JPS60103029A - Method for recovering germanium - Google Patents

Method for recovering germanium

Info

Publication number
JPS60103029A
JPS60103029A JP58206749A JP20674983A JPS60103029A JP S60103029 A JPS60103029 A JP S60103029A JP 58206749 A JP58206749 A JP 58206749A JP 20674983 A JP20674983 A JP 20674983A JP S60103029 A JPS60103029 A JP S60103029A
Authority
JP
Japan
Prior art keywords
resin
germanium
soln
chelate resin
adsorbed
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
Application number
JP58206749A
Other languages
Japanese (ja)
Inventor
Yoshiaki Iwatani
岩谷 嘉昭
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP58206749A priority Critical patent/JPS60103029A/en
Publication of JPS60103029A publication Critical patent/JPS60103029A/en
Pending legal-status Critical Current

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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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To recover Ge especially from a strongly acidic leaching soln. in a high yield by bringing a chelate resin having specified functional groups into contact with a soln. contg. Ge to allow Ge to be adsorbed on the resin and by eluting the adsorbed Ge. CONSTITUTION:A chelate resin having oxine ligands in the molecule such as a resin prepd. by reacting a styrene-divinylbenzene copolymer with halomethylated oxine is brought into contact with a soln. contg. Ge such as a leaching soln. of <=2pH after the treatment of zinc ore with sulfuric acid to allow Ge to be adsorbed on the chelate resin. The chelate resin is then treated with an aqueous soln. of NaOH or the like to elute the adsorbed Ge. The chelate resin is much superior to a conventional known ion exchange resin or iminodiacetic acid type chelate resin in power of selectively adsorbing Ge in an acidic aqueous soln. of <=2pH. It has physical, chemical and mechanical stabilities and can be repeatedly used by regeneration.

Description

【発明の詳細な説明】 本発明は、ゲルマニウムを含有する溶液からゲルマニウ
ムを回収する方法に関するものであり、さらに詳しくば
配位子として分子中にオキシンを有するキレート樹脂を
用いて強酸性液中のゲルマニウムを回収する方法に閏す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for recovering germanium from a solution containing germanium, and more specifically, the present invention relates to a method for recovering germanium from a solution containing germanium. This is a method for recovering germanium.

ゲルマニウムは、現在多くの分野において利用されてお
り1例えば半導体、赤外光学。
Germanium is currently used in many fields, such as semiconductors and infrared optics.

繊維光学、T−線粒子検出、触媒、医薬及びポリマー化
学の分野において用いられている。
It is used in the fields of fiber optics, T-ray particle detection, catalysis, medicine and polymer chemistry.

しかしながら、高品位のゲルマニウム鉱石は極めて少な
いので11M界で回収されているゲルマニウムのほとん
どば1亜iiL 銅+ f+iからの副産物としてであ
る。特に亜1:j)の製造においては、ゲルマニウムの
濃度が比較的高いこと、及びゲルマニウムが電解液から
除去されていないと後の電1す1″二1−程での電流動
率か著しく低下するごとにより、前もって脱ゲルマニウ
ム処理を11・)のが通常である。
However, high-grade germanium ores are extremely rare, and most of the germanium recovered in the 11M field is as a by-product from 12L copper+f+i. Particularly in the production of electrolyte (1:j), the concentration of germanium is relatively high, and if germanium is not removed from the electrolyte, the current mobility in the subsequent electrodes will be significantly reduced. Depending on the process, it is usual to carry out degermanization treatment in advance (11).

従来より、2I;、−/iの硫酸酸性lu出液からゲル
マニウムをうt’ i”j1回収する方法としてば7タ
ンニンにより沈f)ひしまたのち、塩酸処理し、范留操
作によりJ′!1.1化り−ルマニウムとして回収する
方法が採られ−C′いる。しかしながら、この方法は操
作が11常に繁1:Iiであり、工程に伴うケルマニラ
、/A C)) lil失1)大きいことから、近年は
Conventionally, a method for recovering germanium from a sulfuric acid acidic lu effluent of 2I; A method has been adopted to recover 1.1 rumanium as rumanium.However, this method requires a lot of operations, and the loss of kermanila and /A C) lil associated with the process is large. Therefore, in recent years.

