Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6053160B2 - How to extract uranium from seawater - Google Patents
[go: Go Back, main page]

JPS6053160B2 - How to extract uranium from seawater - Google Patents

How to extract uranium from seawater

Info

Publication number
JPS6053160B2
JPS6053160B2 JP3034077A JP3034077A JPS6053160B2 JP S6053160 B2 JPS6053160 B2 JP S6053160B2 JP 3034077 A JP3034077 A JP 3034077A JP 3034077 A JP3034077 A JP 3034077A JP S6053160 B2 JPS6053160 B2 JP S6053160B2
Authority
JP
Japan
Prior art keywords
adsorbent
uranium
seawater
magnetic
magnetic separator
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
Application number
JP3034077A
Other languages
Japanese (ja)
Other versions
JPS53115601A (en
Inventor
義弘 小澤
寿生 山下
一紀 藤田
瀞士 武内
史登 中島
千秋 前小屋
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.)
Hitachi Ltd
Original Assignee
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP3034077A priority Critical patent/JPS6053160B2/en
Publication of JPS53115601A publication Critical patent/JPS53115601A/en
Publication of JPS6053160B2 publication Critical patent/JPS6053160B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Drilling And Exploitation, And Mining Machines And Methods (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 本発明は海水中のウランを吸着採取する方法に関し、
更に詳しくは海水と接触後の吸着剤を磁気分離法を用い
て回収することを特徴とする海水中ウランの採取方法に
関する。
[Detailed description of the invention] The present invention relates to a method for adsorbing and collecting uranium in seawater,
More specifically, the present invention relates to a method for collecting uranium in seawater, which is characterized in that an adsorbent that has come into contact with seawater is recovered using a magnetic separation method.

海水中には約仙億トンのウランが溶存している。 Approximately 100 million tons of uranium is dissolved in seawater.

しカル海水中のウラン濃度は約3.3μg/eときわめ
て低く、膨大な量の海水を吸着剤と接触させる必要があ
る。海水と吸着剤とを接触させる方式を大別すると3つ
に分けられる。第1は吸着剤を固定床につめ、これに海
水を通す方法、第2は吸着剤を担持させたシート等を海
水中に設置し接触させる方法、第3は吸着剤を細かいス
ラリー状にして海水と接触させる方式である。第1の方
法は細かい粒子状吸着剤は圧力損失が大きくなるので採
用できず、したがつて比較的大きな粒子を使用するため
吸着量はあまり大きくならない。また海水中の砂とか他
の固形物で吸着床が目づまりを起こす可能性も強い。第
2の方法は海水との接触に問題があつて、長時間吸着体
を海水中に浸しておかなければならず、吸着量も他に比
べて大きいとは言えない。これに対し第3の方法は粒径
の細かい吸着剤を用いるため吸着剤gあたりの吸着量も
他の2方法に比較して大きくなる。従来の方法ては海水
と接触後、吸着剤の回収を沈降槽を用いて行なつている
。しかしこの方法では沈降に長時間を要しかつ非常に大
きな沈降槽が必要になる。しかも吸着剤の回収率を10
0%にすることは困難でウラン採取量が減少しかつ海洋
汚染の恐れもある。本発明の目的は磁性を有するウラン
吸着剤を海水と接触させた後、吸着剤を磁気分離法によ
つて効率良く回収し、かつ吸着剤からウランを脱着させ
る装置及び方法を提供することにある。
The uranium concentration in seawater is extremely low, approximately 3.3 μg/e, and it is necessary to bring a huge amount of seawater into contact with the adsorbent. The methods of bringing seawater and adsorbent into contact can be roughly divided into three types. The first method is to pack the adsorbent in a fixed bed and pass seawater through it, the second method is to place a sheet etc. carrying the adsorbent in seawater and bring it into contact with it, and the third method is to make the adsorbent into a fine slurry. This method involves contacting with seawater. In the first method, a fine particulate adsorbent cannot be used because the pressure loss becomes large, and therefore relatively large particles are used, so the amount of adsorption is not very large. There is also a strong possibility that the adsorption bed will become clogged with sand or other solid matter in the seawater. The second method has problems with contact with seawater, requiring the adsorbent to be immersed in seawater for a long period of time, and the amount of adsorption cannot be said to be large compared to other methods. On the other hand, since the third method uses an adsorbent with a fine particle size, the amount of adsorption per gram of adsorbent is also larger compared to the other two methods. In the conventional method, after contact with seawater, the adsorbent is recovered using a sedimentation tank. However, this method requires a long time for settling and requires a very large settling tank. Moreover, the recovery rate of the adsorbent is 10
It is difficult to reduce the amount of uranium to 0%, and there is a risk that the amount of uranium extracted will decrease and there will be marine pollution. An object of the present invention is to provide an apparatus and method for bringing a magnetic uranium adsorbent into contact with seawater, then efficiently recovering the adsorbent by a magnetic separation method, and desorbing uranium from the adsorbent. .

