JPS6119958B2 - - Google Patents
Info
- Publication number
- JPS6119958B2 JPS6119958B2 JP12640180A JP12640180A JPS6119958B2 JP S6119958 B2 JPS6119958 B2 JP S6119958B2 JP 12640180 A JP12640180 A JP 12640180A JP 12640180 A JP12640180 A JP 12640180A JP S6119958 B2 JPS6119958 B2 JP S6119958B2
- Authority
- JP
- Japan
- Prior art keywords
- waste liquid
- activated carbon
- radioactive
- ruthenium
- powder
- 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.)
- Expired
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 15
- 239000002699 waste material Substances 0.000 claims description 11
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 8
- 230000002285 radioactive effect Effects 0.000 claims description 8
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 229910052707 ruthenium Inorganic materials 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 4
- 239000002901 radioactive waste Substances 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 229910052725 zinc Inorganic materials 0.000 claims description 2
- 239000011701 zinc Substances 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims 1
- 239000010949 copper Substances 0.000 claims 1
- 229910052742 iron Inorganic materials 0.000 claims 1
- 238000005202 decontamination Methods 0.000 description 7
- 230000003588 decontaminative effect Effects 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- -1 nitrosyl compounds Chemical class 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- KJTLSVCANCCWHF-BKFZFHPZSA-N ruthenium-106 Chemical compound [106Ru] KJTLSVCANCCWHF-BKFZFHPZSA-N 0.000 description 2
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- WZECUPJJEIXUKY-UHFFFAOYSA-N [O-2].[O-2].[O-2].[U+6] Chemical compound [O-2].[O-2].[O-2].[U+6] WZECUPJJEIXUKY-UHFFFAOYSA-N 0.000 description 1
- FJNQSTUXQFLBIS-UHFFFAOYSA-H [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[U+6] Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[U+6] FJNQSTUXQFLBIS-UHFFFAOYSA-H 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910001448 ferrous ion Inorganic materials 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 235000014413 iron hydroxide Nutrition 0.000 description 1
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 239000002925 low-level radioactive waste Substances 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000002915 spent fuel radioactive waste Substances 0.000 description 1
- DNYWZCXLKNTFFI-UHFFFAOYSA-N uranium Chemical compound [U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U][U] DNYWZCXLKNTFFI-UHFFFAOYSA-N 0.000 description 1
- 229910000439 uranium oxide Inorganic materials 0.000 description 1
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
本発明は放射性廃液の処理の方法に関する。よ
り詳細に述べると本発明は特に使用済核燃料再処
理工場から発生する放射性ルテニウムを含む中低
レベル放射性廃液の処理に関する。
廃液中に含まれる放射性ルテニウム106Ruは処
理工程中共存する硝酸によつて多種類のニトロシ
ル化合物を形成し一つの方法によつてはある種の
ニトロシル化合物のみが除去され、他のニトロシ
ル化合物が残るため除去効率を高めることができ
ず、廃棄物処理上甚だ厄介な核種である。多種類
の化学形の混合物として存在しても比較的高い除
去効率で処理できる放射性廃液の処理方法として
は蒸発濃縮法があるが、中低レベル廃液はその量
が著しく大量であるため、蒸発濃縮処理による方
法では経済的処理は困難で、イオン交換法又は凝
集沈殿法等も採用されている。
本発明の目的は従来の凝集沈殿法又はイオン交
換法の代りに金属粉末と活性炭とを混合したもの
を吸着体とするカラム法により、多種類の化学形
をもつ放射性ルテニウムを効率よく除去すること
にある。
本発明は放射性ルテニウム106Ruを含む廃液を
金属粉末と活性炭を混合充てんしたカラムを通過
させることから成る。本発明を実施するに当つて
は106Ruが最も吸着され易い状態にするためPH3
前後に調整することによつて効率を高めることが
できる。
以下実施例を掲げて本発明の構成および効果を
具体的に説明する。尚本実施例その他で使用した
放射性ルテニウムを含む廃液は酸化ウランを原子
炉で照射し、硝酸に溶解後苛性ソーダで中和しウ
ランを水酸化ウランとしてHz過分離した液であ
る。従来使われている水酸化鉄共沈法等で除去し
うる化学形の放射性ルテニウムは僅かしか含まれ
ていない。
実施例 1
内径18mm長さ83mmのガラス製カラムに粒度100
メツシユの活性炭3gと亜鉛粉5gを混合したも
のを充填し、106Ruを含む廃液300c.c./時で通し
た。廃液の酸性度をそれぞれPH=2,3,4およ
び5に調整して通水し、通液(処理液)中の
106Ruの放射能濃度を通水前(原液)の値と比較
し除染係数を求めた。結果を次に示す。