液々抽出に、1、る方法が注目され広く研究されている
。例えば、トリブチルホスフェート長幀アルキル”ノ′
ミン、アルキルリン酸、子スフィン酸、ヒドロキサム酸
、ヒドロキシオキシム、アルキルピロカテコール及びオ
キシン誘導体などの溶媒抽出剤を使用してゲルマニウム
を分離回収する方法が提案されている(例えば特公昭5
B−9134号公報、特開昭聞−9817号公報、特開
昭58−31048号公報等)。これらの方法は、大変
興味のあるものではあるが、抽出剤のゲルマニウムに対
する選択性が乏しかったり、長時間繰り返し使用時に置
換基の分解が起きて抽出能力が低下したり、又はそれら
の価格が卵重に高いこと等の理111により、未だ工業
的に満足されたものではない。
One method for liquid-liquid extraction has attracted attention and has been widely studied. For example, tributyl phosphate Nagahora alkyl
Methods have been proposed for separating and recovering germanium using solvent extractants such as amine, alkyl phosphoric acid, sulfinic acid, hydroxamic acid, hydroxyoxime, alkyl pyrocatechol, and oxine derivatives (for example,
B-9134, JP-A-9817, JP-A-58-31048, etc.). Although these methods are very interesting, they have problems such as poor selectivity of the extractant for germanium, decomposition of substituents during repeated use over a long period of time, resulting in a decrease in extraction ability, or their price is low. Due to reasons 111 such as being extremely expensive, it has not yet been industrially satisfied.

本発明者は、これらの実状に鑑み、」二記不都合を克服
したゲルマニウムの回収方法を1に供することを目的と
して鋭意研究を重ねノこ結果、特定の官能基を有するキ
レ−1−樹脂を用いると、特に酸性浸出液のゲルマニウ
ムが極めて効率よく回収されることを見いだし3本発明
に到達した。
In view of these circumstances, the present inventor has conducted intensive research with the aim of providing a method for recovering germanium that overcomes the disadvantages mentioned in 2. As a result, the present inventor has developed a Kir-1-resin having a specific functional group. It has been found that germanium, especially from acidic leachate, can be recovered very efficiently by using this method, and the present invention has been completed.

すなわち本発明は配位子として分子−中にオキシンを自
する”1−1/−ト樹脂とゲルマニウムを含量jするl
′みl^とを接触させて該キレ−1・樹脂にゲル′l二
・”)hを吸着さ−せ9次いで吸着させたゲルマニ・°
ツノ、を溶離させることを特徴とするゲルマ−1″r、
l、の回収方法である。
That is, the present invention uses a ``1-1/-'' resin containing oxine as a ligand in the molecule and a germanium content j.
The gel is adsorbed onto the resin by contacting with the gel mani.
gelmer-1″r, characterized in that it elutes horns;
This is a method of collecting l.

本発明り二用いし−)れるキレート樹脂としては。The chelate resins used in the present invention include:

配位子、シシ、−(うtJ’中にオキシンを有するキレ
−1樹脂であ、(I、ば、特に制限されるものではない
It is a Kir-1 resin having oxine in the ligand, Shishi, -(UtJ', and (I, B) is not particularly limited.

このよ・)Z住1−]・ 1・樹脂としては1例えばス
チレン ジし、−ルヘンゼン共重合体に代表される交さ
結合のビニル芳香族共重合体にハロメチル化A−1ソン
を反応させた樹脂、交さ結合のビニル、名’ N’+/
IS:共重合体をジアゾ化もしくはハロメチル化したの
ち、オキシンを反応させて得られる(^1脂、クロロメ
チル基、スルホニルクIIリド)、(、カルボニルクロ
リド基。
1. As the resin, for example, styrene is reacted with a cross-linked vinyl aromatic copolymer typified by the -Rhenzene copolymer with halomethylated A-1. resin, cross-bonded vinyl, name 'N'+/
IS: (^1 fatty acid, chloromethyl group, sulfonyl chloride), (carbonyl chloride group) obtained by diazotizing or halomethylating a copolymer and then reacting it with oxine.

イソシアナ 1. J、I;、エポキシ基、アルデヒド
基等アミンとIy’、 Ili;、する基を有するスチ
レン−ジビニル−・ン1:ンJ’: ilr 合体、 
フェノール樹脂。
Isocyanana 1. Styrene-divinyl-1:n J': ilr combination with amines such as J, I;, epoxy group, aldehyde group, etc., Iy', Ili;,
Phenolic resin.