スラリー方式で効率良くウランを回収するには(1)接
着剤のウラン吸着量が大きいこと。
In order to efficiently recover uranium using the slurry method, (1) the adhesive must have a large amount of uranium adsorbed;

また吸着速度が速いこと。(2)吸着剤を効率よく回収
できること。などが望まれる。(1)に関しては、含水
酸化チタン系吸着剤では、gあたりのウラン吸着量は粒
子の見かけ上の外表面積に比例すると報告されている。
(菅野他;日本原子力学会誌VOl.l2、NO.ll
97O)したがつて粒子を細かくすればする程、g吸着
剤あたりのウラン吸着量を大きくすることができる。し
かし(2)の観点から、粒子径を小さくすることは問題
が多い。従来の沈降法によつて吸着剤を効率良く沈降回
収できる粒子径は100μmが限度である。また遠心分
離機を使つて粒子を回収する方法も考えられるが、処理
海水量が膨大なため実用化に問題がある。これに対し磁
気分離法を用いた場合、吸着剤の粒子径をさらに小さく
できること、したがつてウラン吸着量を大幅に増加でき
ること。また磁気分離法は大量の海水を処理する上で問
題がない。磁気分離法で磁気粒子の捕獲限界寸法は、磁
性粒子に働く磁界の吸引力と粒子を取除こうとする流体
圧力や重力などの力との釣合いによつて決定される。マ
グネタイトが1/1唱合された含水酸化チタン・鉄複合
吸着剤の場合KOlm−MarstOn型大勾配磁気分
離機(HGMS)では、第1図に示す通り、粒子径1p
mまで捕獲可能となる。(内山、応用物理VOl.45
sNO.2.l976) 吸着剤の粒径を100pmから1pmまで小さくするこ
とによつて、吸着剤1gあたりのウラン吸着量を10皓
と飛躍的に向上させることができる。
Also, the adsorption speed is fast. (2) The adsorbent can be efficiently recovered. etc. is desired. Regarding (1), it has been reported that in hydrous titanium oxide adsorbents, the amount of uranium adsorbed per gram is proportional to the apparent outer surface area of the particles.
(Sugano et al.; Journal of the Atomic Energy Society of Japan VOl.l2, No.ll
97O) Therefore, the finer the particles, the greater the amount of uranium adsorbed per g adsorbent. However, from the viewpoint of (2), there are many problems in reducing the particle size. The particle size for which adsorbents can be efficiently sedimented and recovered using conventional sedimentation methods is limited to 100 μm. Another option is to collect the particles using a centrifuge, but the amount of seawater that must be processed is enormous, making it difficult to put this into practice. On the other hand, when magnetic separation is used, the particle size of the adsorbent can be further reduced, and the amount of uranium adsorbed can therefore be significantly increased. Furthermore, the magnetic separation method has no problems in treating large amounts of seawater. In the magnetic separation method, the capture limit size of magnetic particles is determined by the balance between the attractive force of the magnetic field acting on the magnetic particles and the forces such as fluid pressure and gravity that try to remove the particles. In the case of a hydrous titanium oxide/iron composite adsorbent in which magnetite is mixed at 1/1, the particle size is 1p in the KOlm-MarstOn type large gradient magnetic separator (HGMS), as shown in Figure 1.
It is possible to capture up to m. (Uchiyama, Applied Physics Vol. 45
sNO. 2. 1976) By reducing the particle size of the adsorbent from 100 pm to 1 pm, the amount of uranium adsorbed per 1 g of adsorbent can be dramatically increased to 10 μm.

また吸着剤に吸着されたウランは炭酸アンモン溶液など
の脱着液で溶離でき、吸着剤は再使用できる。
Moreover, the uranium adsorbed on the adsorbent can be eluted with a desorption solution such as ammonium carbonate solution, and the adsorbent can be reused.