The present invention relates to a method of treating radioactive waste liquid. More specifically, the present invention particularly relates to the treatment of medium and low level radioactive waste fluid containing radioactive ruthenium generated from spent nuclear fuel reprocessing plants. The radioactive ruthenium -106 Ru contained in the waste liquid forms many types of nitrosyl compounds with the coexisting nitric acid during the treatment process, and depending on one method, only some types of nitrosyl compounds are removed and other nitrosyl compounds remain. Therefore, removal efficiency cannot be improved, making it an extremely troublesome nuclide in terms of waste treatment. Evaporative concentration is a method for treating radioactive waste liquids that can be treated with relatively high removal efficiency even if they exist as a mixture of various chemical forms. Economical treatment is difficult with treatment methods, and ion exchange methods, coagulation precipitation methods, etc. are also used. The purpose of the present invention is to efficiently remove radioactive ruthenium, which has many different chemical forms, by using a column method using a mixture of metal powder and activated carbon as an adsorbent instead of the conventional coagulation-precipitation method or ion exchange method. It is in. The present invention consists of passing a waste liquid containing radioactive ruthenium 106 Ru through a column packed with a mixture of metal powder and activated carbon. In carrying out the present invention, the pH is set to 3 to make 106 Ru most easily adsorbed.
Efficiency can be increased by adjusting back and forth. The structure and effects of the present invention will be specifically explained below with reference to Examples. The waste liquid containing radioactive ruthenium used in this example and others is a liquid obtained by irradiating uranium oxide in a nuclear reactor, dissolving it in nitric acid, neutralizing it with caustic soda, and subjecting the uranium to uranium hydroxide by Hz over-separation. It contains only a small amount of chemically radioactive ruthenium that can be removed by the conventionally used iron hydroxide coprecipitation method. Example 1 Particle size 100 in a glass column with an inner diameter of 18 mm and a length of 83 mm.
It was filled with a mixture of 3 g of mesh activated carbon and 5 g of zinc powder, and a waste liquid containing 106 Ru was passed through at 300 c.c./hour. Adjust the acidity of the waste liquid to PH = 2, 3, 4, and 5, respectively, and pass water through it.
The decontamination coefficient was determined by comparing the radioactivity concentration of 106 Ru with the value before water flow (undiluted solution). The results are shown below.
【表】
実施例 2
106Ruを含む廃液の酸性度をPH=3に調整し、
実施例1で使用したものと同じカラムで亜鉛の代
りに100メツシユの銅粉および鉄粉について実施
し除染係数を求めた。本実験の場合通水量は500
c.c.とした。[Table] Example 2 The acidity of the waste liquid containing 106 Ru was adjusted to PH = 3,
Using the same column as used in Example 1, 100 meshes of copper powder and iron powder were used instead of zinc to determine the decontamination coefficient. In this experiment, the water flow rate was 500
I made it cc.
【表】
比較例 1
106Ruを含む廃液の酸性度をPH=3に調整し、
充填物として、活性炭および亜鉛粉をそれぞれ単
独で使用した場合の除染係数を求めた。本実験の
場合通水量は200c.c.とした。[Table] Comparative example 1 The acidity of waste liquid containing 106 Ru was adjusted to PH = 3,
The decontamination coefficient was determined when activated carbon and zinc powder were used alone as fillers. In this experiment, the water flow rate was 200 c.c.
【表】
比較例 2
放射性廃液中の106Ru除去法として代表的なも
ののいくつかについて比較実験を行つた。[Table] Comparative Example 2 Comparative experiments were conducted on some typical methods for removing 106 Ru from radioactive waste liquid.
