JPS5891035A - Metallic ion extracting reagent and extracting method - Google Patents

Metallic ion extracting reagent and extracting method

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Publication number
JPS5891035A
JPS5891035A JP18692481A JP18692481A JPS5891035A JP S5891035 A JPS5891035 A JP S5891035A JP 18692481 A JP18692481 A JP 18692481A JP 18692481 A JP18692481 A JP 18692481A JP S5891035 A JPS5891035 A JP S5891035A
Authority
JP
Japan
Prior art keywords
group
ions
gold
formula
water
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
JP18692481A
Other languages
Japanese (ja)
Inventor
Chiyuki Fujii
千之 藤井
Seiichi Watanabe
誠一 渡辺
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP18692481A priority Critical patent/JPS5891035A/en
Publication of JPS5891035A publication Critical patent/JPS5891035A/en
Pending legal-status Critical Current

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  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

PURPOSE:To separate ions of Cu, Ag, Au, a Pt group metal or Hg contained in an aqueous soln. from other various metallic ions by extraction at a high extraction rate by bringing the soln. into contact with a slightly water-soluble phase contg. chlorobutenyl-tertiary-amine in an acidic range. CONSTITUTION:An aqueous soln. contg. ions of Cu, Ag, Au or a Pt group metal and/or Hg is brought into contact with a slightly water-soluble phase contg. chlorobutenylamine at 2-6pH to separate said ions from other various metallic ions by extraction. The concn. of ions of Cu or the like in the aqueous soln. can be reduced to <= about 1ppm. Said chlorobutenylamine is represented by formulaI(where Y is CH3CCl=CHCH2- and/or CH3CCH=CClCH2-, and each of R1 and R2 is 1-20 C alkyl, alkenyl, alkoxyalkyl, aralkyl, phenyl or cycloalkyl which may have a side chain, or chlorobutenyl prescribed by Y).

Description

【発明の詳細な説明】 こσ)発明は、水性溶液よりW、銀、金、プラチナ族、
水銀イオン!抽出分離する方法に関する。
[Detailed Description of the Invention] σ) The present invention provides for the production of W, silver, gold, platinum group, etc. from an aqueous solution.
Mercury ion! Concerning extraction and separation methods.

さらに詳しぐは、新却に選択された三級アミンを含有す
る水に難溶性の有機相と接触させることにより、該金属
イオン?有機相へ抽…’fる方法に関才る。
More specifically, by bringing the metal ion into contact with a poorly water-soluble organic phase containing a tertiary amine selected for Shinryu, He is knowledgeable about methods of extraction into organic phases.

従来より、三級アミンにより水性溶液から各種の合鴨イ
オンを有機相へ抽出分離てる方法は知られていた、しか
し、抽出能力、アミンσノ水浴性。
Conventionally, a method of extracting and separating various duck ions from an aqueous solution into an organic phase using a tertiary amine has been known, but the extraction ability and water bathability of the amine σ are limited.

金し・イオンθ・相互分離等のrillでは必ずしも光
♀に満足できる状態ではなかった。
RILLs such as gold metal, ion θ, mutual separation, etc. were not always in a satisfactory state with respect to optical ♀.

不兄明は、新規σノ三教アミンにより、低濃度溶液から
でも尚い抽出能力で%足の金■イオンσ)みを抽出てる
方法を開示するものである。す1」ち、鋼、銀、金、プ
ラチナ族及び水銀イオンσ)みか、他の名種金属イオン
から分離抽出できる。しかも、水性溶液中のこれらイオ
ンの濃度はlppm月ノ下に捷で減少させることかでき
るのである。
Akira Fueni discloses a method for extracting gold ions σ) with a high extraction ability even from low concentration solutions using a new σ-no-Sankyo amine. 1) Steel, silver, gold, platinum group and mercury ions σ) can be separated and extracted from other famous metal ions. Moreover, the concentration of these ions in an aqueous solution can be reduced to less than 1 ppm by extraction.

本発明では、特定の三級アミンを抽剤として使用するこ
とが特徴である。す1】ち、式mK示したクロロブテニ
ルアミン (こ\で、Yは0H300に0HOH2−及び/又は0
H3C旧−0010H2−基を示し、R1及びR2は同
一のあるいは相異なる炭素数1乃至20のアルキル基、
アルケニル基、アルコキシアルキル基、側鎖ケ有シマた
は有しないフェニル基及びシクロアルキル基、並びにY
で規定したクロロブテニル基である)か、特定の金属イ
オンと親和性か特に入きいこと′8−第1j用するもの
である。
The present invention is characterized in that a specific tertiary amine is used as an extraction agent. 1] Chlorobutenylamine shown by the formula mK (here, Y is 0H300, 0HOH2- and/or 0
H3C old-0010H2- group, R1 and R2 are the same or different alkyl groups having 1 to 20 carbon atoms,
Alkenyl groups, alkoxyalkyl groups, phenyl groups with or without side chain chains, and cycloalkyl groups, and Y
It is a chlorobutenyl group defined in (1) or is used because of its affinity with a specific metal ion.

式[1)で、Yで現ポしたクロロゾテニルM5&工分子
中に少くとも1個存在することか必須であり、さらにl
(l、F(2で示された基もYであってもよい。
In the formula [1), it is essential that at least one chlorozotenyl M5 & engineered molecule is present in Y, and furthermore, l
(l, F(2) may also be Y.

