JPS6147597A - Method for removing radioactive iodine from exhaust gas - Google Patents

Method for removing radioactive iodine from exhaust gas

Info

Publication number
JPS6147597A
JPS6147597A JP16934484A JP16934484A JPS6147597A JP S6147597 A JPS6147597 A JP S6147597A JP 16934484 A JP16934484 A JP 16934484A JP 16934484 A JP16934484 A JP 16934484A JP S6147597 A JPS6147597 A JP S6147597A
Authority
JP
Japan
Prior art keywords
iodine
silver
adsorbent
ozone
exhaust gas
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.)
Pending
Application number
JP16934484A
Other languages
Japanese (ja)
Inventor
修 栗山
小沢 義弘
清美 船橋
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.)
Central Research Institute of Electric Power Industry
Hitachi Ltd
Original Assignee
Central Research Institute of Electric Power Industry
Hitachi Ltd
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 Central Research Institute of Electric Power Industry, Hitachi Ltd filed Critical Central Research Institute of Electric Power Industry
Priority to JP16934484A priority Critical patent/JPS6147597A/en
Publication of JPS6147597A publication Critical patent/JPS6147597A/en
Pending legal-status Critical Current

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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】 〔発明の利用分野〕 本発明は、原子力施設から放出される排ガス中からの放
射性ヨウ素化合物除去方法に係シ、特に銀化合物を担体
上に添着した吸着材(以下、「銀吸着材」と記す)の再
生方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a method for removing radioactive iodine compounds from exhaust gas emitted from nuclear facilities, and particularly relates to an adsorbent (hereinafter referred to as (referred to as "silver adsorbent").

〔発明の背景〕[Background of the invention]

原子力施設では、周辺住民の放射能被曝を防止するため
、周辺環境へ放出される放射能量を低減するための種々
の対策が講じられている。このうち、放射性ヨウ素に対
しては、これが人体の甲状腺に選択的に吸収される放射
能被曝を増大させるため、特に厳格な放出放射能量の低
減対策が施されている。排ガスの低減対策としては、直
径1〜2喘程度の吸着材を充填したヨウ素除去フィルタ
の設置が一般に行われている。核燃料再処理プラント排
ガス中からのヨウ素除去方法に関しては、幾つかの方法
が研究開発、または実用化されているが、その中の1つ
として、一度ヨウ素の吸着した銀吸着材を500p、水
素雰囲気下で再生して繰り返して使用する方法がある。
At nuclear facilities, various measures are taken to reduce the amount of radioactivity released into the surrounding environment in order to prevent the surrounding residents from being exposed to radiation. Among these, radioactive iodine is selectively absorbed by the human thyroid gland, increasing exposure to radiation, so particularly strict measures are taken to reduce the amount of radioactivity released. As a measure to reduce exhaust gas, it is common practice to install an iodine removal filter filled with an adsorbent having a diameter of about 1 to 2 mm. Regarding methods for removing iodine from nuclear fuel reprocessing plant exhaust gas, several methods have been researched and developed or have been put into practical use.One of them is to remove iodine from a silver adsorbent that has absorbed iodine at 500p in a hydrogen atmosphere. There is a way to play it below and use it repeatedly.

この従来法について第1図を用いて説明する。ヨウ素除
去吸着装置(吸着塔)1,2は、二基切替方式になって
おり、ヨウ素が破過した時点で切替える。吸着操作が終
了した方の吸着塔2には、ヒータ3により500Cまで
加熱された水素を通気する。ヨウ化銀として吸着されて
いたヨウ素はヨウ化水素として脱離する。一方、同時に
銀吸着材は、水素によシ銀(Ag)に還元再生される。
This conventional method will be explained using FIG. 1. The iodine removal and adsorption devices (adsorption towers) 1 and 2 are of a two-unit switching system, and are switched when iodine exceeds the level. Hydrogen heated to 500C by the heater 3 is vented into the adsorption tower 2 where the adsorption operation has been completed. Iodine adsorbed as silver iodide is desorbed as hydrogen iodide. Meanwhile, at the same time, the silver adsorbent is reduced and regenerated into silver (Ag) by hydrogen.