【表】
シーブ法
実施例および比較例の結果から明らかなように
活性炭に亜鉛粉末を混合したものを吸着体とする
カラムを用いて効果的に106Ruを除去することが
できる。また106Ruを含む溶液のPHを3以下とす
ることによりさらに高い除染係数で106Ruを除去
できた。銅粉、鉄粉あるいはそれらの混合粉を使
用した場合も同様の傾向が認められた。
活性炭または亜鉛粉を単独で用いた実験では低
い除染係数しか得られないことから廃液に含まれ
る106Ru化合物が亜鉛粉と活性炭との組合せによ
り陰イオンとして存在しているルテニウムを陽イ
オン化することにより、活性炭に吸着されやすい
状態となるためと考えられる。従来行われている
106Ru除去法のいくつかについて比較実験を行つ
たが、106Ruの除染係数はいづれも1.0以下と低
い。本発明の方法と比較的類似する原理による除
去法として第一鉄イオンを含水チタン酸に吸着さ
せ、カラム上で106Ruを還元して含水チタン酸に
吸着されやすい化学形に変える方法があるが、本
発明による亜鉛粉末+活性炭の方が除染係数が高
く、第一鉄チタネート法のように還元剤である第
一鉄が溶離してなくなることがなく処理量を多く
することができる。[Table] Sieve method As is clear from the results of Examples and Comparative Examples, 106 Ru can be effectively removed using a column whose adsorbent is a mixture of activated carbon and zinc powder. Furthermore, by setting the pH of the solution containing 106 Ru to 3 or less, 106 Ru could be removed with an even higher decontamination coefficient. A similar tendency was observed when copper powder, iron powder, or a mixed powder thereof was used. Since only a low decontamination coefficient was obtained in experiments using activated carbon or zinc powder alone, the 106 Ru compound contained in the waste liquid was used to cationize ruthenium, which is present as an anion, by the combination of zinc powder and activated carbon. This is thought to be due to the fact that it becomes easily adsorbed by activated carbon. Traditionally done
Comparative experiments were conducted on several 106 Ru removal methods, but the decontamination coefficients for 106 Ru were all low at 1.0 or less. As a removal method based on a principle relatively similar to the method of the present invention, there is a method in which ferrous ions are adsorbed on hydrous titanic acid, and 106 Ru is reduced on a column to convert it into a chemical form that is easily adsorbed on hydrous titanic acid. The zinc powder + activated carbon according to the present invention has a higher decontamination coefficient, and unlike the ferrous titanate method, ferrous iron, which is a reducing agent, is not eluted and disappears, making it possible to increase the throughput.
Claims (1)
される金属粉末および活性炭を混合充填したカラ
ムに放射性ルテニウムを含む廃液を通過させるこ
とにより放射性ルテニウムを除去することを特徴
とする放射性廃液の処理の方法。 2 廃液がPH3程度に調整される特許請求の範囲
第1項記載の方法。[Claims] 1. Radioactive ruthenium is removed by passing waste liquid containing radioactive ruthenium through a column packed with a mixture of activated carbon and metal powder selected from zinc, copper, iron, and mixtures thereof. Method of treatment of radioactive waste liquid. 2. The method according to claim 1, wherein the waste liquid is adjusted to a pH of about 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12640180A JPS5750698A (en) | 1980-09-11 | 1980-09-11 | Method of treating waste liquid containing radioactive ruthemium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12640180A JPS5750698A (en) | 1980-09-11 | 1980-09-11 | Method of treating waste liquid containing radioactive ruthemium |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5750698A JPS5750698A (en) | 1982-03-25 |
JPS6119958B2 true JPS6119958B2 (en) | 1986-05-20 |
Family
ID=14934236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12640180A Granted JPS5750698A (en) | 1980-09-11 | 1980-09-11 | Method of treating waste liquid containing radioactive ruthemium |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5750698A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02195623A (en) * | 1989-01-24 | 1990-08-02 | Nippon Thermostat Kk | Bimetallic disk |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58182596A (en) * | 1982-04-19 | 1983-10-25 | 日本原子力事業株式会社 | Method of processing radioactive liquid waste |
JPS6019035A (en) * | 1983-07-13 | 1985-01-31 | Mitsui Mining & Smelting Co Ltd | Adsorbent of radioactive ruthenium waste solution |
JPS60161598A (en) * | 1983-12-15 | 1985-08-23 | 日本原子力研究所 | Method of treating radioactive waste liquor containing radioactive ruthenium |
JPS6145998A (en) * | 1984-08-10 | 1986-03-06 | 日本原子力研究所 | Method of removing radioactive ruthenium in radioactive waste liquor |
JPH0810273B2 (en) * | 1986-01-27 | 1996-01-31 | 株式会社日立製作所 | Reprocessing of spent nuclear fuel |
GB2255087B (en) * | 1991-04-25 | 1995-06-21 | Robert Winston Gillham | System for cleaning contaminated water |
GB2255088A (en) * | 1991-04-25 | 1992-10-28 | Robert Winston Gillham | Removal of contaminants from water |
-
1980
- 1980-09-11 JP JP12640180A patent/JPS5750698A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02195623A (en) * | 1989-01-24 | 1990-08-02 | Nippon Thermostat Kk | Bimetallic disk |
Also Published As
Publication number | Publication date |
---|---|
JPS5750698A (en) | 1982-03-25 |
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