JP3365473B2 - Purification method of uranyl nitrate - Google Patents

Purification method of uranyl nitrate

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Publication number
JP3365473B2
JP3365473B2 JP32537496A JP32537496A JP3365473B2 JP 3365473 B2 JP3365473 B2 JP 3365473B2 JP 32537496 A JP32537496 A JP 32537496A JP 32537496 A JP32537496 A JP 32537496A JP 3365473 B2 JP3365473 B2 JP 3365473B2
Authority
JP
Japan
Prior art keywords
nitric acid
acid solution
uranyl nitrate
concentration
temperature
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 - Lifetime
Application number
JP32537496A
Other languages
Japanese (ja)
Other versions
JPH10167730A (en
Inventor
庸介 宮下
孝弘 近沢
建二 西村
純夫 山上
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Corp
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Publication date
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Priority to JP32537496A priority Critical patent/JP3365473B2/en
Publication of JPH10167730A publication Critical patent/JPH10167730A/en
Application granted granted Critical
Publication of JP3365473B2 publication Critical patent/JP3365473B2/en
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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

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  • Inorganic Compounds Of Heavy Metals (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明はウランを含む硝酸溶
液から硝酸ウラニル結晶を析出させ、回収する方法に関
する。更に詳しくは核燃料再処理工程等で生じるウラン
含有硝酸溶液から硝酸ウラニル結晶を析出・回収する硝
酸ウラニルの精製方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for precipitating and recovering uranyl nitrate crystals from a nitric acid solution containing uranium. More specifically, the present invention relates to a method for purifying uranyl nitrate in which a uranyl nitrate crystal is precipitated and recovered from a uranium-containing nitric acid solution generated in a nuclear fuel reprocessing step or the like.

【0002】[0002]

【従来の技術】従来、使用済核燃料の溶解液を氷点以下
に冷却して硝酸ウラニルを析出させ、回収する方法が知
られている。例えば、特公平6−31802号には、使
用済核燃料物質の再処理工程で回収されるウラン又はプ
ルトニウムのバッチ式純精製法において、硝酸ウラニル
水溶液が−10〜−35℃まで冷却されることが記載さ
れ、また特開平4−140698号には、ウラン・プル
トニウム混合溶液からのウラン及びプルトニウムの分離
方法において、硝酸ウラニル・硝酸プルトニウム混合溶
液が−20〜−40℃まで冷却されることが記載されて
いる。更に特開平4−218797号には使用済核燃料
の再処理方法において、使用済核燃料の溶解液が−10
〜−30℃まで冷却されることが開示されている。
2. Description of the Related Art Conventionally, a method is known in which a solution of a spent nuclear fuel is cooled to a temperature below the freezing point to deposit uranyl nitrate and recover it. For example, in Japanese Examined Patent Publication No. 6-31802, a uranyl nitrate aqueous solution is cooled to −10 to −35 ° C. in a batch pure purification method of uranium or plutonium recovered in a spent nuclear fuel material reprocessing step. JP-A-4-140698 describes a method for separating uranium and plutonium from a uranium-plutonium mixed solution, in which the uranyl nitrate-plutonium nitrate mixed solution is cooled to -20 to -40 ° C. ing. Further, in Japanese Patent Laid-Open No. 4-218797, in a method for reprocessing spent nuclear fuel, a dissolved liquid of spent nuclear fuel is -10.
It is disclosed to be cooled to ~ -30 ° C.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来方法
のいずれの場合においてもウランを含む硝酸溶液を氷点
以下の温度に冷却しなければならないため、大規模な冷
却装置が必要である。また氷点以下に冷却することで氷
や硝酸水和物が析出することがあり、そのため硝酸ウラ
ニル結晶の純度が低下し、その後の工程が複雑になる等
の問題点があった。本発明の目的は、大規模な冷却装置
を必要とせず、高純度な硝酸ウラニル結晶を高収率で回
収することができる硝酸ウラニルの精製方法を提供する
ことにある。
However, in any of the above-mentioned conventional methods, the nitric acid solution containing uranium must be cooled to a temperature below the freezing point, so that a large-scale cooling device is required. Further, cooling below the freezing point may cause precipitation of ice or nitric acid hydrate, which reduces the purity of the uranyl nitrate crystal and complicates subsequent steps. An object of the present invention is to provide a method for purifying uranyl nitrate, which does not require a large-scale cooling device and can recover highly pure uranyl nitrate crystals in high yield.