ポリエチレン、ポリ塩化ビニル、ポリメタクリル酸等の
重合体(以下アミン反応性基を有する重合体と称す)に
アミノ化オキシンを反応させてflられる樹脂、前記ア
ミン反応性基を有する重合体に、アンモニア、エチレン
ジアミン、ジエチレントリアミン、トリエチレンテトラ
ミン、ヘキザメチレンジアミン、グアニジン等のアミン
化合物を反応させてf!? /::重合体中に1級もし
くは2級のアミノ貼を白するアミノ化重合体に、クロロ
メチル基、スルボニルクロリド基、カルボエルクl:1
リド基。
A resin obtained by reacting an aminated oxine with a polymer such as polyethylene, polyvinyl chloride, or polymethacrylic acid (hereinafter referred to as a polymer having an amine-reactive group), or a polymer having an amine-reactive group, ammonia , reacting amine compounds such as ethylenediamine, diethylenetriamine, triethylenetetramine, hexamethylenediamine, and guanidine to form f! ? /:: Chloromethyl group, sulfonyl chloride group, carboerc l:1 to the aminated polymer that whitens the primary or secondary amino group in the polymer.
Lido group.

イワシアナ−1〜基、エポキシ基、アルデヒド基等アミ
ンと反応する基を有するオキシン誘導体を反応さセて得
られる樹脂、アクリル酸−ジビニルベンゼン共重合体、
メタクリル−ジビニルベンゼン共重合体をジアゾ化した
のち、オキシンと反応させて得られる樹脂、ビニルオキ
シンとエチレン系不飽和化合物2例えばスチレン、ジビ
ニルヘンゼン、アクリル酸エステル、エチレングリコー
ルジメタクリレートとを共重合体して得られる樹脂、オ
キシンもしくはメ;1−シン誘導体と、フLノール類及
びポルJz ’J’ルデヒド類との重縮合により得られ
る樹flit等があげられる。
A resin obtained by reacting an oxine derivative having a group that reacts with an amine such as a sardine-1 group, an epoxy group, an aldehyde group, an acrylic acid-divinylbenzene copolymer,
A resin obtained by diazotizing a methacrylic-divinylbenzene copolymer and then reacting it with oxine, a resin obtained by copolymerizing vinyloxine and an ethylenically unsaturated compound 2 such as styrene, divinylbenzene, acrylic ester, or ethylene glycol dimethacrylate. Examples include resins obtained by combining oxine or me;1-syn derivatives with flit, which is obtained by polycondensation with fluorols and pol Jz 'J' aldehydes.

上記のオニ1ビニ・又はその誘導体としては。As the above-mentioned oni 1 vinyl or its derivatives.

例えば、8−1=、、 lIIキシキノリン(オキシン
)。
For example, 8-1=, lII xyquinoline (oxine).

2−メチル 811・1コキシキノリン(2−メチルオ
キソン)、2−エチル−8−ヒドロキシキノリン、2−
rI−プロピル−8−ヒドロキシキノリン、2−イソ−
プロピル−8−ヒドロキシキノリン、2−n−ブチル−
8−ヒトロキシギノリン、2 LarL−ブチル−8−
!ニド1コキシキノリン、5−クロル−8−ヒドロキシ
キノリン、5−ブロム−8−ヒドロキシキノリン、2−
メチル−5−クロル−8−ヒドロキシキノリン等があげ
られ、その中でも、8−ヒl:1:Iキシキノリン、2
−メチル−8−ヒドロキシキノリンが好ましく、特に8
−ヒトし+SlSlキシリンが好ましい。
2-Methyl 811.1koxyquinoline (2-methyloxone), 2-ethyl-8-hydroxyquinoline, 2-
rI-propyl-8-hydroxyquinoline, 2-iso-
Propyl-8-hydroxyquinoline, 2-n-butyl-
8-Hydroxyginoline, 2 LarL-butyl-8-
! Nido-1koxyquinoline, 5-chloro-8-hydroxyquinoline, 5-bromo-8-hydroxyquinoline, 2-
Examples include methyl-5-chloro-8-hydroxyquinoline, among which 8-hyI:1:I xyquinoline, 2
-Methyl-8-hydroxyquinoline is preferred, especially 8-hydroxyquinoline.
- Human+SlSl xylin is preferred.

このオキシンをイ「するキレ−1・樹脂を製造するには
1例えばJornal of Organic che
mis−try、 43巻、 3151−3157頁、
 1978年、 PolymerScience、U、
S、S、R,20巻+ 、53’2 、54Q Uj’
、 。
To produce a resin that removes this oxine, for example, Journal of Organic Che.
mis-try, volume 43, pages 3151-3157,
1978, PolymerScience, U.
S, S, R, 20 volumes +, 53'2, 54Q Uj'
, .

1978年に記載されζいる方法に従って行えばよ(、
il常は適度に架橋三次元化した樹脂を有機溶媒に膨潤
させたのち、触媒もしくは脱酸剤の存在下に、オキシン
又はその誘導体を反応させることにより製造することが
できる。
Follow the method described in 1978 (
Usually, it can be produced by swelling an appropriately crosslinked three-dimensional resin in an organic solvent and then reacting it with oxine or a derivative thereof in the presence of a catalyst or a deoxidizing agent.

