JPH0262032B2 - - Google Patents
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- Publication number
- JPH0262032B2 JPH0262032B2 JP11582784A JP11582784A JPH0262032B2 JP H0262032 B2 JPH0262032 B2 JP H0262032B2 JP 11582784 A JP11582784 A JP 11582784A JP 11582784 A JP11582784 A JP 11582784A JP H0262032 B2 JPH0262032 B2 JP H0262032B2
- Authority
- JP
- Japan
- Prior art keywords
- collection
- collection material
- seawater
- rate
- radionuclides
- 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.)
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Description
イ 発明の目的
産業上の利用分野
本発明は放射性核種、重金属等の捕集材であ
る。
本発明は原子力発電所、放射性同位元素取扱等
事業所を始めとする原子力施設から発生する放射
性廃液中に含まれる放射性核種の分離除去および
海洋河川あるいは産業廃水等に含まれている放射
性核種および重金属等の分離除去に利用される。
従来の技術
原子力発電所(水型)、放射性同位元素取扱事
業所等各種原子力施設から発生する放射性廃液に
は各種放射性核種が含まれている。これらの放射
性廃液の処理においては、被曝低減の観点などか
ら廃液中に含まれる放射性核種を分離除去して放
射線レベルを低減させることぎ必要である。又、
海洋河川中には微量ではあるが60CO,90Sr,137Cs
など種々の人工性核種の存在が確認されており、
これらの放射性核種の濃度および分布に関するデ
ータを長期間にわたり蓄積することは海洋学、海
洋生態学また中低レベル放射性廃棄物の海洋投棄
などの観点から重要なことである。
従来、放射性廃液中の放射性核種の分離・除去
あるいは海洋河川からの放射性核種および重金属
の回収には主として凝集沈殿法およびイオン交換
法が利用されている。
凝集沈殿法は、廃液に凝集剤を混合して放射性
物質の電荷を中和し、これを凝集させて大きな分
子の集団、すなわちフロツクを生成させ、このフ
ロツクを沈降、分離させる処理方法で、一般に
Al2(SO4)3+Ca(OH)2、粘土(+高分子凝集剤)、
FeCl3+Na2S,Na3PO4+Ca(OH)2等が凝集剤と
して使用されている。この方法は、小量ないし複
雑な廃液の処理には、手数がかかる割に、除染係
数は大きくないが安価簡便であり、単純な液質の
大量廃液を処理するのに適するので広く用いられ
ている。イオン交換法は各種合成陽イオン交換
体、合成陰イオン交換体、混床イオン交換樹脂、
あるいは石炭、褐炭、泥炭等をベースとする天然
有機交換体、グリンサイド、カオリナイト、ゼオ
ライト等をベースとする無機交換体を使用して廃
液の処理を行う方法である。かかる凝集沈殿法お
よびイオン交換法によつて廃液を処理するとき放
射能は各々スラツジ(汚泥)および再生廃液に濃
縮される。非放射性廃液の場合には浄化された水
を得さえすればこれら濃縮液は一般に放置廃棄さ
れるのであるが、放射性廃液の場合には濃縮放射
能を再拡散させず保持固定するため二次処理が必
要である。現在、かかるスラツジ、再生廃液は沈
降、砂床ロ過、加圧ロ過、真空ロ過、遠心分離、
オートクレーブ処理等の二次処理方法で脱水減容
をはかつた後固型化が施されているが、これらの
二次処理による減容比は各々<1,4,5〜10,
10〜15,25〜35および2〜4というのが実情であ
る。
上述した理由により、各種原子力事業所から発
生する放射性廃液に含まれる放射性核種、海洋河
川あるいは産業廃水等に含まれる放射性核種ある
いは重金属を効率よく分離・除去し且つ減容比が
高い捕集材が斯界で望まれていた。
発明が解決しようとする問題点
本発明によつて捕集効率および減容比の高い放
射性核種および重金属捕集材が提供される。
本発明によつて放射性廃液、海洋河川あるいは
産業廃水中に含まれる放射性核種特に、59Fe,
60CO,65Zn,103+106Rn,134+137Cs,144Ce等を高い効
率で捕集し且つ高い比率で減容される捕集材が提
供される。
本発明によつて深層海水中の微量放射性核種を
採水現場で捕集することが可能な捕集材が提供さ
れる。
本発明によつて解決される問題は以下逐次明ら
かにされる。
ロ 発明の構成
問題点を解決するための手段
上述した問題点は、アクリル繊維に一般式
K2M〓〔Fe(CN)6〕で表わされるフエロシアン酸
塩化合物(ここでM〓はCo,Zn,Ni,Zr等2価
金属から選ばれる一種)を担持固定した捕集材を
使用することによつて解決される。
本発明者等は深層海水中に含まれる極低濃度の
134+137Cs,65Zn等の放射性核種を効率よく捕集し、
而も、減容比の高い捕集材の開発を行つてきた。
その結果、アクリル繊維に式K2Co〔Fe(CN)6〕
で表わされるフエロシアン化コバルト・カリウム