吸着塔2を出たヨウ化水素を含むガスは、クーラ4によ
シ150Cまで冷却され、ヨウ素固定化装置5に通気さ
れる。ガス中のヨウ化水素は、ヨウ素固定化装置5内の
固定化用吸着材(例えば、鉛ゼオライト)に吸着固定化
される。しかし、上記の方法で再生された銀吸着材は、
有機ヨウ素を吸着できないという欠点がある。再処理排
ガス中にはヨウ化メチルを主とした有機ヨウ素が約5%
含まれているといわれるため、水素ガスによる銀吸着材
の再生システムを再処理排ガスに適用した場合、吸着塔
1゜2の後段に新たに有機ヨウ素を吸着除去するだめの
吸着塔6を取りつける必要がある。このため、水素ガス
による銀吸着材の再生プロセスには、高価な銀の消費量
が増え、プロセスが複雑になるという問題点が出てくる
The hydrogen iodide-containing gas leaving the adsorption tower 2 is cooled to 150C by the cooler 4 and vented to the iodine fixation device 5. Hydrogen iodide in the gas is adsorbed and fixed on a fixing adsorbent (for example, lead zeolite) in the iodine fixing device 5. However, the silver adsorbent regenerated by the above method is
The drawback is that it cannot adsorb organic iodine. Approximately 5% of organic iodine, mainly methyl iodide, is in the reprocessed exhaust gas.
Therefore, when applying a silver adsorbent regeneration system using hydrogen gas to reprocessed exhaust gas, it is necessary to install an additional adsorption tower 6 to adsorb and remove organic iodine after adsorption tower 1゜2. There is. For this reason, the regeneration process of silver adsorbents using hydrogen gas has the problem of increasing consumption of expensive silver and complicating the process.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、上記した問題点を解決するた ・めに
、有機ヨウ素の吸着も可能なように銀吸着材を再生でき
る方法を提供するにある。
An object of the present invention is to provide a method for regenerating a silver adsorbent so that it can also adsorb organic iodine, in order to solve the above-mentioned problems.

〔発明の概要〕[Summary of the invention]

本発明は、銀吸着材をオゾンによって再生し、再生後の
形態を酸化銀にすると、銀吸着材がヨウ化メチル等の有
機ヨウ素まで吸着可能になるという点に着目してなされ
たものである。
The present invention was made with the focus on the point that when a silver adsorbent is regenerated with ozone and the regenerated form is made into silver oxide, the silver adsorbent becomes capable of adsorbing even organic iodine such as methyl iodide. .

〔発明の実施例〕[Embodiments of the invention]

本発明を実施しうるに好適な実施例を図面を用いて、以
下詳細に述べる。
Preferred embodiments for carrying out the present invention will be described in detail below with reference to the drawings.

第2図に本発明を実施しうるに好適な一実施例の基本フ
ローを示す。二基切替方式になっているヨウ素吸着除去
装置(吸着塔)7,8には、銀吸着材が充填されている
。吸着塔はヨウ素が破過した時点で切り替える。酸素濃
度が約30%の酸素窒素混合ガス(再生ガス)をオゾン
発生器9に通気させ、混合ガス中のオゾン濃度が数チに
なるように調節する。、数−のオゾンを含んだ混合ガス
を、吸着操作の終了した吸着塔8に通気して再生を行9
゜銀吸着材上のヨウ化銀は、下記の反応により、酸化銀
に酸化され再生される。一方、吸着材上に吸着されてい
たヨウ素は、元素状ヨウ素ガス(I2 )として脱着す
る。
FIG. 2 shows the basic flow of a preferred embodiment for carrying out the present invention. The iodine adsorption and removal devices (adsorption towers) 7 and 8, which are of a two-unit switching type, are filled with silver adsorbent. The adsorption tower is switched when the iodine content is exceeded. Oxygen-nitrogen mixed gas (regeneration gas) with an oxygen concentration of about 30% is passed through the ozone generator 9, and the ozone concentration in the mixed gas is adjusted to several inches. , a mixed gas containing several ozone is vented into the adsorption tower 8 where the adsorption operation has been completed for regeneration.
゜Silver iodide on the silver adsorbent is oxidized to silver oxide and regenerated by the following reaction. On the other hand, the iodine adsorbed on the adsorbent is desorbed as elemental iodine gas (I2).