本発明を要約すると (1)磁性吸着剤を海水と接触させた後、ウランを吸着
した吸着剤を磁気分離によつて海水から分離回収し、1
段または複数段でウランを溶離せしめることを特徴とす
る海水中ウラン採取方法。
To summarize the present invention, (1) after bringing a magnetic adsorbent into contact with seawater, the adsorbent adsorbing uranium is separated and recovered from the seawater by magnetic separation;
A seawater uranium extraction method characterized by eluting uranium in one or more stages.

(2)磁気分離で磁性吸着剤を分離回収するのに磁気分
離フィルターによつて吸着剤をフィルター内に捕獲した
後、脱着液を磁気分離フィルター内に送り吸着剤中のウ
ランを溶離することを特徴とするウラン脱着方法。
(2) To separate and recover the magnetic adsorbent using magnetic separation, the adsorbent is captured in the filter using a magnetic separation filter, and then the desorption liquid is sent into the magnetic separation filter to elute the uranium in the adsorbent. Characteristic uranium desorption method.

(3)ウラン脱着後、吸着剤を水洗した後、磁気フィル
ターの磁場を切り、フィルターで捕獲された吸着剤を逆
洗して脱離し、再使用に供する方法。
(3) After uranium desorption, the adsorbent is washed with water, the magnetic field of the magnetic filter is turned off, and the adsorbent captured by the filter is backwashed and desorbed for reuse.

が得られる。is obtained.

以下本発明の実施例について詳細に説明する。Examples of the present invention will be described in detail below.

第2図は発明の概略を示すフローシートである。海水は
海水入口3から攪拌槽1に導入される。一方磁性吸着剤
は吸着剤投入口4から海水中に供給され、攪拌器2で混
合される。吸着剤が海水中のウランを吸着した後、バル
ブ6およびバルブ7を開いて、吸着剤を含む海水を磁気
分離機5に送り、磁気分離フィルター17に生ずる大勾
配磁界によつてフィルター17内に磁性吸着剤を捕獲す
る。次にバルブ6,7を閉じ、バルブ8,9を開けて、
ウラン脱着液、例えば数%の炭酸アンモニウム溶液を通
して吸着剤に吸着されたウランを溶離させる。脱着液を
できるだけ少なくして、脱着液中のウラン濃度を高める
ため、脱着液入口13と脱着液出口14間を結んで数回
磁気フィルター内を脱着液を通しても良い。最終的には
脱着液出口14から高濃度5ウラン溶液を取り出す。ウ
ランを吸着剤から脱着させた後、グルブ8,9をしめ、
バルブ10,11を開けて逆洗液入口15から逆洗水を
通す。この時磁気分離フィルター14の磁界を切ること
によつて、磁気分離フィルター14内に捕獲された吸着
剤は逆洗水によつて容易に磁気分離フィルター14から
脱離され吸着剤導入管16を通つて、海水へ再び供給さ
れる。第3図は、磁気分離機を2台並列に設けて、ウラ
ンの吸着および脱着を連続的におこなわせたものである
。第4図は、磁気分離機118で捕獲されたウランを吸
着した吸着剤から、ウランを脱着させると同時に磁気分
離フィルターの磁界を切ることによつて吸着剤を磁気分
離フィルターから脱離させ、これを磁気分離機■で回収
する。
FIG. 2 is a flow sheet outlining the invention. Seawater is introduced into the stirring tank 1 from the seawater inlet 3. On the other hand, the magnetic adsorbent is supplied into the seawater from the adsorbent inlet 4 and mixed by the stirrer 2. After the adsorbent adsorbs uranium in seawater, valves 6 and 7 are opened to send the seawater containing the adsorbent to the magnetic separator 5, where it is absorbed into the filter 17 by the large gradient magnetic field generated in the magnetic separation filter 17. Capture magnetic adsorbent. Next, close valves 6 and 7, open valves 8 and 9,
The uranium adsorbed on the adsorbent is eluted through a uranium desorption fluid, such as a few percent ammonium carbonate solution. In order to reduce the amount of desorption liquid as much as possible and increase the uranium concentration in the desorption liquid, the desorption liquid may be passed through the magnetic filter several times by connecting the desorption liquid inlet 13 and the desorption liquid outlet 14. Finally, the high concentration 5 uranium solution is taken out from the desorption liquid outlet 14. After desorbing uranium from the adsorbent, close grooves 8 and 9,
Open the valves 10 and 11 and let the backwash water pass through the backwash liquid inlet 15. At this time, by turning off the magnetic field of the magnetic separation filter 14, the adsorbent captured in the magnetic separation filter 14 is easily desorbed from the magnetic separation filter 14 by backwash water and passes through the adsorbent introduction pipe 16. Then, it is fed back into the seawater. In Figure 3, two magnetic separators are installed in parallel to continuously adsorb and desorb uranium. FIG. 4 shows that uranium is desorbed from the adsorbent that has adsorbed uranium captured by the magnetic separator 118, and at the same time, the magnetic field of the magnetic separation filter is cut to remove the adsorbent from the magnetic separation filter. is recovered using a magnetic separator ■.