を担持・固定した捕集材が134+137Csをほぼ100%
捕集することを発見した。更に研究を発展させた
所かかる捕集材は134+137Csの他に39Fe,60Co,
65Zn,103+106Ru,144Ceも捕集出来ることを発見し
た。更に、検討を重ねた結果、放射性廃液の態様
によつてはアクリル繊維のフエロシアン化ニツケ
ル・カリウム(K2Ni〔Fe(CN)6)〕あるいはフエ
ロシアン化亜鉛・カリウム(K2Zn〔Fe(CN)6〕)
あるいはフエロシアン化ジルコニウム・カリウム
(K2Zr〔Fe(CN)6〕)等を担持・固定した捕集材も
フエロシアン化コバルト・カリウムを担持・固定
させた捕集材より有効であることを発見した。
以下、アクリル繊維にフエロシアン化コバル
ト・カリウムを担持・固定させた捕集材の製造方
法について解説する。
アクリル繊維100gを10%フエロシアン化カリ
ウム水溶液に浸漬し3時間60〜70℃で加温し、取
り出した後、10%硝酸コバルト水溶液に浸漬し3
時間60〜70℃に加温した後水洗後60〜70℃で10時
間乾燥し、この操作を3回繰り返すこによつてア
クリル繊維にフエロシアン化コバルト・カリウム
を担持・固定させることによつて製造される。
又、別の態様としては、アクリル繊維100gを10
%硝酸コバルト水溶液に浸漬し3時間60〜70℃で
加温し、取り出した後10%フエロシアン化カリウ
ム水溶液に浸漬し3時間60〜70℃で加温した後水
洗後60〜70℃で10時間乾燥し、この操作を3回繰
り返すことによつてもアクリル繊維にフエロシア
ン化コバルト・カリウムを担持・固定させること
が出来る。
この様にして製造された本発明の捕集材の色調
は赤褐色でフエロシアン化コバルト・カリウムを
担持・固定させた後も綿状である。交換容量を求
めた結果0.13meq/g・捕集材であつた。捕集材
中の成分を調べるためカリウム、鉄、コバルトを
定量した結果(K:Fe:Co)=(9.8:12:35)
mg/g・捕集材であつた。
本発明の捕集材を製造するのに使用されるアク
リル繊維は繊径18μm,8wt%のアクリル酸メチ
ルを共重合したものでアニオンン基として
0.05meq/g・繊維のSO3 -を含有している。30%
以下の塩酸、硝酸、硫酸等の耐酸性は非常に強
く、逆に耐アルカリ性は弱く1%水酸化ナトリウ
ム溶液でも変性する。
本発明の捕集材はPH7〜9の範囲でバツチ法に
より、65Zn,106Ru,144Ceを90%以上捕集する他
54Mn,60Co,59Feを一部捕集し、カラム法で59Fe,
60Co,65Zn,134+137Cs,144Ceを90%以上捕集する。
更に重要なことは多量のNa+の存在下においても
137Csを捕集することが出来るという特徴をもつ
ている。
上述した本発明の捕集材の製造において、硝酸
コバルトに替えて硝酸亜鉛を用いることによつて
アクリル繊維にフエロシアン化亜鉛・カリウム
を、又硝酸コバルトに替えて硝酸ニツケルを用い
ることによつてフエロシアン化ニツケル・カリウ
ム又硝酸コバルトに替えて硝酸ジルコニウムを用
いることによつてフエロシアン化ジルコニウム・
カリウムを担持・固定させることが出来る。本発
明の捕集材は放射性廃液の態様によつて使い分け
ることが好ましい、例えば軽水一次冷却水系の
放射性核種を分離・除去するにはフエロシアン化
コバルト・カリウムよりフエロシアン化ニツケ
ル・カリウムを担持・固定させた捕集材を用いる
方が好ましい。
以下実施例および参考例によつて本発明の効果
を具体的に説明する。
実施例−捕集材の製造
繊径18μm,8wt%のアクリル酸メチルを共重
合したアニオン基として0.05meq/g・繊維の
SO3 -を含有しているアクリル繊維100gを10%フ
エロシアン化カリウム溶液に浸し60〜70℃で3時
間加温した。取り出した後、10%硝酸コバルト溶
液に浸し60〜70℃で3時間加温した。水洗後60〜
70℃で、10時間乾燥した。この操作を3回繰り返
してアクリル繊維上にフエロシアン化コバルト・
カリウムを担持・固定させた赤褐色の捕集材を製
造した。この捕集材の交換容量は0.13meq/g・
捕集材であつた。捕集材中のカリウム、鉄および
コバルトを定量した結果(K:Fe:Co)=(9.8:
12:35)mg/g・捕集材であつた。
次に実施例で製造した捕集材を使用して海水か
らの各種放射性核種の捕集テストを行つて得た結
果を参考例1,2および3として記載する。
参考例1 バツチ法による捕集テスト
1.1 実験材料
1.1.1 海水
海水(千葉県勝浦市で採水)は富士フイルム社
製・ミクロフイルター(0.45μm)でろ過したも
のを使用し、トレーサーとしての各種の放射性核
種添加後、塩酸ならびに水酸化ナトリウム溶液で
PHを8.0±0.5に調整した。また使用した海水の塩
分は33.7%であつた。
1.1.2 使用核種
54Mn(MnCl2,0.5NHCl) 無担体
59Fe(FeCl3,0.5NHCl) 11mCi/mgFe
60Co(CoCl2,0.1NHCl) 136mCi/mgCo
65Zn(ZnCl2,0.5NHCl) 2.8mCi/mgZn
85Sr(SrCl2,0.5NHCl) 7.4mCi/mgSr
106Ru(塩化物、4NHCl) 7.7mCi/mgRu
137Cs(CsCl,0.5NHCl) 9.0mCi/mgCs
144Ce(CeCl3,1NHCl) 250mCi/mgCe
これらの核種を放射能濃度として約100nCi/