本発明で対象とするゲルマニウムを含有する溶液として
は9通常、pH2以下の酸性溶液があげられるが、もち
ろん他のゲルマニウムを含有する78液であっても適用
することができる。そのような具体例としては、亜鉛鋳
二の酸性浸出液、もしくは亜鉛製錬残渣の酸性浸出液が
あげられるが、これらの溶液は通常亜鉛を大量に含有す
るp112以下の硫酸酸性溶液である。
The germanium-containing solution that is the object of the present invention is usually an acidic solution with a pH of 2 or less, but of course other germanium-containing solutions can also be used. Specific examples of such solutions include acidic leachates of zinc castings or acidic leachates of zinc smelting residues; these solutions are usually acidic sulfuric acid solutions with a p112 or lower content containing a large amount of zinc.

本発明の方法を実施するには、まず上記のキレート樹脂
とゲルマニウムを含有する溶流とを接触させてキレート
樹脂にゲルマニウムを吸着させる。そのためには1通常
イオン交換樹脂による方法と同様にハツチ法及びカラム
法が用いられイlが、カラム法で行う方が片作上有利で
ある。カラム法で行う場合には。
To carry out the method of the present invention, first, the above chelate resin is brought into contact with a solution containing germanium to adsorb germanium onto the chelate resin. For this purpose, the hatch method and the column method are usually used as well as the method using an ion exchange resin, but the column method is more advantageous in terms of monolithic production. When using the column method.

樹脂を塔に充jQ L、 、ゲルマニウムを含有する溶
液を空間連速(1時間当たり、樹脂容積の何倍量の液を
処理したかを示すもの)0.5〜5hr”、温1朝’l
’;’I ’1品ないしは60’(4こ設定してダウン
フローQ、二より通l(lさせればよい。
Fill the column with the resin and heat the germanium-containing solution at a continuous rate (indicating how many times the volume of the resin is processed per hour) for 0.5 to 5 hours, warm for 1 morning. l
';'I '1 item or 60' (Set 4 items, downflow Q, 2 twists 1 (1).

次にゲルマニウムを吸着したキレート樹脂からゲルマニ
・″ツム’k ?”6 X[させるには9例えば。
Next, from the chelate resin that has adsorbed germanium, germanium ``Tsum'k?'' 6X [For example, 9.

キレート樹脂をi’ /l・、カリ金属の水酸化物水溶
液を用いて処理”1ればよく1例えば0.1〜5モル/
1.々酉1.1.<ば1〜4モル/βカセイソーダ、カ
セ・イノノリなどのアルカリ水溶液が溶凡11剤とし°
(用いられる。
The chelate resin is treated with an aqueous potash metal hydroxide solution at i'/l.
1. Rooster 1.1. <1 to 4 mol/β An alkaline aqueous solution such as caustic soda, kase, and inonori is used as a dissolving agent.
(Used.

以上説明した11.・)に1本発明はキレート樹脂によ
る方法Cあろので、簡単な操作で、しかも効率よくゲル
−lニウムを回収することができる。さCpに本発明に
用いられるキレート樹脂は従来公知のイオン交換樹脂や
イミノジ酢酸型キレート樹脂に比較してpH2以下の酸
性水溶液中でゲルマニウムに対して選1)シ吸、17性
が著しく優れているので、ゲルマニラJいり外に1例え
ば亜鉛、カドミウム、コバルト。
11. explained above. (1) Since the present invention uses method C using a chelate resin, gel-lium can be recovered efficiently with simple operations. In addition, the chelate resin used in the present invention has significantly superior 1) absorption and 17 properties for germanium in an acidic aqueous solution with a pH of 2 or less compared to conventionally known ion exchange resins and iminodiacetic acid type chelate resins. Therefore, Gel Manila J is required for example zinc, cadmium, and cobalt.

鉄、ヒ素及びニッケルなどが共存するM (’L 溶液
からでもゲルマニウムを選択的に回収することができる
という効果も有する。また1本発明に用いられるキレー
ト樹脂は、物理的。
It also has the effect of being able to selectively recover germanium even from M('L) solutions in which iron, arsenic, nickel, etc. coexist.

化学的及び機械的安定にも優れており、樹脂を再生する
ことにより何回でも使用することができるので、その工
業的価値は大なるものである。
It has excellent chemical and mechanical stability, and can be used many times by regenerating the resin, so its industrial value is great.

以下実施例により本発明をさらに具体的に説明する。な
お参考例及び実施例中の%は−・jべて重量%を示す。
The present invention will be explained in more detail with reference to Examples below. In addition, % in Reference Examples and Examples indicates weight % in total.