必要ならば脱着液を磁気分離機■に二くり返し通すこと
によつて、脱着液中ウラン濃度を高めることができる。
なお磁気分離機1からの吸着剤からの脱離はごく短時間
で終了するので、半連続的に磁気分離機1で海水中の吸
着剤を回収することが可能てある。第5図は比較的粒径
の大きな吸着剤に適するもので、粒子径が100pm以
上で、マグネタイトのような強磁性体の場合、小さな磁
界でも回収可能であるため主に永久磁石を用いたドラム
型磁気分離機が適用される。吸着剤を含んだ海水がドラ
ム型磁気分離機20の上部から供給される。回転ドラム
22の内側に設けた永久磁石21によつて磁性吸着剤は
回転ドラム上を移動し、海水と分離されて、脱着層23
に送られる。ここでウランは吸着剤から溶離されとり出
される。一方吸着剤は再便用にまわされる。第6図は広
範囲の粒径を持つた吸着剤の回収に適用されるもので、
比較的大きな粒径の吸着剤は沈降槽24で沈降させ、沈
降しない小さな粒径の吸着剤を大勾配磁気分離によつて
回収するものてあり、磁気分離機の負荷を小さくできる
If necessary, the uranium concentration in the desorption solution can be increased by passing the desorption solution through the magnetic separator (2) twice.
Note that since the desorption from the adsorbent from the magnetic separator 1 is completed in a very short time, it is possible to semi-continuously recover the adsorbent in seawater using the magnetic separator 1. Figure 5 is suitable for adsorbents with relatively large particle sizes; in the case of particles with a particle size of 100 pm or more and a ferromagnetic material such as magnetite, it is possible to collect them even in a small magnetic field, so drums using permanent magnets are mainly used. type magnetic separator is applied. Seawater containing adsorbent is supplied from the top of the drum-type magnetic separator 20. The magnetic adsorbent moves on the rotating drum by a permanent magnet 21 provided inside the rotating drum 22, is separated from the seawater, and forms a desorption layer 23.
sent to. Here, the uranium is eluted and extracted from the adsorbent. On the other hand, the adsorbent is used for reconsumption. Figure 6 is applicable to the recovery of adsorbents with a wide range of particle sizes.
The adsorbent with a relatively large particle size is allowed to settle in the sedimentation tank 24, and the adsorbent with a small particle size that does not settle is recovered by large gradient magnetic separation, thereby reducing the load on the magnetic separator.