mlに希釈したのち海水に添加した。
1.1.3 測定装置
Nal(Tl)シンチレーシヨンスペクトロメー
タ:44φ×51mm井戸型Nal(Tl)検出器をAloka社
製ユニバーサルスケーラ(モデルTDC−501)に
接続して測定した。
1.2 実験操作
1.2.1バツチ法による撹拌時間と捕集率
海水200ml毎に各種のトレーサーを添加する。
これに捕集材を加え、撹拌時間を2,5,10,20
分と変化させた。各撹拌時間が終了した後、海水
の一定量を測定用ポリエチレン管に移し入れ、
Nal(Tl)検出器で測定し捕集率を求めた。捕集
率Aは次式のように定義した。
A(%)={(R1−R2)/R1}×100
A:繊維(KCFC)の捕集率
R1:トレーサー添加海水の計数率
R2:撹拌後の海水の計数率
1.3 結果と考察
1.3.1 撹拌時間と捕集率
表−1はバツチ法の実験条件とPHの変化を示し
てある。海水のPHは実験開始時と20分間撹拌後と
の間に差は見られなかつた。
バツチ法での実験結果を表−2、および第1図
に示した。図、および表より明らかなように、捕
集材には20分間の撹拌時間で65Zn,106Ru,144Ceが
90%以上とよく捕集される他、54Mn,60Co,59Feが
一部捕集されている。しかしながら85Srは全く捕
集されていないことが明らかとなつた。
A. Field of industrial application of the invention The present invention is a collection material for radionuclides, heavy metals, etc. The present invention relates to the separation and removal of radionuclides contained in radioactive waste liquid generated from nuclear facilities such as nuclear power plants and radioisotope handling facilities, and the radionuclides and heavy metals contained in marine rivers or industrial wastewater. It is used for separation and removal of etc. BACKGROUND ART Radioactive waste fluids generated from various nuclear facilities, such as nuclear power plants (water type) and offices that handle radioactive isotopes, contain various radionuclides. In the treatment of these radioactive waste liquids, it is necessary to separate and remove the radionuclides contained in the waste liquids to reduce the radiation level from the perspective of reducing exposure. or,
60 CO, 90 Sr, 137 Cs are present in marine rivers, although in trace amounts.
The existence of various artificial nuclides such as
Accumulating data on the concentration and distribution of these radionuclides over a long period of time is important from the viewpoints of oceanography, marine ecology, and ocean dumping of medium- and low-level radioactive waste. Conventionally, coagulation-sedimentation methods and ion exchange methods have been mainly used to separate and remove radionuclides from radioactive waste liquids or to recover radionuclides and heavy metals from marine rivers. The coagulation-sedimentation method is a treatment method in which a flocculant is mixed with the waste liquid to neutralize the electric charge of the radioactive substance, and this is flocculated to produce a group of large molecules, or flocs, and the flocs are sedimented and separated.