2AgI+03→AgzO+Iz+Oz   ・・・・
・・・・・(1)オゾンの大部分は、(1〕の反応式に
従い、ヨウ化銀を酸化銀に酸化するために消費される。
2AgI+03→AgzO+Iz+Oz ・・・・
(1) Most of the ozone is consumed to oxidize silver iodide to silver oxide according to the reaction formula (1).

再生ガス中に残存した微量のオゾンは、白金触媒を充填
したオゾン分解装置10で完全に分解される。また、再
生ガス中のヨウ素は、銅をアルミナに添着しだ鋼吸入f
材を充填したヨウ素固定化装置11によって、99.9
%以上が[d走化される。第3図に再生ガス温匿を斐え
た場合、固定化材である銅吸着材に対してヨウ素度W’
WEがどのように変るかを調べだ結果を示す。第3図に
示されるように、再生ガス温度を150C以下に保てば
、オゾンガスによる銀吸714材の再生が可能であり、
更に再生ガス中に含まれるヨウ素を銅吸着材に固定化で
きることがわかった。
The trace amount of ozone remaining in the regeneration gas is completely decomposed by the ozone decomposition device 10 filled with a platinum catalyst. In addition, the iodine in the regeneration gas is absorbed into the steel by impregnating copper with alumina.
The iodine fixation device 11 filled with 99.9
% or more are chemotactic. Figure 3 shows that when the regeneration gas is heated, the iodine content W' is
We will investigate how WE changes and show the results. As shown in Figure 3, if the regeneration gas temperature is kept below 150C, it is possible to regenerate the silver-absorbed 714 material with ozone gas.
Furthermore, it was found that the iodine contained in the regeneration gas could be immobilized on the copper adsorbent.

この実施例によれば、ヨウ化メチル等の有機ヨウ素を除
去するだめの硫酸銀を添着した銀吸着材が不用となり、
有機ヨウ素も再生した銀吸着材(酸化銀として存在)で
除去できるため、銀吸着材の使用量が大幅に減り、貴重
な銀員原の消費を減らすという効果がある。また、再生
ガス温度は150C以下と、水素による再生ガス温度5
00Cと比べて、比較的低温で再生が可能であるため、
エネルギーが節約できる。更に、再生ガスとして水素ガ
スを使用しないため、安全であシかつ装置がIm単にな
るという効果もおる。以上のように本実施例によれば、
数々の効果を奏しうろことができる。
According to this embodiment, a silver adsorbent impregnated with silver sulfate for removing organic iodine such as methyl iodide becomes unnecessary,
Since organic iodine can also be removed with the regenerated silver adsorbent (present as silver oxide), the amount of silver adsorbent used is significantly reduced, which has the effect of reducing the consumption of valuable silver sources. In addition, the regeneration gas temperature is 150C or less, and the regeneration gas temperature due to hydrogen is 5.
Since it can be regenerated at a relatively low temperature compared to 00C,
Energy can be saved. Furthermore, since hydrogen gas is not used as the regeneration gas, it is safe and the apparatus is simple. As described above, according to this embodiment,
You can play around with a number of effects.

先の実施例において、再生ガスとして酸素・窒素混合ガ
スの代わりに、純酸素を使うことも可能である。この場
合、酸素・窒素混合ガスを使うよシもオゾンの発生効率
がよくなり、ヨウ素の吸着した銀吸着材の再生速度が上
るため、再生時間を短縮できるという効果がある。
In the previous embodiment, it is also possible to use pure oxygen as the regeneration gas instead of the oxygen/nitrogen mixture. In this case, even if an oxygen/nitrogen mixed gas is used, the efficiency of ozone generation is improved, and the regeneration speed of the silver adsorbent that has adsorbed iodine is increased, so the regeneration time can be shortened.

