JPH0324499A - Removal of ruthenium in radioactive waste gas - Google Patents
Removal of ruthenium in radioactive waste gasInfo
- Publication number
- JPH0324499A JPH0324499A JP15986089A JP15986089A JPH0324499A JP H0324499 A JPH0324499 A JP H0324499A JP 15986089 A JP15986089 A JP 15986089A JP 15986089 A JP15986089 A JP 15986089A JP H0324499 A JPH0324499 A JP H0324499A
- Authority
- JP
- Japan
- Prior art keywords
- waste gas
- silica gel
- composition
- nitrogen
- nitrogen oxides
- 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
Links
- 239000002901 radioactive waste Substances 0.000 title claims abstract description 12
- 239000007789 gas Substances 0.000 title claims description 8
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 title claims description 7
- 229910052707 ruthenium Inorganic materials 0.000 title claims description 7
- 238000000034 method Methods 0.000 claims abstract description 35
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000741 silica gel Substances 0.000 claims abstract description 20
- 229910002027 silica gel Inorganic materials 0.000 claims abstract description 20
- 239000002912 waste gas Substances 0.000 claims abstract description 19
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000002915 spent fuel radioactive waste Substances 0.000 claims abstract description 9
- 239000000203 mixture Substances 0.000 claims abstract description 8
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 claims abstract description 7
- 230000004992 fission Effects 0.000 claims abstract description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 6
- 229910052778 Plutonium Inorganic materials 0.000 claims abstract description 4
- 229910052770 Uranium Inorganic materials 0.000 claims abstract description 4
- OYEHPCDNVJXUIW-UHFFFAOYSA-N plutonium atom Chemical compound [Pu] OYEHPCDNVJXUIW-UHFFFAOYSA-N 0.000 claims abstract description 4
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 claims abstract description 4
- 238000012545 processing Methods 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 230000003647 oxidation Effects 0.000 claims 1
- 238000007254 oxidation reaction Methods 0.000 claims 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 42
- 229910017604 nitric acid Inorganic materials 0.000 abstract description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 abstract description 5
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical compound CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 abstract description 4
- SNRUBQQJIBEYMU-UHFFFAOYSA-N dodecane Chemical compound CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 abstract description 3
- 238000000605 extraction Methods 0.000 abstract description 3
- 238000000638 solvent extraction Methods 0.000 abstract description 3
- 238000004090 dissolution Methods 0.000 abstract description 2
- 238000007873 sieving Methods 0.000 abstract description 2
- 238000004017 vitrification Methods 0.000 abstract description 2
- 238000001179 sorption measurement Methods 0.000 description 6
- 239000000428 dust Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000012958 reprocessing Methods 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229940094933 n-dodecane Drugs 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 230000002285 radioactive effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、使用済核燃料再処理工場から発生する廃ガス
中に含有されるルテニウムの除去方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for removing ruthenium contained in waste gas generated from a spent nuclear fuel reprocessing plant.
使用済核燃料再処理工場では、ウラン(U),プルトニ
ウム(P u)及び各種の核分裂生成物を含有する使用
済核燃料を濃硝酸に溶解し、トリブチルフォスフェート
(TBP)のn−ドデカン溶液でUとPuとを溶媒抽出
した後、再度希硝酸で逆抽出を行なう所謂ピュレックス
法によって処理されている。At a spent nuclear fuel reprocessing plant, spent nuclear fuel containing uranium (U), plutonium (Pu), and various fission products is dissolved in concentrated nitric acid, and then reprocessed using a n-dodecane solution of tributyl phosphate (TBP). The treatment is carried out by the so-called Purex method, in which after solvent extraction of and Pu is carried out, back extraction is performed again with dilute nitric acid.
