気の導入を止め、アルゴンガス、窒素ガス等の不活性ガスを注入して空気の置換をなし、空気、ガスの導入口、排出口を閉塞して空気の侵入を防止しておくことを特徴としている。
【0010】
【作用】
かかる構成としたことにより、従来必要とされていた窒素ガス等の不活性ガスの連続注入装置や水蒸気やアルコール等の洗浄剤の注入装置が不要となり、設備、作業の面で大幅な費用の節減が図れ、しかも砂層を設けることで下記のようにより一層の確実な安全性が得られる。
【0011】
即ち、砂層でアルカリ金属の少なくとも表面を覆うことで、目的とする容器、機器の内部局部に予想される滞留水分や、微量な水を注入した際のその水の流入等に起因して予期せぬ過反応が生じ、水素ガスが一時に大量に発生したとしても、爆発性の水素ガスと、水と反応して発熱し、高温となっているアルカリ金属とが隔離されることとなり、着火源となることを防止できる。
【0012】
また、砂層内に含まれる爆発性の水素ガスが高温となっているアルカリ金属の表面で爆発を開始したとしても、その爆発火炎が砂層内を通過することで冷却され消炎されてしまい、砂層外部の大量に存する爆発性ガスには火炎が到達することがなく、砂層内における小さな爆発のみで消滅してしまうことになる。
【0013】
さらに、砂層を大量の水が通過する場合、砂の有する保水、拡散の作用によって水の流出側にあっては流路面積が広くなり、加えて水の流れのピークは均されて平坦となる。そのために、通過水が一時に集中してアルカリ金属と反応することが防げ、大量の水素ガスの発生や着火源となる反応アルカリ金属の高温化も抑えることができる。
【0014】
【発明の実施の形態】
次に、本発明の実施の形態を図1を参照して説明する。図1は本発明を実施したナトリウム汚染容器の洗浄方法を示す図である。
【0015】
この図1にあって10は内部にナトリウムNが付着残留した容器を示している。この図1にあってはナトリウム10の少なくとも表面は砂層11により覆われており、容器1の入口水平配管からブロワー12によって湿気を含む外気を大量に容器10内へ送気する。なお、この実施の形態にあってはブロワー12を利用した送気としたが、必要に応じファンその他の手段を用いて外気を吸気させることもできる。
【0016】
また、図中、想像線で示す13は微量の水の注水装置であり、ポンプ14により容器10内への注水がなされるが、この注水装置13は冬期等、大気が乾燥し、湿度が少ない場合に補助的に使用されることになる。なお、図中15は排気系を示している。
【0017】
ここで、この図1に基づいて具体的な実施例を説明すると、容器10としては、内部に特に図示しない複雑な構造物を有する直径3m、高さ8mの円筒状のものとし、ナトリウムN(一部は水酸化ナトリウム)は約2t存在するものであり、容器10の下部胴に複数(4ケ所)の透孔を穿ち、乾燥砂を投入して砂層11とした。この砂層11の厚さは約30cmであった。
【0018】
次いで、ブロワー12によって外気を大量(より具体的には送気量50m3/分、大気温度摂氏30度、湿度80%では1、169Kgw/分の水が注入され、1日5時間の送気で4日間行なうと1403Kgwの水が注入されることになる)に送気した。また、容器10内の反応状況を監視するため、容器10内の水素濃度を常時測定器により測定した。
【0019】
ブロワー12による送気開始直後から容器10の胴内壁面に付着していた反応生成物は潮解を始め、その潮解液と反応生成物は容器10の内壁面を流下し、砂層11の表面に至り、潮解液はこの砂層11内に吸収されていき、反応生成物はこの砂層11の表面でさらに潮解していった。この過程は極めて穏やかになされた。
【0020】
砂層11で覆われている容器10の下部鏡板のナトリウムNは、砂層11内を伝い落ちる潮解液や、砂層11の表面の空気から拡散してくる湿気によって反応し、不活性化していった。この反応過程には、時折、砂層11内で鈍い爆発音を伴う比較的激しい反応が見られ、下部鏡板近傍の容器10の外壁に触れると、温度がやや上昇しているのが判った。
【0021】
容器10内の水素濃度が顕著な値となって爆発予防のための作業続行制限値を越えた場合、ブロワー12による送気を止め、アルゴンガスを注入しながら排気を行ない、反応の沈静化を待ち、水素濃度が低下すると、再びブロワー12による送気を行なった。
【0022】
一日の作業時間(前記した5時間)が終了すると、送気を止め、容器10内にアルゴンガスを注入して容器10内の空気を置換し、その状態で送気口、排気口をめくら板で閉塞遮断し、外気が容器10内に侵入するのを防ぎ、放置した。
【0023】
上記の作業過程を繰り返し、1週間後に、送気しても水素濃度の上昇が観察されなくなった時点で不活性化は完了したと判断して解体作業に移行した。
【0024】
容器10の解体はガス切断により行なった。容器10の胴部の上部鏡板近傍及び下部鏡板近傍の2箇所を切断し、上部及び中間部は散水して残った反応生成物を洗い落とし、下部鏡板部分はスコップで砂を取り除き、ガス切断機によって解体しながら、付着した反応生成物を掻き取り、水で洗浄処理を行なった。
【0025】
以上の具体的な実施例では、非常に経済的にしかも大きな安全性を確保して作業を終了することができた。
【0026】
【発明の効果】
本発明に係るアルカリ金属汚染体の洗浄解体方法は上述のように構成されている。そのため、より一層の安全性が確保され、しかも設備、作業に要する費用が大幅に節減され、作業自体の煩わしさも解消されるものとなっている。
【図面の簡単な説明】
【図1】本発明を実施した洗浄方法を示す図である。
【図2】従来の技術を示し、水蒸気による洗浄方法を示す図である。
【図3】従来の技術を示し、アルコールによる洗浄方法を示す図である。
【符号の説明】
10 容器
11 砂層
12 ブロワー
13 微量の注水装置
14 ポンプ
15 排気系
N ナトリウム