沈降槽24底部に沈積した吸着剤はスラリーポンプ25
に移送され、脱着層2゛3で処理される。本発明は吸着
剤の回収に磁気分離法を適用することによつて、吸着剤
の粒子の大きさを従来に比べ格段と小さくでき、したが
つて吸着剤1gあたりのウラン吸着量を飛躍的に増加さ
せることは明白で、海水中ウランの採取および低濃度ウ
ラン溶液からのウランの採取に非常に有効である。
The adsorbent deposited at the bottom of the sedimentation tank 24 is removed by a slurry pump 25.
and treated with a desorption layer 2-3. By applying a magnetic separation method to the collection of adsorbent, the present invention can significantly reduce the particle size of the adsorbent compared to conventional methods, thereby dramatically increasing the amount of uranium adsorbed per gram of adsorbent. This increase is obvious and is very effective for extracting uranium from seawater and from low-concentration uranium solutions.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は磁気分離によつて捕獲される粒子径と誘導磁化
の関係図、第2図は海水中ウランの採取装置の基本図、
第3図は連続的にウランの吸着、脱着を行なう場合の、
第4図は吸着剤中のウランと吸着剤の磁気分離フィルタ
ーからの脱離を同時におこなわせる場合の、第5図は粒
径が比較的大きな吸着剤を回収する場合の、第6図は沈
降と磁気による分離を併用して吸着剤を回収する場合の
装置系統図を示す。 1・・・・・・攪拌槽、2・・・・・・攪拌器、3・・
・・・・海水入口、4・・・・・・吸着剤投入口、5・
・・・・・磁気分離機、6●◆●●バルブ19710…
●バルブ2、8111バルブ3、9・・・・・・バルブ
牡10・・・・・・バルブ5、11・・・・・・バルブ
6、12・・・・・・海水出口、13・・・・・・脱着
液入口、14・・・・・・脱着液出口、15・・・・・
逆洗液入)口、16・・・・・・吸着剤導入管、17・
・・・・・磁気分離フィルター、18・・・・・磁気分
離機1、19・・・・・・磁気分離機■、20・・・・
・・ドラム型磁気分離機、21・・・・・永久磁石、2
2・・・・・・回転ドラム、23・・・・・・脱着層、
24・・・・・・沈降槽、25・・・・・・スラリーポ
ンプ。
Figure 1 is a diagram of the relationship between particle size captured by magnetic separation and induced magnetization, Figure 2 is a basic diagram of a seawater uranium extraction device,
Figure 3 shows the case in which uranium is adsorbed and desorbed continuously.
Figure 4 shows the case where uranium in the adsorbent and the adsorbent are desorbed from the magnetic separation filter at the same time, Figure 5 shows the case where adsorbent with relatively large particle size is recovered, and Figure 6 shows the case of sedimentation. A system diagram of the system is shown in which the adsorbent is recovered using a combination of magnetic separation and magnetic separation. 1... Stirring tank, 2... Stirrer, 3...
...Seawater inlet, 4...Adsorbent inlet, 5.
...Magnetic separator, 6●◆●●Valve 19710...
●Valve 2, 8111 Valve 3, 9... Male valve 10... Valve 5, 11... Valve 6, 12... Seawater outlet, 13... ... Desorption liquid inlet, 14 ... Desorption liquid outlet, 15 ...
Backwash liquid inlet) port, 16... Adsorbent inlet pipe, 17.
...Magnetic separation filter, 18...Magnetic separator 1, 19...Magnetic separator ■, 20...
...Drum type magnetic separator, 21...Permanent magnet, 2
2... Rotating drum, 23... Desorption layer,
24... Sedimentation tank, 25... Slurry pump.

Claims (1)