参考例1 市販のスチレンージビニルベンゼンノい口合体(ジビニ
ルベンゼン/3molθ%)10.(11!にニトロヘ
ンゼン150m1を加えて膨潤さ−Vk後。
Reference Example 1 Commercially available styrene-divinylbenzene composite (divinylbenzene/3 mol θ%) 10. (After adding 150ml of nitrohenzene to 11! and swelling -Vk.

次いでごの糸1:ツjj[水塩化アルミニウム1.3g
と5−り101メ1−ルー8−ヒドロキシキノリン塩酸
塩23 、01! 、!:を添加し、80℃で24時間
反応させた。
Next, thread 1: Tsujj [aluminum chloride hydrate 1.3 g
and 5-ri 101 me-1-ru 8-hydroxyquinoline hydrochloride 23, 01! ,! : was added and reacted at 80°C for 24 hours.

反応路J′ik 、 lJ:Jj、別し、水とメタノー
ルで洗浄したの’)、4%カセイソーダ水?′8液で中
和処理し、続いて1分に水洗することにより。
Reaction path J'ik, lJ: Jj, separated and washed with water and methanol'), 4% caustic soda water? ' By neutralizing with liquid 8 and then washing with water for 1 minute.

目的とする;l’i−1樹脂を得た。The desired l'i-1 resin was obtained.

参考例2 市販のス千Lノンージビニルベンゼン共重合体(ジビニ
ル−、ンビン3 mole% )10.0gを50m1
の濃硫酸番、二’:’; /ll□11下で浸清し、こ
の混合物を50°C以下にLi2”)なから5濃硝酸と
濃硫酸との濃酸(1: l Vol/Vol ) 25
m1を1時間要して滴下し二1−1I化し7た。反応終
了後5氷水中に混合物を〆1い(生成物を単離した。つ
いで、ごの?」、成1シ1j・5(11<の塩化第1ず
ずを100m1の濃塩酸&:二l’+i°かじた溶媒中
に入れ、徐々に昇温し、最鈴的に5+1”cで3時間反
応させてアミノ化した。Jy応終f1&、氷水中に混合
物を注いで生成物を単離した。十分るこ水洗したのち、
乾燥してスチレンージビニルヘンセンノI、重合体のア
ミノ化物1(1,7gを得た。
Reference Example 2 10.0 g of commercially available non-divinylbenzene copolymer (divinyl, 3 mole%) was added to 50 m1
of concentrated sulfuric acid, 2':'; ) 25
m1 was added dropwise over a period of 1 hour to form 21-1I. After the reaction was completed, the mixture was poured into ice water (the product was isolated). The temperature was gradually raised, and the reaction was finally carried out for 3 hours at 5+1"c for amination. At the end of the reaction, the mixture was poured into ice water to isolate the product. I let go. After washing thoroughly with water,
After drying, 1.7 g of styrene-divinylhensenno I and polymer aminated product 1 were obtained.

このアミノ化物にジメチルボルムアミl” 5(iml
を加えて膨潤させたのら、5−クロI、1〕f−ルー8
−ヒドロキシキノリン塩酸基23.014を添加し、9
0℃で5時間反応さ−Uた。反応路r後、参考例1と同
様にして単離し、目的と一4゛るキレート樹脂を得た。
To this aminated product, add dimethylborumamyl 5 (iml
After adding and swelling, 5-chlor I, 1]f-ru 8
- Adding 23.014 hydroxyquinoline hydrochloride groups, 9
The reaction was carried out at 0°C for 5 hours. After the reaction was completed, it was isolated in the same manner as in Reference Example 1 to obtain a desired chelate resin.

参考例3 市販のスチレン−ジビニルベンゼン共iF合体(ジビニ
ルヘンゼン3mole%)1.O,Ogにクロロメチル
エーテル30gを加えて膨潤さセた後、テ1−ラクロル
エタン12.5’gを加え、シ1コいて粉末状無水塩化
アルミニウム10.0gを61に度が5°Cを越えない
ようにして徐々に加えたのち、0〜5℃で2時間反応さ
せてクロロメチル化した。反応終了後、氷水「1弓こ反
応物を投入し、黒色の樹脂球が黄色に変化するまで浸漬
し、水、アセトンにて十分に洗浄しノこのし。
Reference Example 3 Commercially available styrene-divinylbenzene co-iF combination (divinylbenzene 3 mole%)1. After adding 30 g of chloromethyl ether to O. After gradually adding the mixture without exceeding the temperature, the mixture was reacted at 0 to 5°C for 2 hours to effect chloromethylation. After the reaction is complete, add the reactant to ice water and soak until the black resin sphere turns yellow, then rinse thoroughly with water and acetone.