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method of cleaning and disassembling prior to disposal of tanks, containers, and equipment in which alkali metal contaminants, particularly sodium, remain attached.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, as the above-described alkali metal contamination container and equipment cleaning and dismantling methods, water vapor cleaning shown in FIG. 2 and alcohol cleaning shown in FIG. 3 are generally known.
[0003]
Alkali metal has high chemical activity, reacts with cleaning agents such as water and alcohol, and releases hydrogen gas to be chemically inactivated. That is, in the case of sodium, it reacts with water to form sodium hydroxide and reacts with alcohol to ethoxylate. In this case, if the container and the equipment to be treated are filled with air, there is a risk that the released hydrogen gas reacts with oxygen in the air in particular to cause an explosion.
[0004]
The steam cleaning method shown in FIG. 2 will be described. In FIG. 2, reference numeral 1 denotes a container in which sodium N remains attached. An inert gas such as nitrogen gas is fed into the container 1 from the gas tank 2 to fill and replace the inside, and by injecting water vapor from the water vapor generator 3, the sodium N is changed to sodium hydroxide N ′. It is intended to inactivate sodium N. In FIG. 2, 4 is a drainage tank, and 5 is an exhaust system in which a flame arrester (backfire prevention device) 6 is interposed.
[0005]
Also, FIG. 3 shows a cleaning method using alcohol, and parts common to those in FIG. In this case, an inert gas such as nitrogen gas is filled in the container 1 from the gas tank 2, and the alcohol 8 is injected from the alcohol tank 7 into the container 1 via the pump 8. The alcohol 8 is circulated by a circulation pump 9.
[0006]
In this way, after alkali metal (sodium N) is inactivated and hydrogen gas is no longer generated, the container 1 is disassembled and discarded by mechanical means such as a gas cutting method.
[0007]
[Problems to be solved by the invention]
However, according to the conventional method described above, it is necessary to always inject an inert gas in order to remove the danger of explosion caused by hydrogen gas, alcohol, or steam, a continuous inert gas injection device, water vapor Many additional devices such as a device for injecting a cleaning agent such as alcohol or the like are required, the operation becomes complicated, and the cost including the work execution cost increases.
[0008]
OBJECT OF THE INVENTION
Therefore, the present invention pays attention to the actual situation and problems of the related art, and solves such problems, thereby obtaining more reliable safety and reducing the cost required for equipment and work. An object of the present invention is to provide a method for cleaning and disassembling an alkali metal contaminant that is supposed to be sufficient.