【0004】[0004]

【課題を解決するための手段】請求項1に係る発明は、
ウランを含む硝酸溶液を0〜25℃に保持し、硝酸溶液
の硝酸濃度を高めることによりこの硝酸溶液から硝酸ウ
ラニル結晶を析出させ、回収する硝酸ウラニルの精製方
法である。硝酸溶液を0〜25℃に保持して硝酸濃度を
高めると硝酸溶液中の硝酸ウラニルの溶解度が小さくな
り、硝酸ウラニル結晶が高収率で析出する。請求項2に
係る発明は、請求項1に係る発明であって、硝酸溶液に
60〜98%の高濃度硝酸を添加することにより硝酸溶
液の硝酸濃度を高める方法である。この方法によれば、
従来のように硝酸溶液を氷点以下に冷却することなく、
濃度調整の簡単な高濃度硝酸の添加操作により硝酸溶液
の硝酸濃度を容易に高めて硝酸ウラニル結晶を析出する
ことができる。
The invention according to claim 1 is
This is a method for purifying uranyl nitrate in which a nitric acid solution containing uranium is maintained at 0 to 25 ° C. and the nitric acid concentration of the nitric acid solution is increased to precipitate uranyl nitrate crystals from the nitric acid solution and recover the crystals. When the nitric acid solution is kept at 0 to 25 ° C. to increase the nitric acid concentration, the solubility of uranyl nitrate in the nitric acid solution becomes small, and uranyl nitrate crystals are deposited in high yield. The invention according to claim 2 is the invention according to claim 1, a method of increasing the nitric acid concentration of the nitric acid solution by adding a high concentration of nitric acid of 60 to 98 percent in nitric acid solution. According to this method
Without cooling the nitric acid solution below the freezing point as before,
It is possible to easily increase the nitric acid concentration of the nitric acid solution and precipitate the uranyl nitrate crystal by the operation of adding high-concentration nitric acid whose concentration is easily adjusted.

【0005】 請求項3に係る発明は、請求項1に係る発
明であって、この硝酸溶液を蒸発濃縮することにより硝
酸溶液の硝酸濃度を高めるとき、硝酸溶液の温度を0℃
近傍に保持する場合には、硝酸濃度を7〜8Nに高める
か、又は硝酸溶液の温度を25℃近傍に保持する場合に
は、硝酸濃度を4〜5Nに高める方法である。この方法
では従来のように硝酸溶液を氷点以下に冷却することな
く、また取扱いの難しい高濃度硝酸を使用せずに硝酸溶
液を蒸発濃縮することにより硝酸溶液の硝酸濃度を容易
に高めて硝酸ウラニル結晶を析出することができる。請
求項4に係る発明は、請求項1ないし3いずれか1項
係る発明であって、25℃よりも高い温度のウラン含有
硝酸溶液を冷却することにより0〜25℃の温度に保持
する方法である。この方法では冷却により硝酸ウラニル
の溶解度を低下させるとともに、硝酸溶液の濃度上昇に
より、更に効率的に常温で硝酸ウラニル結晶を析出する
ことができる。
The invention according to claim 3 is the invention according to claim 1, wherein when the nitric acid concentration of the nitric acid solution is increased by evaporating and concentrating the nitric acid solution, the temperature of the nitric acid solution is 0 ° C.
When maintaining near, increase nitric acid concentration to 7-8N
Or if the temperature of the nitric acid solution is kept near 25 ° C
Is a method of increasing the nitric acid concentration to 4 to 5N . In this method, the nitric acid solution can be easily concentrated to evaporate and concentrate without evaporating and concentrating the nitric acid solution without cooling the nitric acid solution below the freezing point and without using high-concentration nitric acid, which is difficult to handle. Crystals can be precipitated. The invention according to claim 4 is the invention according to any one of claims 1 to 3 , wherein the uranium-containing nitric acid solution having a temperature higher than 25 ° C is cooled to be maintained at a temperature of 0 to 25 ° C. Is. According to this method, the solubility of uranyl nitrate is lowered by cooling, and the concentration of nitric acid solution is increased, whereby uranyl nitrate crystals can be more efficiently precipitated at room temperature.