減圧下で乾j%’4し、’i−,I(i、ORの樹脂を
得た。
It was dried under reduced pressure to obtain a resin of 'i-,I(i,OR).

このりIIJ l:I)Iル化スチレンージしやニルヘ
ンゼン共屯合体t、−ジメヂルボルムアミド5Qm 1
を加えて膨潤さ−1)ノこのら、b−アミノ−8−ヒト
ロキシ゛トノリン15.6 gと炭酸ソー ダ5.3g
とを添加し、 8!i’(:で4時間反応させた。反応
終了後、参−8例1と同様にしCt)罵1Fシ、目的と
するキレ−1・1へ1脂をiソた。
Consolidation IIJ l:I) I-dylated styrene disilane and nilhenzen covalent t,-dimethylborumamide 5Qm 1
-1) These were swollen by adding 15.6 g of b-amino-8-hydroxytonolin and 5.3 g of soda carbonate.
and 8! The reaction was allowed to proceed for 4 hours with i' (:). After the reaction was completed, the same procedure as in Example 1 was carried out.

参考例4 8−ヒ1−ロキシキノリン14.5 [を8.0%水酸
化ブーI〜リウム水ン容ン皮75gに多’f Iikさ
せ、37%ホルマリン32.4gを25〜30℃下で滴
下すると均一な溶液がi:1られたので、そのまま30
℃で10分攪拌を続り1初期生成物を冑た。この初期生
成物に、レゾルシン11.0 gを8.0%水酸化す1
ヘリウJ・水溶11ン75Hに溶解した水溶液。
Reference Example 4 8-H-1-roxyquinoline 14.5 was added to 75 g of 8.0% hydroxide solution and 32.4 g of 37% formalin was heated at 25 to 30°C. When added dropwise, a homogeneous solution was obtained at i:1, so the
Stirring was continued for 10 minutes at 0.degree. C. to remove the initial product. To this initial product, 11.0 g of resorcin was 8.0% hydroxylated.
An aqueous solution dissolved in Heliu J.Aqueous 11-75H.

ポリエチレンイミン(分子量1,800) 3.6g及
び37%ポルマリン水溶液32.4gを添加して30℃
で20分攪1’l’ L、て反応液を冑た。この反応液
をパークレンを溶剤として富法により水を透水に留去し
つつパール重縮合を行うと、小球状に架橋三次元化した
。樹脂が得られた。
Add 3.6 g of polyethyleneimine (molecular weight 1,800) and 32.4 g of a 37% Polmarine aqueous solution and heat at 30°C.
The reaction mixture was stirred for 20 minutes at 1'l' L, and the reaction solution was cooled down. When this reaction solution was subjected to pearl polycondensation using perchloromethane as a solvent and water was distilled off while water was being distilled off, the product was crosslinked into small spheres in three-dimensional form. A resin was obtained.

この樹脂を水洗浄したのら、4.0%塩酸で処理し、水
洗後、4.0%水酸化すトリウ入水溶液で中和処理し2
次いで十分に水洗することにより、目的とするキレート
樹脂を得た。
After washing this resin with water, it was treated with 4.0% hydrochloric acid, and after washing with water, it was neutralized with an aqueous solution containing 4.0% tritonium hydroxide.
Next, the desired chelate resin was obtained by sufficiently washing with water.

実施例1 ゲルマニウム、i2!JL銅、二ノゲル2ゲル及びヒ素
イオンをそれぞれloOmg/j!含白するp++ 0
.5の硫酸酸性溶液50m1に参考例1へ・4で製造さ
れたキレート樹脂を湿潤状態で各々1.0ml添加し、
振とうさせなから25”Cで2脂1時間接触させたのち
、処理液中の各種金属イオンの温度を原子吸光光度法に
より測定した。
Example 1 Germanium, i2! loOmg/j of JL copper, Ninogel 2 gel and arsenic ion, respectively! Whitening p++ 0
.. Add 1.0 ml each of the chelate resins produced in Reference Examples 1 and 4 to 50 ml of the sulfuric acid acidic solution of No. 5 in a wet state,
After contacting the two resins for 1 hour at 25"C without shaking, the temperature of various metal ions in the treatment solution was measured by atomic absorption spectrophotometry.