[0009]
[Means for Solving the Problems]
In order to achieve this object, the method for cleaning and decomposing alkali metal contaminants according to the present invention covers at least the surface of the existing alkali metal with a sand layer, then introduces moist air to reduce the hydrogen concentration. The alkali metal is reacted to inactivate, and when the inactivation is completed and generation of hydrogen ceases, mechanical dismantling work is performed in an air atmosphere. In the case of a small amount, it is characterized by injecting a small amount of water as an auxiliary, and when the hydrogen concentration becomes a remarkable value, the introduction of the above-mentioned moist air is stopped and an inert gas such as argon gas or nitrogen gas is injected. It is characterized by reducing the hydrogen concentration while exhausting while stopping the introduction of humid air at the end of the working time and injecting inert gas such as argon gas and nitrogen gas to replace the air Air, is characterized in that inlet of the gas, and closes the discharge port keep prevent ingress of air.
[0010]
[Action]
Such a configuration eliminates the need for a continuous injecting apparatus for inert gas such as nitrogen gas and an injecting apparatus for cleaning agents such as water vapor and alcohol, which have been required in the past, and greatly reduces costs in terms of equipment and work. In addition, by providing a sand layer, more reliable safety can be obtained as described below.
[0011]
That is, by covering at least the surface of the alkali metal with a sand layer, it is anticipated due to the expected water retention in the target container, the internal local part of the equipment, or the inflow of water when a small amount of water is injected. Even if a large amount of hydrogen gas is generated at one time, the explosive hydrogen gas reacts with water to generate heat and sequester high-temperature alkali metals, and ignition It can be prevented from becoming a source.
[0012]
Moreover, even if the explosive hydrogen gas contained in the sand layer starts an explosion on the surface of the alkali metal where the temperature is high, the explosion flame is cooled and extinguished by passing through the sand layer, and the outside of the sand layer A large amount of explosive gas does not reach the flame and disappears only by a small explosion in the sand layer.
[0013]
Furthermore, when a large amount of water passes through the sand layer, the flow area is widened on the water outflow side due to the action of water retention and diffusion of sand, and in addition, the water flow peak is leveled and flattened. . Therefore, it is possible to prevent the passing water from concentrating and reacting with the alkali metal at a time, and it is possible to suppress the generation of a large amount of hydrogen gas and the high temperature of the reaction alkali metal serving as an ignition source.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Next, an embodiment of the present invention will be described with reference to FIG. FIG. 1 is a diagram showing a method for cleaning a sodium contaminated container embodying the present invention.
[0015]
In FIG. 1, reference numeral 10 denotes a container in which sodium N adheres and remains inside. In FIG. 1, at least the surface of the sodium 10 is covered with a sand layer 11, and a large amount of outside air including moisture is fed into the container 10 from the inlet horizontal piping of the container 1 by the blower 12. In this embodiment, air is supplied using the blower 12, but external air can be sucked using a fan or other means as necessary.
[0016]
In addition, in the figure, reference numeral 13 shown by an imaginary line is a water injection device for a very small amount of water, and water is injected into the container 10 by the pump 14, but the water injection device 13 is dry in the winter and the like and has low humidity. It will be used as a supplementary case. In the figure, reference numeral 15 denotes an exhaust system.
[0017]
Here, a specific example will be described with reference to FIG. 1. As the container 10, a cylindrical structure having a diameter of 3 m and a height of 8 m having a complicated structure not particularly shown inside is used. Some (sodium hydroxide) is present in about 2 t, and a plurality of (four locations) through holes are made in the lower body of the container 10, and dry sand is poured into the sand layer 11. The thickness of this sand layer 11 was about 30 cm.
[0018]
Next, a large amount of outside air is supplied by the blower 12 (more specifically, air supply amount is 50 m 3 / min, air temperature is 30 degrees Celsius, humidity is 80%, 1,169 Kgw / min water is injected, and air supply is performed for 5 hours a day. If it is performed for 4 days, 1403 Kgw of water will be injected). Moreover, in order to monitor the reaction state in the container 10, the hydrogen concentration in the container 10 was always measured with the measuring device.
[0019]
The reaction product adhering to the inner wall surface of the container 10 immediately after the start of air supply by the blower 12 begins to deliquesce, and the deliquescent solution and the reaction product flow down the inner wall surface of the container 10 to reach the surface of the sand layer 11. The deliquescent liquid was absorbed into the sand layer 11, and the reaction product further deliquescent on the surface of the sand layer 11. This process was extremely gentle.
[0020]
The sodium N in the lower end plate of the container 10 covered with the sand layer 11 reacted and became inactive due to the deliquescent liquid that passed through the sand layer 11 and the moisture diffused from the air on the surface of the sand layer 11. In this reaction process, a relatively intense reaction with a blunt explosion sound was occasionally observed in the sand layer 11, and it was found that the temperature slightly increased when the outer wall of the container 10 near the lower end plate was touched.