上記工程においては、硝酸溶解時,廃液濃縮時及びガラ
ス,コンクリート等による濃縮廃液の固化処理時におい
て、NO2.NO等の窒素酸化物(NOx)や水分及び
ダストと共に核分裂生成物のうち揮発し易い元素主とし
て放射性ルテニウム(Ru)が混入したガスが発生する
。これらの廃ガスをサイクロン及びスクラバー等の乾式
及び湿式処理の後、シリカゲル等の吸着剤を充填した吸
着塔に通している。そして、上記N O x及びダスト
等は乾式及び湿式処理にてほとんど除去されるが、核分
裂生戒物含有の廃ガスはシリカゲル等の吸着剤によって
初めて除去される。In the above process, NO2. A gas containing radioactive ruthenium (Ru), which is an element that is easily volatile among nuclear fission products, is generated along with nitrogen oxides (NOx) such as NO, moisture, and dust. These waste gases are subjected to dry and wet treatment using cyclones and scrubbers, and then passed through an adsorption tower filled with an adsorbent such as silica gel. Although most of the above-mentioned N O x and dust are removed by dry and wet processing, waste gas containing fission products is only removed by an adsorbent such as silica gel.
〔発明が解決しようとする課題〕・
しかしながら、放射性Ruはシリカゲルに対して吸着量
が極めて低いので(例えば1gのR. uに対して4〜
5mg/g程度)、絶えず新しいシリカゲルに交換しな
ければならず、そのため大量の放射性廃棄物が発生し、
その処理及び保管が極めて大変であった。[Problem to be solved by the invention]- However, since the adsorption amount of radioactive Ru to silica gel is extremely low (for example, 4 to 1 g of Ru is adsorbed to silica gel).
5mg/g), and must be constantly replaced with new silica gel, which generates a large amount of radioactive waste.
Processing and storage were extremely difficult.
本発明は、上記問題点に鑑み、放射性廃棄物になるシリ
カゲルの発生量を低く抑えることのできる放射性廃ガス
中のルテニウムの除去方法を提供することを目的として
いる。SUMMARY OF THE INVENTION In view of the above-mentioned problems, an object of the present invention is to provide a method for removing ruthenium from radioactive waste gas, which can reduce the amount of silica gel generated as radioactive waste.
本発明による放射性廃ガス中のルテニウムの除去方法は
、使用済核燃料をピュレックス法を主体とした方法で処
理し、ウランとプルトニウムを回収すると同時に核分裂
生成物を分離し固化した後保管する工程に於いて、前記
工程で発生する廃ガス中の窒素酸化物組成を二酸化窒素
が主体となるように制御した後、該廃ガスをシリカゲル
に吸着させるようにした点に特徴がある。The method of removing ruthenium from radioactive waste gas according to the present invention involves processing spent nuclear fuel using a method mainly based on the Purex method, recovering uranium and plutonium, and at the same time separating and solidifying fission products, which are then stored. The process is characterized in that the composition of nitrogen oxides in the waste gas generated in the process is controlled so that nitrogen dioxide is the main component, and then the waste gas is adsorbed onto silica gel.
ピュレックス法を主体とした方法で処理する工程とは、
例えば、使用済核燃料の粉砕,篩別,濃硝酸による溶解
,トリブチルフォスフエートのn一ドデカン溶液による
溶媒抽出,希硝酸による逆抽出,放射性廃棄物のコンク
リート固化及びガラス固化等よりなる工程であり、上記
工程に使用される設備の他、廃ガス処理設備,廃液処理
設備等の付属設備を当然含むものである。そして、上記
工程に於いて発生する廃ガスとは、窒素酸化物(NOx
).水分,核分裂生戊物を含有する粉塵とガス及び主或
分である空気等からなるものである。又、通常の使用済
核燃料再処理工場での廃ガス組成調査によれば、二酸化
窒素濃度(NO2)と一酸化窒素濃度〔NO〕との比[
:NO.)/[NO]は約1/2であり、二酸化窒素(
NO2)が少ない。What is the process of processing using the Purex method as the main method?