このほか、オゾンの代わりに過酸化水素のような元生肋
の酸素ケ発生させることができるものを組み合せて用い
ても、オゾンの場合と同様の効果がある。
In addition, the same effect as ozone can be obtained by using a combination of hydrogen peroxide, which can generate oxygen in the original ribs, instead of ozone.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、ヨウ素の吸着した銀吸着材を再生する
際に、簡単な方法で有機ヨウ素化合物まで吸着可能なよ
うに再生できるという効果がある。
According to the present invention, when regenerating a silver adsorbent that has adsorbed iodine, it is possible to regenerate it so that even organic iodine compounds can be adsorbed by a simple method.

図面の]νj′j単な説明 第1図は従来の実施例を説明するためのフロー図、第2
図は・ド発明の詳細な説明するためのフロー図、第3図
は本発明を実施した一実施例の結果図である。
[of the drawings] νj′j Simple explanation FIG. 1 is a flow diagram for explaining the conventional embodiment, and FIG.
The figure is a flowchart for explaining the invention in detail, and FIG. 3 is a diagram showing the results of an embodiment of the invention.

1.2・・・ヨウ素除去吸着装置、3・・・ヒータ、4
・・・クーラ、5・・・ヨウ素固定化装置、6・・・有
機ヨウ素除去用吸着塔、7,8・・・ヨウ楽除去吸着装
置、9・・・オゾン発生器、10・・・オゾン分解装置
、11・・・第1図
1.2... Iodine removal adsorption device, 3... Heater, 4
... Cooler, 5 ... Iodine fixation device, 6 ... Adsorption tower for removing organic iodine, 7, 8 ... Iodine removal adsorption device, 9 ... Ozone generator, 10 ... Ozone Decomposition device, 11...Figure 1

Claims (1)

【特許請求の範囲】 1、担体上に銀を添着させたヨウ素除去用吸着材を再生
して繰り返し使用する方法において、吸着材上の反応生
成物であるヨウ化銀を発生期状態の酸素によって酸化し
て再生することを特徴とする排ガス中からの放射性ヨウ
素除去方法。 2、特許請求の範囲第1項において、発生期状態の酸素
がオゾンであり150℃以下の酸素・窒素混合ガスを、
オゾン発生器、ヨウ素の吸着した銀吸着材が充填された
ヨウ素除去装置、オゾン分解装置、固定化用吸着材の充
填されたヨウ素固定化装置の順で、それぞれの装置に通
気した後、再びオゾン発生器に戻すという工程でヨウ化
銀を酸化銀に酸化することを特徴とする排ガス中からの
放射性ヨウ素除去方法。
[Claims] 1. In a method of regenerating and repeatedly using an adsorbent for removing iodine in which silver is impregnated on a carrier, silver iodide, which is a reaction product on the adsorbent, is removed by oxygen in a nascent state. A method for removing radioactive iodine from exhaust gas, which is characterized by oxidation and regeneration. 2. In claim 1, the oxygen in the nascent state is ozone and the oxygen/nitrogen mixed gas at 150°C or less,
The ozone generator, the iodine removal device filled with silver adsorbent that has adsorbed iodine, the ozone decomposition device, and the iodine fixation device filled with the fixation adsorbent are ventilated in this order, and then the ozone is removed again. A method for removing radioactive iodine from exhaust gas, which is characterized by oxidizing silver iodide to silver oxide in the process of returning it to a generator.
JP16934484A 1984-08-15 1984-08-15 Method for removing radioactive iodine from exhaust gas Pending JPS6147597A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16934484A JPS6147597A (en) 1984-08-15 1984-08-15 Method for removing radioactive iodine from exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16934484A JPS6147597A (en) 1984-08-15 1984-08-15 Method for removing radioactive iodine from exhaust gas

Publications (1)

Publication Number Publication Date
JPS6147597A true JPS6147597A (en) 1986-03-08

Family

ID=15884818

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16934484A Pending JPS6147597A (en) 1984-08-15 1984-08-15 Method for removing radioactive iodine from exhaust gas

Country Status (1)

Country Link
JP (1) JPS6147597A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04138369U (en) * 1991-06-21 1992-12-25 旭物産株式会社 down comforter with fur

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04138369U (en) * 1991-06-21 1992-12-25 旭物産株式会社 down comforter with fur

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