[0021]
When the hydrogen concentration in the container 10 becomes a significant value and exceeds the work continuation limit value for preventing explosions, air supply by the blower 12 is stopped and exhausted while injecting argon gas to calm the reaction. Waiting, when the hydrogen concentration decreased, air was blown again by the blower 12.
[0022]
When the working time of the day (the above-mentioned 5 hours) ends, the air supply is stopped, argon gas is injected into the container 10 to replace the air in the container 10, and the air supply and exhaust ports are blinded in that state. The plate was closed off with a plate to prevent outside air from entering the container 10 and left to stand.
[0023]
The above work process was repeated, and one week later, when no increase in the hydrogen concentration was observed even when air was supplied, it was judged that the inactivation was completed, and the operation was shifted to the dismantling work.
[0024]
The container 10 was disassembled by gas cutting. Cut the two parts of the body of the container 10 near the upper end plate and the lower end plate, water the upper and middle parts to wash away the remaining reaction products, and remove the sand from the bottom end plate part with a scoop. While dismantling, the attached reaction product was scraped off and washed with water.
[0025]
In the specific embodiment described above, the operation could be completed while being extremely economical and ensuring a large level of safety.
[0026]
【The invention's effect】
The alkali metal contaminant cleaning and disassembling method according to the present invention is configured as described above. Therefore, further safety is ensured, the cost required for equipment and work is greatly reduced, and the troublesomeness of the work itself is eliminated.
[Brief description of the drawings]
FIG. 1 shows a cleaning method embodying the present invention.
FIG. 2 is a diagram showing a conventional technique and a cleaning method using water vapor.
FIG. 3 is a diagram showing a conventional technique and a cleaning method using alcohol.
[Explanation of symbols]
10 Container 11 Sand layer 12 Blower 13 Small amount of water injection device 14 Pump 15 Exhaust system N Sodium

Claims (4)

存在するアルカリ金属の少なくとも表面を砂層で覆い、次いで含湿空気を導入して換気を行ない、水素濃度を薄めるとともに前記アルカリ金属を反応させて不活性化し、その不活性化が完了して水素の発生がなくなった時点で空気雰囲気において機械的解体作業をなすことを特徴とするアルカリ金属汚染体の洗浄解体方法。Cover at least the surface of the existing alkali metal with a sand layer, then introduce humidified air to ventilate, reduce the hydrogen concentration and react with the alkali metal to inactivate it. A cleaning and dismantling method for alkali metal contaminants, characterized in that mechanical dismantling work is performed in an air atmosphere at the time when the generation disappears. 前記した含湿空気の湿分が少ない場合、補助的に微量の水を注入することを特徴とする請求項1に記載のアルカリ金属汚染体の洗浄解体方法。2. The method for cleaning and disassembling an alkali metal contaminant according to claim 1, wherein when the moisture content of the moisture-containing air is low, a small amount of water is injected as an auxiliary. 水素濃度が顕著な値となった場合、前記した含湿空気の導入を止め、アルゴンガス、窒素ガス等の不活性ガスを注入しつつ排気し、水素濃度を低下させることを特徴とする請求項1または請求項2に記載のアルカリ金属汚染体の洗浄解体方法。When the hydrogen concentration becomes a significant value, the introduction of the moisture-containing air is stopped, the exhaust gas is exhausted while injecting an inert gas such as argon gas and nitrogen gas, and the hydrogen concentration is lowered. A method for cleaning and disassembling an alkali metal contaminant according to claim 1 or 2. 作業時間の終了に伴い、含湿空気の導入を止め、アルゴンガス、窒素ガス等の不活性ガスを注入して空気の置換をなし、空気、ガスの導入口、排出口を閉塞して空気の侵入を防止しておくことを特徴とする請求項1、請求項2または請求項3に記載のアルカリ金属汚染体の洗浄解体方法。At the end of the work time, the introduction of humid air is stopped, inert gas such as argon gas and nitrogen gas is injected to replace the air, and the air, gas inlet and outlet are closed, and the air The method for cleaning and disassembling an alkali metal contaminant according to claim 1, 2 or 3, wherein intrusion is prevented.
JP05834397A 1997-02-26 1997-02-26 Cleaning and dismantling method for alkali metal contaminants Expired - Lifetime JP3839121B2 (en)

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