Al 2 (SO 4 ) 3 +Ca(OH) 2 , clay (+polymer flocculant),
FeCl 3 +Na 2 S, Na 3 PO 4 +Ca(OH) 2 , etc. are used as flocculants. Although this method is time-consuming for processing small volumes or complex waste liquids, the decontamination coefficient is not large, but it is cheap and simple, and is suitable for processing large quantities of simple liquid waste liquids, so it is widely used. ing. Ion exchange methods include various synthetic cation exchangers, synthetic anion exchangers, mixed bed ion exchange resins,
Alternatively, there is a method of treating waste liquid using a natural organic exchanger based on coal, lignite, peat, etc., or an inorganic exchanger based on greenside, kaolinite, zeolite, etc. When wastewater is treated by such coagulation-sedimentation and ion exchange methods, radioactivity is concentrated in the sludge and regenerated wastewater, respectively. In the case of non-radioactive waste liquids, these concentrated liquids are generally disposed of as long as purified water is obtained, but in the case of radioactive waste liquids, secondary treatment is required to retain and fix the concentrated radioactivity without re-diffusion. is necessary. Currently, such sludge and recycled waste liquid are processed through sedimentation, sand bed filtration, pressure filtration, vacuum filtration, centrifugation,
Solidification is performed after dehydration and volume reduction using secondary treatment methods such as autoclaving, but the volume reduction ratios due to these secondary treatments are <1, 4, 5 to 10, respectively.
The actual situation is 10-15, 25-35 and 2-4. For the reasons mentioned above, a collection material with a high volume reduction ratio that can efficiently separate and remove radionuclides contained in radioactive waste fluids generated from various nuclear power plants, radionuclides or heavy metals contained in marine rivers or industrial wastewater, etc. is needed. It was desired in this world. Problems to be Solved by the Invention The present invention provides a radionuclide and heavy metal trapping material with high trapping efficiency and volume reduction ratio. According to the present invention, radionuclides contained in radioactive liquid waste, marine rivers or industrial wastewater, in particular, 59 Fe,
A collection material is provided that can collect 60 CO, 65 Zn, 103+106 Rn, 134+137 Cs, 144 Ce, etc. with high efficiency and reduce the volume at a high rate. The present invention provides a collection material capable of collecting trace amounts of radionuclides in deep seawater at a water sampling site. The problems solved by the present invention will be successively clarified below. (b) Means for solving the structural problems of the invention The above-mentioned problems are solved by the general formula
A collection material that supports and fixes a ferrocyanate compound represented by K 2 M〓 [Fe(CN) 6 ] (where M〓 is a type selected from divalent metals such as Co, Zn, Ni, and Zr) is used. This is solved by The present inventors have discovered that ultra-low concentrations contained in deep seawater
Efficiently collects radionuclides such as 134+137 Cs and 65 Zn,
In addition, we have been developing a collection material with a high volume reduction ratio.
As a result, acrylic fibers have the formula K2Co [Fe(CN) 6 ]
The collection material supporting and fixing cobalt and potassium ferrocyanide expressed as 134+137 Cs is almost 100%
I discovered that I could collect it. Further research has shown that in addition to 134+137 Cs, the collection material contains 39 Fe, 60 Co,
We discovered that 65 Zn, 103+106 Ru, and 144 Ce can also be collected. Furthermore, as a result of repeated studies, we found that depending on the form of the radioactive waste liquid, acrylic fibers such as nickel/potassium ferrocyanide (K 2 Ni [Fe (CN) 6 )] or zinc/potassium ferrocyanide (K 2 Zn [Fe (CN) ) 6 〕)
Alternatively, we discovered that a collection material supported and fixed with zirconium/potassium ferrocyanide (K 2 Zr [Fe(CN) 6 ]) is more effective than a collection material supported/fixed with cobalt/potassium ferrocyanide. . Below, we will explain the method for producing a collection material in which cobalt and potassium ferrocyanide are supported and fixed on acrylic fibers. 100g of acrylic fiber was immersed in a 10% potassium ferrocyanide aqueous solution, heated at 60 to 70℃ for 3 hours, taken out, and immersed in a 10% cobalt nitrate aqueous solution.
Manufactured by heating and fixing cobalt and potassium ferrocyanide on acrylic fibers by heating to 60-70℃ for an hour, washing with water, drying at 60-70℃ for 10 hours, and repeating this operation three times. be done.
In addition, in another embodiment, 100g of acrylic fiber is
% cobalt nitrate aqueous solution and heated at 60 to 70°C for 3 hours, then taken out, immersed in a 10% potassium ferrocyanide aqueous solution and heated at 60 to 70°C for 3 hours, then washed with water and heated at 60 to 70°C for 10 hours. By drying and repeating this operation three times, cobalt/potassium ferrocyanide can be supported and fixed on the acrylic fiber. The color of the collecting material of the present invention produced in this manner is reddish brown and remains flocculent even after supporting and fixing cobalt/potassium ferrocyanide. The exchange capacity was determined to be 0.13 meq/g of collection material. Results of quantifying potassium, iron, and cobalt to investigate the components in the collection material (K:Fe:Co) = (9.8:12:35)
mg/g/collection material. The acrylic fiber used to produce the collection material of the present invention has a fiber diameter of 18 μm and is copolymerized with 8 wt% methyl acrylate, and has anionic groups.