【特許請求の範囲】 1 海水中ウランを採取するに当り、磁性を有する吸着
剤を海水と接触後、磁気分離機を用いて前記の吸着剤を
捕獲しウランを採取することを特徴とする海水中ウラン
の採取方法。 2 特許請求の範囲第1項において磁性を有する吸着剤
を磁気分離機内にとどめたまま、ウランの脱着液を前記
吸着剤に接触せしめることを特徴とするウランの採取方
法。 3 特許請求の範囲第1項において吸着剤回収用磁気分
離機を並列に設置し、第1の磁気分離機で吸着剤を海水
中から回収している間に、第2の磁気分離機内の吸着剤
に吸着されたウランを脱着することを特徴とする海水中
ウランの採取方法。 4 特許請求の範囲第1項において第1の磁気分離機内
に捕獲されたウランを吸着した吸着剤を、ウラン脱着液
で逆洗して当該磁気分離機から前記吸着剤を脱離させ、
つぎに第2の磁気分離機に前記吸着剤を捕獲させ、ウラ
ン脱着液でウランを溶離することを特徴とするウランの
採取方法。 5 海水中ウランを吸着剤を用いて採取するに当り、磁
性を有する吸着剤を海水と接触後、吸着剤を含む海水を
沈降槽に導き、該沈降槽下部より粒子の大きい吸着剤を
回収し、沈降槽上部より、粒子の小さい吸着剤を含む海
水を磁気分離機に導き、吸着剤を磁気分離機で回収する
ことを特徴とする海水中ウランの採取方法。
[Scope of Claims] 1. Seawater characterized in that when extracting uranium from seawater, a magnetic adsorbent is brought into contact with seawater, and then a magnetic separator is used to capture the adsorbent and extract uranium. How to extract middle uranium. 2. A method for extracting uranium according to claim 1, characterized in that a uranium desorption liquid is brought into contact with a magnetic adsorbent while the adsorbent remains in a magnetic separator. 3 In claim 1, magnetic separators for adsorbent recovery are installed in parallel, and while the first magnetic separator is recovering adsorbent from seawater, the adsorption in the second magnetic separator is A method for collecting uranium from seawater, which is characterized by desorbing uranium adsorbed by a reagent. 4. In claim 1, the adsorbent adsorbing uranium captured in the first magnetic separator is backwashed with a uranium desorption liquid to desorb the adsorbent from the magnetic separator,
A method for collecting uranium, characterized in that the adsorbent is then captured by a second magnetic separator and the uranium is eluted with a uranium desorption solution. 5. When collecting uranium from seawater using an adsorbent, after the magnetic adsorbent comes into contact with seawater, the seawater containing the adsorbent is led to a sedimentation tank, and the adsorbent with large particles is collected from the bottom of the sedimentation tank. A method for collecting uranium in seawater, which is characterized by introducing seawater containing adsorbent with small particles into a magnetic separator from the upper part of a sedimentation tank, and recovering the adsorbent with the magnetic separator.
JP3034077A 1977-03-22 1977-03-22 How to extract uranium from seawater Expired JPS6053160B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3034077A JPS6053160B2 (en) 1977-03-22 1977-03-22 How to extract uranium from seawater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3034077A JPS6053160B2 (en) 1977-03-22 1977-03-22 How to extract uranium from seawater

Publications (2)

Publication Number Publication Date
JPS53115601A JPS53115601A (en) 1978-10-09
JPS6053160B2 true JPS6053160B2 (en) 1985-11-22

Family

ID=12301087

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3034077A Expired JPS6053160B2 (en) 1977-03-22 1977-03-22 How to extract uranium from seawater

Country Status (1)

Country Link
JP (1) JPS6053160B2 (en)

Also Published As

Publication number Publication date
JPS53115601A (en) 1978-10-09

Similar Documents

Publication Publication Date Title
US4284511A (en) Process for using magnetically ballasted sorbents
JP6358520B1 (en) Soil purification system
JP6358519B1 (en) Soil purification system
US20210346822A1 (en) Methods and systems for recovery of valuable target species from brine solutions
JPH0531477A (en) Method for removing metal contaminants from solid materials utilizing contact with ion exchange powder
JP6399326B1 (en) Soil purification system
JP7300119B2 (en) soil purification system
Yamashita et al. Extraction of uranium from seawater using magnetic adsorbents
CN106622104A (en) Method for treating heavy metal ion-containing wastewater by using high-iron fly ash
CN110961248B (en) A method for separating scandium and uranium from scandium-containing uranium ore
JPS6053160B2 (en) How to extract uranium from seawater
JP3814263B2 (en) Separation and recovery of iron and manganese coexisting in water
RU2088534C1 (en) Powder sorbent for collecting petroleum, oil and other hydrocarbons
JPS5939163B2 (en) Composite magnetic adsorbent for uranium
Navratil Pre-analysis separation and concentration of actinides in groundwater using a magnetic filtration/sorption method I. Background and concept
Hoffner et al. Washing processes for disperse particulate systems–process spectrum and aspects for the process choice
JP6134892B2 (en) Method for producing silica / polymer composite type iminodiacetic acid chelate adsorbent, quantitative analysis method using silica / polymer composite type iminodiacetic acid chelate adsorbent, and method for recovering trace metal elements
JP3334067B2 (en) Magnetic separation device and water treatment device with magnetic separation device
CN207877833U (en) The extraction system of rhenium element in a kind of wet process iron-smelting copper spent acid
CN113387527B (en) Treatment method of bottom mud with heavy metal and organic compound pollution
EA037278B1 (en) Removal of organic solvents from aqueous process streams
CN223263540U (en) Filter aid for mud water sample
CN119838745B (en) Tin recovery method of secondary tailings
US12214363B2 (en) Method for separating fine particles in soil using cationic magnetic nanoparticles
JPS6044964B2 (en) Method for collecting particles captured by magnetic separator