【0006】[0006]

【発明の実施の形態】本発明において、ウランを含む硝
酸溶液の硝酸濃度を高めるためには、硝酸溶液を0〜2
5℃に保持し、この硝酸溶液に60〜98%の高濃度硝
酸を添加するか、又は硝酸溶液を蒸発濃縮する。請求項
2〜4に係る発明において、硝酸溶液の保持温度が25
℃を越える場合には、硝酸ウラニルが結晶として析出し
にくく好ましくない。保持温度が0℃より低い場合に
は、従来と同様の問題点を生じる。硝酸溶液の温度を0
℃近傍に保持する場合には、硝酸濃度を7〜8Nに選択
すると、硝酸溶液中の硝酸ウラニルの溶解度が小さくな
り、回収率が高くなる。また硝酸溶液の温度を25℃近
傍に保持する場合には、硝酸濃度を4〜5Nに選択する
と、硝酸溶液中の硝酸ウラニルの溶解度が小さくなり、
回収率が高くなる。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, in order to increase the nitric acid concentration of a nitric acid solution containing uranium, the nitric acid solution is added to 0-2.
The temperature is kept at 5 ° C., and 60-98% highly concentrated nitric acid is added to the nitric acid solution, or the nitric acid solution is concentrated by evaporation. In the invention according to claims 2 to 4, the holding temperature of the nitric acid solution is 25.
If the temperature exceeds ° C, uranyl nitrate is not likely to precipitate as crystals, which is not preferable. If the holding temperature is lower than 0 ° C, the same problems as in the conventional case occur. The temperature of nitric acid solution is 0
If the nitric acid concentration is selected to be 7 to 8 N when the temperature is kept in the vicinity of 0 ° C., the solubility of uranyl nitrate in the nitric acid solution becomes small and the recovery rate becomes high. Further, when the temperature of the nitric acid solution is kept near 25 ° C., if the nitric acid concentration is selected to be 4 to 5 N, the solubility of uranyl nitrate in the nitric acid solution becomes small,
Higher recovery rate.

【0007】[0007]

【実施例】次に本発明の具体的態様を示すために、本発
明の実施例を説明する。 <実施例1> 硝酸ウラニルの硝酸溶液を50ml調製した。この硝酸
溶液は40℃においてウラン濃度622gU/l、硝酸
濃度2.2Nを有している。この温度40℃の硝酸溶液
を温度15℃の恒温槽に入れて同温度に保持した後、こ
の硝酸溶液に60%の硝酸を17.9ml添加し、撹拌
を続けたところ、硝酸ウラニルの結晶が析出した。その
後、析出した結晶と母液を濾過により分離した。母液の
硝酸濃度を測定したところ6.8Nまで増大していた。
得られた硝酸ウラニル結晶の回収率を下記の表1に示
す。
EXAMPLES Next, examples of the present invention will be described in order to show specific embodiments of the present invention. <Example 1> 50 ml of a nitric acid solution of uranyl nitrate was prepared. This nitric acid solution has a uranium concentration of 622 gU / l and a nitric acid concentration of 2.2 N at 40 ° C. This nitric acid solution at a temperature of 40 ° C. was placed in a constant temperature bath at a temperature of 15 ° C. and maintained at the same temperature. Then, 17.9 ml of 60% nitric acid was added to the nitric acid solution and stirring was continued. Precipitated. Then, the precipitated crystals and the mother liquor were separated by filtration. When the nitric acid concentration of the mother liquor was measured, it increased to 6.8N.
The recovery rate of the obtained uranyl nitrate crystals is shown in Table 1 below.

【0008】<実施例2> 硝酸ウラニルの硝酸溶液を50ml調製した。この硝酸
溶液は5℃においてウラン濃度293gU/l、硝酸濃
度2.0Nを有している。この温度5℃の硝酸溶液を温
度5℃の恒温槽に入れた後、この硝酸溶液に98%の硝
酸を11.5ml添加し、撹拌を続けたところ、硝酸ウ
ラニルの結晶が析出した。その後、析出した結晶と母液
を濾過により分離した。母液の硝酸濃度を測定したとこ
ろ7.0Nまで増大していた。得られた硝酸ウラニル結
晶の回収率を下記の表1に示す。
Example 2 50 ml of a nitric acid solution of uranyl nitrate was prepared. This nitric acid solution has a uranium concentration of 293 gU / l and a nitric acid concentration of 2.0 N at 5 ° C. This nitric acid solution at a temperature of 5 ° C. was placed in a constant temperature bath at a temperature of 5 ° C., 11.5 ml of 98% nitric acid was added to the nitric acid solution, and stirring was continued, whereby crystals of uranyl nitrate were precipitated. Then, the precipitated crystals and the mother liquor were separated by filtration. When the nitric acid concentration of the mother liquor was measured, it increased to 7.0N. The recovery rate of the obtained uranyl nitrate crystals is shown in Table 1 below.