Contains 0.05 meq/g of fiber SO 3 - . 30%
It has very strong resistance to acids such as hydrochloric acid, nitric acid, and sulfuric acid, but has weak alkali resistance and can be denatured even with a 1% sodium hydroxide solution. The collection material of the present invention can collect 90% or more of 65 Zn, 106 Ru, and 144 Ce using the batch method in the pH range of 7 to 9.
Part of 54 Mn, 60 Co, and 59 Fe was collected and 59 Fe, 59 Fe,
Captures over 90% of 60 Co, 65 Zn, 134+137 Cs, and 144 Ce.
More importantly, even in the presence of large amounts of Na +
It has the characteristic of being able to collect 137 Cs. In the production of the above-mentioned collection material of the present invention, zinc ferrocyanide and potassium ferrocyanide can be added to the acrylic fiber by using zinc nitrate instead of cobalt nitrate, and ferrocyanide can be added to the acrylic fiber by using nickel nitrate instead of cobalt nitrate. By using zirconium nitrate instead of potassium nickel chloride or cobalt nitrate, zirconium ferrocyanide
It can support and fix potassium. It is preferable to use the collection material of the present invention depending on the type of radioactive waste liquid.For example, to separate and remove radionuclides from a light water primary cooling water system, nickel/potassium ferrocyanide is supported and fixed rather than cobalt/potassium ferrocyanide. It is preferable to use a collection material that is The effects of the present invention will be specifically explained below using Examples and Reference Examples. Example - Manufacture of collection material Fiber diameter 18μm, 8wt% methyl acrylate copolymerized as an anion group 0.05meq/g fiber
100 g of acrylic fiber containing SO 3 - was immersed in a 10% potassium ferrocyanide solution and heated at 60 to 70° C. for 3 hours. After taking it out, it was immersed in a 10% cobalt nitrate solution and heated at 60 to 70°C for 3 hours. 60~ after washing with water
It was dried at 70°C for 10 hours. Repeat this operation three times to coat the acrylic fiber with cobalt ferrocyanide.
A reddish-brown collection material supporting and fixing potassium was produced. The exchange capacity of this collection material is 0.13meq/g・
It was a collection material. The results of quantifying potassium, iron and cobalt in the collection material (K:Fe:Co) = (9.8:
12:35) mg/g/collection material. Next, the results obtained by performing a collection test of various radionuclides from seawater using the collection material manufactured in the example will be described as Reference Examples 1, 2, and 3. Reference example 1 Collection test using batch method 1.1 Experimental materials 1.1.1 Seawater Seawater (collected in Katsuura City, Chiba Prefecture) was filtered with a microfilter (0.45μm) manufactured by Fujifilm, and various tracers were used. After adding the radionuclide, it was added with hydrochloric acid and sodium hydroxide solution.
The pH was adjusted to 8.0±0.5. The salinity of the seawater used was 33.7%. 1.1.2 Nuclides used 54 Mn (MnCl 2 , 0.5NHCl) No carrier 59 Fe (FeCl 3 , 0.5NHCl) 11 mCi/mgFe 60 Co (CoCl 2 , 0.1NHCl) 136 mCi/mgCo 65 Zn (ZnCl 2 , 0.5NHCl) 2.8 mCi/mgZn 85 Sr (SrCl 2 , 0.5NHCl) 7.4mCi/mgSr 106 Ru (chloride, 4NHCl) 7.7mCi/mgRu 137 Cs (CsCl, 0.5NHCl) 9.0mCi/mgCs 144 Ce (CeCl 3 , 1NHCl) 250mCi/ mgCe The radioactive concentration of these nuclides is approximately 100nCi/
After diluting to ml, it was added to seawater. 1.1.3 Measuring device Nal (Tl) scintillation spectrometer: Measurement was performed by connecting a 44φ x 51 mm well type Nal (Tl) detector to a universal scaler (model TDC-501) manufactured by Aloka. 1.2 Experimental procedures 1.2.1 Stirring time and collection rate by batch method Add various tracers to every 200 ml of seawater.
Add collection material to this and stir for 2, 5, 10, 20
I changed it to minutes. After each stirring period, a certain amount of seawater is transferred into the measuring polyethylene tube.