For example, the process consists of pulverization of spent nuclear fuel, sieving, dissolution with concentrated nitric acid, solvent extraction with n-dodecane solution of tributyl phosphate, back extraction with dilute nitric acid, solidification of radioactive waste into concrete and vitrification, etc. In addition to the equipment used in the above process, it naturally includes auxiliary equipment such as waste gas treatment equipment and waste liquid treatment equipment. The waste gas generated in the above process refers to nitrogen oxides (NOx
). It consists of dust and gas containing moisture, fission products, and air, which is the main component. In addition, according to a survey of waste gas composition at a normal spent nuclear fuel reprocessing plant, the ratio of nitrogen dioxide concentration (NO2) to nitrogen monoxide concentration [NO] [
:NO. )/[NO] is approximately 1/2, and nitrogen dioxide (
NO2) is low.
そこで、本発明者等が廃ガス中の窒素酸化物中の[NO
z)の割合を増加させたところ、シリカゲルに吸着され
るRuの量が大幅に増加することが発見された。これは
、RuはNOxと複合化合物を形成してシリカゲルに吸
着されるものと思われ、N O xが多い程該複合化合
物の量が多くなることが原因であると思われる。実際本
発明方法を実施するにあたり、〔NO2〕/〔NO〕を
1/2を越えるようにすることが必要であり、より好ま
しくは1以上が好適である。窒素酸化物組成をNO2が
主体であるように制御する方法は通常の方法で良く、例
えば廃ガスを送る系内にN O 2を吹き込む方法やN
oを触媒等で酸化させてN O 2に変換する方法等が
挙げられる。NO2が主体である廃ガスは、一般の廃ガ
ス処理設備例えばサイクロンやスクラバーや電気集塵機
等でNOxを除去してNOxとして100ppm以上〜
50000ppm以下となるようにした後、シリカゲル
を充填した吸着塔に通気してRuを吸着させて除去する
。シリカゲル吸着塔は水分乾燥用のもので差し支えない
。Therefore, the present inventors investigated the effects of [NO] in nitrogen oxides in waste gas.
It was discovered that when the proportion of z) was increased, the amount of Ru adsorbed onto the silica gel increased significantly. This is thought to be because Ru forms a complex compound with NOx and is adsorbed on the silica gel, and the more NOx there is, the greater the amount of the complex compound. In practice, in carrying out the method of the present invention, it is necessary to make the ratio [NO2]/[NO] more than 1/2, and more preferably 1 or more. The nitrogen oxide composition can be controlled so that NO2 is the main component, such as by blowing NO2 into the waste gas delivery system or
Examples include a method of oxidizing o with a catalyst or the like to convert it into N O 2 . Waste gas consisting mainly of NO2 is treated with general waste gas processing equipment, such as cyclones, scrubbers, and electrostatic precipitators, to remove NOx to a level of 100 ppm or more as NOx.
After adjusting the concentration to 50,000 ppm or less, Ru is adsorbed and removed by venting into an adsorption tower filled with silica gel. A silica gel adsorption tower for water drying may be used.
内径25mm,高さ7 8 0 mmの吸着塔内にシリ
カゲルを充填し、この吸着塔内へ温度70°C,線速度
0.3m/’secで、RuをR u O 4の形態で
含む廃ガスを供給した。An adsorption tower with an inner diameter of 25 mm and a height of 780 mm was filled with silica gel, and waste containing Ru in the form of R u O 4 was introduced into the adsorption tower at a temperature of 70°C and a linear velocity of 0.3 m/'sec. Gas was supplied.
廃ガスの組成がN2 7 5〜8 0 v o 1.%
+0215〜20vol.%,水分4vol.%,NO
x2 0 0 0 0ppm ( (NO2
〕 / (No)=1/2),Rub.3■/Nlの
時にシリカゲルに吸着されたRuは、約4〜5■/gで
あったが、NOx組或をNOx 2 0 0 0 0
1)1)m ( (NO2 〕/ (No)=1/0)
とした時にシリカゲルに吸着されたRuは、約17〜1
8■/gであった。The composition of the waste gas is N2 75 to 80 v o 1. %
+0215~20vol. %, moisture 4vol. %,NO
x2 0 0 0 0ppm ((NO2
] / (No)=1/2), Rub. The amount of Ru adsorbed on silica gel was about 4 to 5 μ/g when the concentration was 3 μ/Nl, but the amount of Ru adsorbed on the silica gel was about 4 to 5 μ/g.