【0009】<実施例3> 硝酸ウラニルの硝酸溶液を50ml調製した。この硝酸
溶液は5℃においてウラン濃度389gU/l、硝酸濃
度1.0Nを有している。この温度5℃の硝酸溶液を温
度5℃の恒温槽に入れた後、この硝酸溶液に98%の硝
酸を10.9ml添加し、撹拌を続けたところ、硝酸ウ
ラニルの結晶が析出した。その後、析出した結晶と母液
を濾過により分離した。母液の硝酸濃度を測定したとこ
ろ5.7Nまで増大していた。得られた硝酸ウラニル結
晶の回収率を下記の表1に示す。
Example 3 50 ml of a nitric acid solution of uranyl nitrate was prepared. This nitric acid solution has a uranium concentration of 389 gU / l and a nitric acid concentration of 1.0 N at 5 ° C. The nitric acid solution at a temperature of 5 ° C. was placed in a constant temperature bath at a temperature of 5 ° C., and 10.9 ml of 98% nitric acid was added to the nitric acid solution, and stirring was continued. As a result, crystals of uranyl nitrate were precipitated. Then, the precipitated crystals and the mother liquor were separated by filtration. When the nitric acid concentration of the mother liquor was measured, it increased to 5.7N. The recovery rate of the obtained uranyl nitrate crystals is shown in Table 1 below.

【0010】<実施例4> 硝酸ウラニルの硝酸溶液を50ml調製した。この硝酸
溶液は0℃においてウラン濃度414gU/l、硝酸濃
度1.1Nを有している。この温度0℃の硝酸溶液を温
度0℃の恒温槽に入れて同温度に保持した後、この硝酸
溶液に98%の硝酸を10.9ml添加し、撹拌を続け
たところ、硝酸ウラニルの結晶が析出した。その後、析
出した結晶と母液を濾過により分離した。母液の硝酸濃
度を測定したところ6.9Nまで増大していた。得られ
た硝酸ウラニル結晶の回収率を下記の表1に示す。
Example 4 50 ml of a nitric acid solution of uranyl nitrate was prepared. This nitric acid solution has a uranium concentration of 414 gU / l and a nitric acid concentration of 1.1 N at 0 ° C. This nitric acid solution at a temperature of 0 ° C. was placed in a constant temperature bath at a temperature of 0 ° C. and kept at the same temperature, and then 10.9 ml of 98% nitric acid was added to this nitric acid solution, and stirring was continued. Precipitated. Then, the precipitated crystals and the mother liquor were separated by filtration. When the nitric acid concentration of the mother liquor was measured, it increased to 6.9N. The recovery rate of the obtained uranyl nitrate crystals is shown in Table 1 below.

【0011】<実施例5> 硝酸ウラニルの硝酸溶液を100ml調製した。この硝
酸溶液は25℃においてウラン濃度206gU/l、硝
酸濃度2.3Nを有している。この硝酸溶液を昇温する
ことにより硝酸溶液の水分を蒸発し溶液を約50mlに
濃縮した。この硝酸溶液を温度25℃の恒温槽に入れて
同温度を保持した結果、硝酸ウラニルの結晶が析出し
た。その後、析出した結晶と母液を濾過により分離し
た。母液の硝酸濃度を測定したところ5.3Nまで増大
していた。得られた硝酸ウラニル結晶の回収率を下記の
表1に示す。
<Example 5> 100 ml of a nitric acid solution of uranyl nitrate was prepared. This nitric acid solution has a uranium concentration of 206 gU / l and a nitric acid concentration of 2.3 N at 25 ° C. By heating the nitric acid solution, the water content of the nitric acid solution was evaporated and the solution was concentrated to about 50 ml. This nitric acid solution was placed in a constant temperature bath at a temperature of 25 ° C. and kept at the same temperature, and as a result, crystals of uranyl nitrate were precipitated. Then, the precipitated crystals and the mother liquor were separated by filtration. When the nitric acid concentration of the mother liquor was measured, it increased to 5.3N. The recovery rate of the obtained uranyl nitrate crystals is shown in Table 1 below.

【0012】[0012]

【表1】 [Table 1]

【0013】表1から明らかなように、実施例1〜5の
いずれの場合においても、硝酸ウラニル結晶が50%以
上の高い回収率で得られた。
As is clear from Table 1, in any of Examples 1 to 5, uranyl nitrate crystals were obtained at a high recovery rate of 50% or more.