The collection rate was determined by measurement using a Nal (Tl) detector. The collection rate A was defined as in the following equation. A (%) = {(R 1 − R 2 )/R 1 }×100 A: Collection rate of fiber (KCFC) R 1 : Count rate of tracer-added seawater R 2 : Count rate of seawater after stirring 1.3 Results 1.3.1 Stirring time and collection rate Table 1 shows the experimental conditions of the batch method and changes in pH. There was no difference in the pH of seawater between the beginning of the experiment and after stirring for 20 minutes. The experimental results using the batch method are shown in Table 2 and Figure 1. As is clear from the figure and table, 65 Zn, 106 Ru, and 144 Ce were added to the collection material after stirring for 20 minutes.
In addition to being well collected at over 90%, 54 Mn, 60 Co, and 59 Fe were also partially collected. However, it became clear that 85 Sr was not collected at all.
【表】【table】
【表】
参考例2 カラム法による捕集テスト
2.1 実験材料
参考例1と同じ海水および核種並びに測定装置
を使用した。
2.2 実験操作
2.2.1カラム法による流速と捕集率
内径15mmφ、長さ20cmのガラスに捕集材を詰
め、トレーサーを添加した海水200mlを流速を変
化させて通した。通過液の一定量を測定用ポリエ
チレン管に移し入れ、Nal(Tl)検出器で装定し
捕集率を求めた。捕集率Aは次式のように定義し
た。
A(%)={(R1−R3)/R1}×100
A:捕集材の捕集率
R1:トレーサー添加海水の計数率
R3:捕集材カラム通過液の計数率
2.3 結果と考察
2.3.1 流速と捕集率
実験条件と結果を表−3および第2図に示し
た。流速20ml/minで59Fe,60Co,65Zn,137Cs,
144Ceの捕集率は90%以上であり、180ml/minと
流速を増加しても、これらの核種は80%と高い捕
集率を示した。65Zn,137Cs,144Ceでは捕集率の減
少がみられなかつたが、59Feで5%,60Coで10%の
減少が認められた。106Ruは20ml/minと180ml/
minでは55%と大幅な減少を示した。これらの結
果から65Zn,137Cs,144Ceは大型カラムでも十分適
用できることが判明した。しかしながらバツチ法
で捕集率の高かつた106Ru(バツチ法で91%)はカ
ラム法では意外に低くしかも流速の増加とともに
急速に捕集率は減少している。この原因は、カラ
ム法で用いた106Ruトレーサー(塩酸系)による
ものと考えられる。[Table] Reference Example 2 Collection test using column method 2.1 Experimental materials The same seawater, nuclides, and measurement equipment as in Reference Example 1 were used. 2.2 Experimental operations 2.2.1 Flow rate and collection rate by column method A glass with an inner diameter of 15 mmφ and a length of 20 cm was filled with a collection material, and 200 ml of seawater added with a tracer was passed through it at varying flow rates. A fixed amount of the passing liquid was transferred to a polyethylene tube for measurement, and the collection rate was determined by equipping it with a Nal (Tl) detector. The collection rate A was defined as follows. A (%) = {(R 1 − R 3 )/R 1 }×100 A: Collection rate of the collection material R 1 : Count rate of tracer-added seawater R 3 : Count rate of the liquid passing through the collection material column 2.3 Results and discussion 2.3.1 Flow rate and collection rate The experimental conditions and results are shown in Table 3 and Figure 2. 59 Fe, 60 Co, 65 Zn, 137 Cs at a flow rate of 20 ml/min.
The collection rate of 144 Ce was over 90%, and even when the flow rate was increased to 180ml/min, the collection rate of these nuclides was as high as 80%. No decrease in collection rate was observed for 65 Zn, 137 Cs, and 144 Ce, but a decrease of 5% for 59 Fe and 10% for 60 Co was observed. 106 Ru is 20ml/min and 180ml/min
At min, it showed a significant decrease of 55%. These results revealed that 65 Zn, 137 Cs, and 144 Ce can be sufficiently applied to large columns. However, 106 Ru, which had a high collection rate in the batch method (91% in the batch method), was surprisingly low in the column method, and the collection rate decreased rapidly as the flow rate increased. The cause of this is thought to be the 106 Ru tracer (hydrochloric acid type) used in the column method.