その結果、第2鉄、銅、コノゲル2曲鉛及びヒ素イオン
の濃度は処理前とほぼ同一で5)0〜100 ml/ 
12であったが、ゲルマニウム・イオンの濃度は、いず
れの樹脂を用いた場合も5mg/β以下で1回収率は9
5%であった。
As a result, the concentrations of ferric iron, copper, Conogel 2 bent lead, and arsenic ions were almost the same as before treatment5) from 0 to 100 ml/
However, the germanium ion concentration was less than 5 mg/β and the recovery rate was 9 when using any resin.
It was 5%.

なお、比較のため、市販のイミノジ酢酸型キレート樹脂
(樹脂1々)体、スチレンージビニルヘンゼンjい11
合体)を用い、同様にして処理したとごノ1.残存する
ゲルマニウムイオンの濃度は40町X/Cで2回収率は
60例であった。
For comparison, commercially available iminodiacetic acid type chelate resin (resin 1), styrene-divinylhenzen 11
1. was processed in the same manner using The concentration of remaining germanium ions was 40% X/C, and the recovery rate was 60 cases.

これより、A、2明に用いられるキレート樹脂は、低p
H領b(c、−、をンい゛乙ケルマニウムイオンのみを
選択的6.′回収できることが明らかである。
From this, the chelate resin used for A and 2 Ming has a low p
It is clear that only kermanium ions can be selectively recovered in the H region b(c, -, -).

実施例2 参考例14こ土ツノ〕(11られだキレ−1−する(脂
30+n lヲ内t’J 9 mmの力”ノスカラムに
充填し、各々10(1m+;/ 7!のり″ルマニウム
、第2鉄、銅、ニアう−ル、jJ14]1)J壺と):
ヒ素イオンを含有するpHO17ノ硫((J、 (’+
Q t’l ?’j1?I’j−を(時間&: 60m
 1(7) 速度(Sv211r−1)ごjlli i
’& した。
Example 2 Reference Example 14 Earth horns] (11 dirt horns) (30 + nl of t'J 9 mm of force were filled in the column, each 10 (1 m +; / 7! glue) Rumanium, Ferric iron, copper, near wool, jJ14] 1) J pot):
pHO17nosulfur containing arsenic ions ((J, ('+
Qt'l? 'j1? I'j-(Time &: 60m
1 (7) Speed (Sv211r-1)
'& did.

その結果、第2鉄、銅、ニッケル、亜鉛及びヒ素イオン
4.1.. lA+脂容積に対して1〜5倍9にに1洩
(I nIIX/’ Eをもって漏洩濃度とした。
As a result, ferric, copper, nickel, zinc and arsenic ions 4.1. .. The leakage concentration was defined as 1 to 5 times 9 to 1A + fat volume (InIIX/'E).

したのに対し7゛乙ゲルマニウムイオンは樹脂容積に対
して4 (l (+’i m、 31:では漏洩しなか
った′。
On the other hand, germanium ions did not leak when the resin volume was 4 (+'i m, 31:).

次にゲルマニウムを吸着したキレ−L 4A4 fli
tを水洗し、樹脂容積に対して3倍量の1696(4モ
ル)カセイソーダ水溶液をSV21+r−、’で通液し
たところ、ゲルマニウムが1.3g含むカセイソーダ水
溶液が得られた。
Next, Kirei-L 4A4 fli which adsorbed germanium
t was washed with water, and a 1696 (4 mol) aqueous solution of caustic soda of 3 times the volume of the resin was passed through the resin at SV21+r-,', thereby obtaining an aqueous solution of caustic soda containing 1.3 g of germanium.

実施例3 参考例2により得られたキレート4R1脂:t(1ml
を内径9mmのガラスカラムに充填し、ゲルマニウムを
含有するpif−0,5の硫酸酸性/8液を1時間に6
0m lの速度(SV 2 hr−’ )で通液した。
Example 3 Chelate 4R1 fat obtained in Reference Example 2: t (1 ml
was packed into a glass column with an inner diameter of 9 mm, and a sulfuric acid acidic/8 solution of pif-0,5 containing germanium was added at 6 times per hour.
The solution was passed at a rate of 0 ml (SV 2 hr-').

その結果、樹脂容積に対して60倍M処理i々も、流出
液中のゲルマニウムイオンは50m+H/Il以下であ
った。
As a result, the germanium ions in the effluent were less than 50 m+H/Il even after each treatment with M of 60 times the resin volume.