【0014】[0014]

【発明の効果】以上述べたように、本発明によれば、ウ
ランを含む硝酸溶液を0〜25℃に保持し、この硝酸溶
の硝酸濃度を高めることにより硝酸溶液から硝酸ウラ
ニル結晶を析出させ、回収するようにしたので、ウラン
を含む硝酸溶液を氷点以下に冷却することなく、硝酸ウ
ラニル結晶を高収率で回収することができる。従って、
ウランを含む硝酸溶液を氷点以下の温度に冷却しなけれ
ばならない従来の方法に比べて、大規模な冷却装置を必
要としない利点がある。また氷点以上の温度で硝酸ウラ
ニルを析出させるため、氷や硝酸水和物が析出すること
がなく高純度な硝酸ウラニル結晶が得られる。
As described above, according to the present invention, the nitric acid solution containing uranium is kept at 0 to 25 ° C.
Uranyl nitrate crystals were precipitated from the nitric acid solution by increasing the nitric acid concentration of the liquid and collected, so that it is possible to recover the uranyl nitrate crystals in a high yield without cooling the nitric acid solution containing uranium below the freezing point. You can Therefore,
Compared with the conventional method in which the nitric acid solution containing uranium must be cooled to a temperature below the freezing point, there is an advantage that a large-scale cooling device is not required. Further, since uranyl nitrate is precipitated at a temperature equal to or higher than the freezing point, highly pure uranyl nitrate crystals can be obtained without precipitation of ice or nitric acid hydrate.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 西村 建二 茨城県那珂郡那珂町大字向山字六人頭 1002番地の14 三菱マテリアル株式会社 那珂エネルギー研究所内 (72)発明者 山上 純夫 茨城県那珂郡那珂町大字向山字六人頭 1002番地の14 三菱マテリアル株式会社 那珂エネルギー研究所内 (56)参考文献 特開 平4−140698(JP,A) 特開 昭60−205398(JP,A) (58)調査した分野(Int.Cl.7,DB名) C01G 43/00 G21C 19/46 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Kenji Nishimura Inventor, Kenji Nishimura, Naka-machi, Naka-gun, Naka-gun, Ibaraki Prefecture, No. 1002, Mukaiyama, No. 14 14 No. 14 at Mitsubishi Materials Corporation, Naka Energy Laboratory (72) Inventor, Sumio Yamagami, Naka-gun, Ibaraki Prefecture Nakamachi, Oka, Mukaiyama, Rokujinto, No. 1002 14 14 Mitsubishi Materials Corporation, Naka Energy Laboratory (56) References JP-A-4-140698 (JP, A) JP-A-60-205398 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C01G 43/00 G21C 19/46

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ウランを含む硝酸溶液を0〜25℃に保
持し、前記硝酸溶液の硝酸濃度を高めることにより前記
硝酸溶液から硝酸ウラニル結晶を析出させ、回収する硝
酸ウラニルの精製方法。
1. A nitric acid solution containing uranium is kept at 0 to 25 ° C.
A method for purifying uranyl nitrate, which comprises holding and increasing the nitric acid concentration of the nitric acid solution to precipitate and recover uranyl nitrate crystals from the nitric acid solution.
【請求項2】 酸溶液に60〜98%の高濃度硝酸を
添加することにより前記硝酸溶液の硝酸濃度を高める請
求項1記載の精製方法。
2. A purification process according to claim 1, wherein increasing the nitric acid concentration of said nitric acid solution by adding a high concentration of nitric acid of 60 to 98 percent in nitric acid solution.
【請求項3】 酸溶液を蒸発濃縮することにより前記
硝酸溶液の硝酸濃度を高めるとき、前記硝酸溶液の温度
を0℃近傍に保持する場合には、前記硝酸濃度を7〜8
Nに高めるか、又は前記硝酸溶液の温度を25℃近傍に
保持する場合には、前記硝酸濃度を4〜5Nに高める
求項1記載の精製方法。
Wherein when increasing the nitrate concentration of the nitric acid solution by evaporation of the nitric acid solution, the temperature of the nitric acid solution
Is maintained near 0 ° C., the nitric acid concentration should be 7 to 8
Or increase the temperature of the nitric acid solution to around 25 ° C.
The refining method according to claim 1 , wherein the nitric acid concentration is increased to 4 to 5 N when it is held .
【請求項4】 25℃よりも高い温度のウラン含有硝酸
溶液を冷却することにより0〜25℃の温度に保持する
請求項1ないし3いずれか1項に記載の精製方法。
4. A 25 Purification process according to any one of claims 1 to 3 kept at a temperature of 0 to 25 ° C. by cooling the high temperature of the uranium-containing nitric acid solution than ° C..
JP32537496A 1996-12-05 1996-12-05 Purification method of uranyl nitrate Expired - Lifetime JP3365473B2 (en)

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