【表】
参考例3 大型カラムによる捕集テスト
参考例3では捕集材を大型捕集カラムに詰め、
大量海水(200)を流した場合の捕集率と流速
との関係について検討した。
3.1 実験材料
3.1.1 捕集材
実施例で製造した本発明の捕集材
3.1.2 カラム
特製のアクリル製カラム内径50mmφ,100mmφ、
長さ40cmを使用した。
3.1.3 海水
海水(千葉県勝浦市で採水)は富士フイルム社
製・ミクロフイルター(0.45μm)でろ過したも
のを使用し、トレーサーとしての各種の放射性核
種添加後、塩酸ならびに水酸化ナトリウム溶液で
PHを8.0±0.5に調整した。また使用した海水の塩
分は33.7%であつた。
3.1.4 使用核種
54Mu MnCl2(MnCl2 2μg/g in 0.1NHCl)
202.5pCi/ml
59Fe FeCl3,(FeCl3 2μg/g in 0.1NHCl)
337.6pCi/ml
60Co CoCl2(CoCl2 1μg/g in 0.1NHCl)
255.3pCi/ml
65Zn ZnCl2(ZnCl2 2μg/g in 0.1NHCl)
216.9pCi/ml
85Sr SrCl2(SrCl2 2μg/g in 0.1NHCl)
290.0pCi/ml
106Ru RuCl3(RuCl3 10μg/g in 0.1NHCl)
248.0pCi/ml
137Cs CsCl(CsCl1μg/g in 0.1NHCl)
201.2pCi/ml
144Ce CeCl3(CeCl3 2μg/g in 0.1NHCl)
210.5pCi/ml
3.1.5 測定装置
γ線分光分析装置:ゲルマニウム検出器は
ORTEC社製のものをまた波高分析器はCANB−
ERRA社製を使用した。
3.2 実験操作
3.2.1 54Mn,59Fe,60Co.65Zn,106Ru,137Cs,144Ce
の捕集
内径50mmφおよび100mmφのアクリル製捕集カ
ラムに54Mn,59Fe,60Co,65Zn,106Ru,144Ceならび
に137Csの捕集に捕集材を詰め、トレーサーを添
加した海水200を表−4に示した実験条件でカ
ラムに通した。本発明の捕集材およびイオン交換
樹脂を測定容器に移し入れたのちGe半導体検出
器で測定し捕集率を求めた。捕集率Aは次式のよ
うに定義した。
A(%)=R10/R9×100
A:捕集材の捕集率
R9:添加したトレーサーの濃度(pCi)
R10:捕集されたトレーサーの濃度(pCi)[Table] Reference Example 3 Collection test using a large column In Reference Example 3, the collection material was packed into a large collection column,
We investigated the relationship between collection efficiency and flow velocity when a large amount of seawater (200) was flowing. 3.1 Experimental materials 3.1.1 Collection material Collection material of the present invention manufactured in the example 3.1.2 Column Specially made acrylic column inner diameter 50mmφ, 100mmφ,
A length of 40cm was used. 3.1.3 Seawater Seawater (sampled in Katsuura City, Chiba Prefecture) was filtered using a microfilter (0.45 μm) manufactured by Fujifilm, and after adding various radionuclides as tracers, hydrochloric acid and sodium hydroxide solution were used. in
The pH was adjusted to 8.0±0.5. The salinity of the seawater used was 33.7%. 3.1.4 Nuclide used 54 Mu MnCl 2 (MnCl 2 2μg/g in 0.1NHCl)
202.5pCi/ml 59 Fe FeCl 3 , (FeCl 3 2μg/g in 0.1NHCl)
337.6pCi/ml 60 CoCoCl 2 (CoCl 2 1μg/g in 0.1NHCl)
255.3pCi/ml 65 Zn ZnCl 2 (ZnCl 2 2μg/g in 0.1NHCl)
216.9pCi/ml 85 Sr SrCl 2 (SrCl 2 2μg/g in 0.1NHCl)
290.0pCi/ml 106 RuRuCl 3 (RuCl 3 10μg/g in 0.1NHCl)
248.0pCi/ml 137 Cs CsCl (CsCl1μg/g in 0.1NHCl)
201.2pCi/ml 144 Ce CeCl 3 (CeCl 3 2μg/g in 0.1NHCl)
210.5pCi/ml 3.1.5 Measuring device Gamma ray spectrometer: Germanium detector is
The wave height analyzer is CANB- manufactured by ORTEC.