なお、ゲルマニウム含有溶液の液組成り、1次の通りで
あった(Ge (IV) 500mg/ (1,Zn5
00mg/ 12 、 pH0,5)次にゲルマニウム
を吸着したキレ−+1Δ1脂を水洗し、樹脂容積に対し
て4倍量の12%(3モル)カセイソーダ水溶液をSV
 2 hr−’で1ffl液したところ、ゲルマニウム
が5g含むカセイソータ゛水ンl’i’ W<がj:/
られた。
The composition of the germanium-containing solution was as follows (Ge(IV) 500mg/(1,Zn5
00mg/12, pH 0.5) Next, the germanium-adsorbed Kire-+1Δ1 fat was washed with water, and a 12% (3 mol) caustic soda aqueous solution was added in an amount 4 times the resin volume by SV.
When I poured 1 ffl solution in 2 hours, I found that the caustic soda water containing 5 g of germanium l'i'W< is j:/
It was done.

実h1!i例4 参考例Iに、j、すtrIられたキレ−1・樹脂20m
 lを内径1)m…φのガラスカラムに充填し、塔頂よ
りC++(lν) 211fハII+!/β、Zn33
.000mg/ (lを含むptlo、5の+jiL 
f’IQ 酸性78液を1時間に50m lの速度(S
V 2.5br” ) −(:’>U&シタ。
Real h1! i Example 4 Kiri-1 resin 20m with j and strI applied to Reference Example I
A glass column with an inner diameter of 1) m...φ is filled with C++(lν) 211f HII+! from the top of the column. /β, Zn33
.. 000mg/(ptlo including l, +jiL of 5
f'IQ Acidic 78 liquid at a rate of 50 ml per hour (S
V 2.5br") -(:'>U&Sita.

その結果、1δI脂体積に対して20倍量処理後も、流
出lt’を中θ月1(・(1ν)の濃度は5mg/β以
下であっノこ。
As a result, even after treatment in an amount 20 times the volume of 1δI fat, the concentration of 1 (·(1ν)) in the outflow lt' was less than 5 mg/β.

次にゲルマ−い’/ Jzを吸着したキレ−1・樹脂を
水洗し、 1’、I脂1“1′積に対して3倍量の12
%(3モル)力トイソーダ水溶l皮をSV21+r″1
で通液したと・−7′)、ゲルマニウムが1.4g含む
カセイソー〃゛水〆11液が得られた。
Next, wash the Kirei-1 resin that has adsorbed Gelmar'/Jz with water, and add 3 times the amount of 12
% (3 moles) of toy soda water solution SV21+r″1
When the solution was passed through the solution, 11 liquids containing 1.4 g of germanium were obtained.

Claims (1)

【特許請求の範囲】[Claims] (1)配位子として分子中にオキシンを有するキレート
樹脂とゲルマニウムを含量jする溶液とを接触させて該
キレート樹脂にゲルマニウムを吸着させ1次いで吸着さ
せたゲルマニウムを溶舗させることを1(11徴とする
ゲルマニウムの回収方法。
(1) The process of contacting a chelate resin having oxine as a ligand in its molecule with a solution having a germanium content j, adsorbing germanium onto the chelate resin, and then melting the adsorbed germanium. A method for recovering germanium.
JP58206749A 1983-11-01 1983-11-01 Method for recovering germanium Pending JPS60103029A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58206749A JPS60103029A (en) 1983-11-01 1983-11-01 Method for recovering germanium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58206749A JPS60103029A (en) 1983-11-01 1983-11-01 Method for recovering germanium

Publications (1)

Publication Number Publication Date
JPS60103029A true JPS60103029A (en) 1985-06-07

Family

ID=16528457

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58206749A Pending JPS60103029A (en) 1983-11-01 1983-11-01 Method for recovering germanium

Country Status (1)

Country Link
JP (1) JPS60103029A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60145914A (en) * 1983-12-30 1985-08-01 Dowa Mining Co Ltd Recovery of germanium
JPS60166225A (en) * 1984-02-10 1985-08-29 Dowa Mining Co Ltd Method of recovery of germanium
CN103866124A (en) * 2014-04-16 2014-06-18 六盘水中联工贸实业有限公司 Method for extracting germanium from germanium-containing acidic solution by using TiO2.nH2O

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60145914A (en) * 1983-12-30 1985-08-01 Dowa Mining Co Ltd Recovery of germanium
JPH0243686B2 (en) * 1983-12-30 1990-10-01 Dowa Kogyo Kk
JPS60166225A (en) * 1984-02-10 1985-08-29 Dowa Mining Co Ltd Method of recovery of germanium
JPH0339013B2 (en) * 1984-02-10 1991-06-12 Dowa Kogyo Kk
CN103866124A (en) * 2014-04-16 2014-06-18 六盘水中联工贸实业有限公司 Method for extracting germanium from germanium-containing acidic solution by using TiO2.nH2O
CN103866124B (en) * 2014-04-16 2016-01-20 六盘水中联工贸实业有限公司 One TiO 2nH 2o extracts the method for germanium from germanic acidic solution

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