1) 1) m ((NO2) / (No) = 1/0)
The amount of Ru adsorbed on the silica gel is approximately 17 to 1
It was 8■/g.
従って、本発明方法によれば、Ruを含有する放射性廃
棄物としてのシリカゲルの発生量を大幅に減少させるこ
とができる。Therefore, according to the method of the present invention, the amount of silica gel generated as radioactive waste containing Ru can be significantly reduced.
〔発明の効果〕
上述のごとく、本発明による放射性廃ガス中ルテニウム
の除去方法によれば、放射性廃棄物になるシリカゲルの
発生量を低く抑えることのでき、従ってその処理及び保
管が容易になるという実用上極めて重要な利点を有して
いる。[Effects of the Invention] As mentioned above, according to the method for removing ruthenium from radioactive waste gas according to the present invention, the amount of silica gel that becomes radioactive waste can be suppressed to a low level, and therefore its processing and storage become easier. It has extremely important practical advantages.
Claims (1)
し、ウランとプルトニウムを回収すると同時に核分裂生
成物を分離し固化した後保管する工程に於いて、前記工
程で発生する廃ガス中の窒素酸化物組成を二酸化窒素が
主体となるように制御した後、該廃ガスをシリカゲルに
吸着させるようにした、放射性廃ガス中ルテニウムの除
去方法。In the process of processing spent nuclear fuel using a method mainly based on the Purex method, recovering uranium and plutonium, and at the same time separating and solidifying fission products and storing them, nitrogen oxidation occurs in the waste gas generated in the process. A method for removing ruthenium from radioactive waste gas, which comprises controlling the composition of the waste gas so that it is mainly composed of nitrogen dioxide, and then adsorbing the waste gas onto silica gel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15986089A JPH0324499A (en) | 1989-06-22 | 1989-06-22 | Removal of ruthenium in radioactive waste gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15986089A JPH0324499A (en) | 1989-06-22 | 1989-06-22 | Removal of ruthenium in radioactive waste gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0324499A true JPH0324499A (en) | 1991-02-01 |
Family
ID=15702807
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15986089A Pending JPH0324499A (en) | 1989-06-22 | 1989-06-22 | Removal of ruthenium in radioactive waste gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0324499A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030090454A (en) * | 2002-05-21 | 2003-11-28 | 박재원 | screw compound Pump, turbine inclined diffuser ystem |
US7300641B2 (en) * | 2003-02-10 | 2007-11-27 | Compagnie Generale Des Matieres Nucleaires | Method and device for capturing ruthenium present in a gaseous effluent |
KR101642948B1 (en) * | 2015-04-24 | 2016-07-26 | 한국전력기술 주식회사 | Off-shore floating power generation |
KR101642949B1 (en) * | 2015-04-24 | 2016-07-26 | 한국전력기술 주식회사 | Off-shore floating power generation |
-
1989
- 1989-06-22 JP JP15986089A patent/JPH0324499A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030090454A (en) * | 2002-05-21 | 2003-11-28 | 박재원 | screw compound Pump, turbine inclined diffuser ystem |
US7300641B2 (en) * | 2003-02-10 | 2007-11-27 | Compagnie Generale Des Matieres Nucleaires | Method and device for capturing ruthenium present in a gaseous effluent |
KR101642948B1 (en) * | 2015-04-24 | 2016-07-26 | 한국전력기술 주식회사 | Off-shore floating power generation |
KR101642949B1 (en) * | 2015-04-24 | 2016-07-26 | 한국전력기술 주식회사 | Off-shore floating power generation |
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