A product manufactured by ERRA was used. 3.2 Experimental operations 3.2.1 54 Mn, 59 Fe, 60 Co. 65 Zn, 106 Ru, 137 Cs, 144 Ce
Collection of 54 Mn, 59 Fe, 60 Co, 65 Zn, 106 Ru, 144 Ce, and 137 Cs were packed in acrylic collection columns with inner diameters of 50 mmφ and 100 mmφ, and 200 mm of seawater added with tracer was collected. was passed through the column under the experimental conditions shown in Table 4. The collection material and ion exchange resin of the present invention were transferred to a measurement container, and then measured with a Ge semiconductor detector to determine the collection rate. The collection rate A was defined as follows. A (%) = R 10 / R 9 × 100 A: Collection rate of collection material R 9 : Concentration of added tracer (pCi) R 10 : Concentration of collected tracer (pCi)
【表】【table】
【表】
3.3 結果と考察
表−4および5の実験条件と結果から明らかな
ように、本発明の捕集材の捕集実験においては
137Csの他、65Znもほぼ100%で捕集されているこ
とが明らかになつた。しかしながら、表−3で示
されている本発明の捕集材に捕集され易い59Fe,
60Co,144Ceは本実験では32〜69%と低い捕集率を
示したことから、大量海水処理中に離脱するもの
と考えられる。
発明の効果
以上を通覧することによつて(1)本発明の捕集材
は;
(1) PH7〜9の範囲で59Fe,60Co,65Zn,103+106Ru,
134+137Cs,144Ceを捕集すること、
(2) 多量のNa+の存在下に於いても137Csを捕集
すること、
(3) 綿状であるためフイルターへの加工が容易で
ありまたカートリツジ式にも加工出来ること、
(4) 綿状であるため燃焼させると廃棄物としての
処理が極めて容易である。等の効果があること
がわかる。[Table] 3.3 Results and Discussion As is clear from the experimental conditions and results in Tables 4 and 5, in the collection experiment using the collection material of the present invention,
It became clear that in addition to 137 Cs, 65 Zn was also collected at almost 100%. However, 59 Fe, which is easily collected by the collection material of the present invention shown in Table 3,
Since 60 Co and 144 Ce showed a low capture rate of 32 to 69% in this experiment, it is thought that they are released during treatment of large amounts of seawater. Effects of the Invention By reviewing the above, (1) the collection material of the present invention: (1) 59 Fe, 60 Co, 65 Zn, 103+106 Ru, in the pH range of 7 to 9
( 2) Captures 137 Cs even in the presence of a large amount of Na (4) Since it is cotton-like, it is extremely easy to dispose of it as waste when burned. It can be seen that there are similar effects.
第1図および第2図は各々本発明の捕集材を用
いてバツチ法およびカラム法で捕集テストをして
得た結果を示すグラフである。
FIG. 1 and FIG. 2 are graphs showing the results of a collection test using the collection material of the present invention in a batch method and a column method, respectively.
Claims (1)
〔M〓2価の金属〕で表わされるフエロシアン酸塩
化合物を担持固定して成る放射性核種および重金
属捕集材。 2 M〓がコバルトである特許請求の範囲第1項
記載の捕集材。 3 M〓が亜鉛である特許請求の範囲第1項記載
の捕集材。 4 M〓がニツケルである特許請求の範囲第1項
記載の捕集材。 5 M〓がジルコニウムである特許請求の範囲第
1項記載の捕集材。[Claims] 1 General formula K 2 M〓[Fe(CN) 6 ] in acrylic fiber
A radionuclide and heavy metal collection material comprising a supported and fixed ferrocyanate compound represented by [M = divalent metal]. 2. The collection material according to claim 1, wherein M is cobalt. 3. The collection material according to claim 1, wherein M is zinc. 4. The collection material according to claim 1, wherein M is nickel. 5. The collection material according to claim 1, wherein M is zirconium.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11582784A JPS60260000A (en) | 1984-06-06 | 1984-06-06 | Radioactive nuclide and heavy-metal capture material |
| US06/719,433 US4720422A (en) | 1984-06-06 | 1985-04-03 | Material for collecting radionuclides and heavy metals |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11582784A JPS60260000A (en) | 1984-06-06 | 1984-06-06 | Radioactive nuclide and heavy-metal capture material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60260000A JPS60260000A (en) | 1985-12-23 |
| JPH0262032B2 true JPH0262032B2 (en) | 1990-12-21 |
Family
ID=14672097
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11582784A Granted JPS60260000A (en) | 1984-06-06 | 1984-06-06 | Radioactive nuclide and heavy-metal capture material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60260000A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2501831B2 (en) * | 1987-07-13 | 1996-05-29 | 旭化成工業株式会社 | Cartridge for collecting radionuclides and heavy metals |
| JP5750388B2 (en) * | 2012-03-12 | 2015-07-22 | 大日精化工業株式会社 | Method for removing radioactive iodine and radioactive cesium and hydrophilic resin composition for removing radioactive iodine and radioactive cesium |
| IN2014KN00960A (en) * | 2011-12-28 | 2015-10-09 | Dainichiseika Color Chem | |
| JP2013167470A (en) * | 2012-02-14 | 2013-08-29 | Nitto Denko Corp | Radioactive waste treatment method and method for manufacturing inorganic ion exchanger |
| JP6213978B2 (en) * | 2012-02-14 | 2017-10-18 | 国立研究開発法人産業技術総合研究所 | Cesium adsorbent and method for removing cesium using the same |
-
1984
- 1984-06-06 JP JP11582784A patent/JPS60260000A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60260000A (en) | 1985-12-23 |
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