ま7,1.Yけ上記σ)いずれσ)クロロブテニル基も
1効であり、七ねそれの信造σアミンθ・混合物、ある
いは1分子中に両省の構造が共存していてもよい。1(
l汲びI(2は広い柁団力炭化水索残基ならびにアルコ
キシ基から選択することかできるか、とくにR1とR2
の少くとも一方には、炭素数4乃至18の範囲にあるこ
とが望ましい。
7.1. The chlorobutenyl group also has a single effect, and a mixture of the seven-layered sigma amine θ, or a mixture of both types of structures may be present in one molecule. 1(
1 (2 can be selected from a wide range of hydrocarbon residues as well as alkoxy groups, especially R1 and R2
It is desirable that at least one of the carbon atoms is in the range of 4 to 18 carbon atoms.

抽出の操作は、適当なPH″″Qhうべきである。PH
が重過き゛ると金属化合物が沈澱したり他種の金属イオ
ンか共雑物として混入することがある。−!た、低過ぎ
ると金属イオンの抽出能力が低下する。とくに他抑の金
属イオンとの分離が必要な場合はPl−1σ)選択は1
費である。したかつて、糸により至適−]は異なり一概
には1えないか、一般的に&’! p)(は2から8の
範囲で選択することかできる。−力、抽出さね、た金属
イオンは、PHを2以下の水浴液と接触させることによ
り告ひ水相へ完全に回収てることかできる。
The extraction operation should be carried out at a suitable pH''Qh. P.H.
If it is too heavy, the metal compound may precipitate or other metal ions may be mixed in as contaminants. -! On the other hand, if it is too low, the ability to extract metal ions will decrease. In particular, when separation from other suppressive metal ions is required, Pl-1σ) is selected.
It is an expense. Once upon a time, the most suitable - ] differs depending on the thread, and it is generally not 1, or generally &'! p) (can be selected in the range from 2 to 8.) - The extracted metal ions must be completely recovered to the aqueous phase by contacting with a water bath solution with a pH below 2. I can do it.

抽出藺度にはとくに制限はない。水#液相及び不憔相か
液体で接触できる範囲で且つ金属イオンが浴任し得る範
囲であればよい。−飯には室温から80℃の範囲で選ば
ハるであろう。
There are no particular restrictions on the degree of extraction. It may be within a range where water can contact the liquid phase and the amorphous phase as a liquid, and within which metal ions can be exposed. - For rice, the temperature range will be from room temperature to 80°C.

抽出剤であるアミンは単独で4 m一様相として使用す
ることができるが、必要r(応じ、炭化水素、島級了ル
コール、エーテルその他の溶媒で希釈することができる
。アミンの濃度としては1係以上が実用的であろう。但
し金属イオンが錯イオンとして存在している場合は、本
プロセスの適用は有効でない場合もある。水浴液中の金
属イオンの濃度は、 ppmオーダーまで適用可能であ
る。上限は金叫イオンが完全に解像として存在していれ
ば適用できる。
The extractant amine can be used alone as a 4 m homogeneous phase, but it can be diluted with hydrocarbons, organic alcohols, ethers, and other solvents as required.The concentration of the amine is 1 However, if metal ions exist as complex ions, the application of this process may not be effective.The concentration of metal ions in the water bath liquid can be applied down to the ppm order. Yes, the upper limit can be applied if the golden cry ion exists as a complete resolution.

本発明の方法は、水溶液中まり金Mを効率よく回収する
ために、あるいは多種の苦槁イオンの混合溶液より特定
の金属を分離回収するために広く第11用することかで
きる。例オば、メッキ液やエツチング族よりO)特冗會
槁の回収、鉱石リーチンダ液よりの神定金鵡の抽出、工
業排水や鉱山セト水中の有害金属の除去などである。
The method of the present invention can be widely used for efficiently recovering Marikin M from an aqueous solution or for separating and recovering a specific metal from a mixed solution of various types of bitter ions. Examples include the recovery of O) special metals from plating solutions and etchings, the extraction of golden parrots from ore leaching fluids, and the removal of harmful metals from industrial wastewater and mining wastewater.

以下、実施例について説明するが、本発明の範囲はこの
態様によって制限されるものではない。
Examples will be described below, but the scope of the present invention is not limited by these embodiments.

実施例1 塩化パラジウムの[]、1’moJ水浴液100ゴとオ
クチル−2クロロデテニルーメチルアミンの10係オク
タツ一ル溶液IQ7y分液ロートに入れ、室温でpH=
 4.5に壌酸で調整し10分IW振腓した後、静置し
分液した。水溶液中のパラジウムイオンを分仇したとこ
ろ、60 ppmに減少していた。
Example 1 A 100% solution of palladium chloride in a 1'moJ water bath and a 10% octyl solution of octyl-2chlorodetenyl-methylamine were placed in an IQ7y separating funnel and the pH was adjusted at room temperature.
After adjusting the temperature to 4.5 with monic acid and shaking with IW for 10 minutes, the mixture was allowed to stand and the liquids were separated. When the palladium ions in the aqueous solution were separated, they were found to have decreased to 60 ppm.

さらに同量の液で再抽出し定ところ水溶液中のパラジウ
ムは1 ppm以下となった。
Furthermore, the palladium in the aqueous solution was re-extracted with the same amount of solution and became 1 ppm or less.

次に上記θ・有機相と堪酸水浴液100 mi″とを1
0分間振組上分液した( pt+=1.OKi’ltl
整)。水浴液中のパラジウムイオンを分析したところは
ソ定童的に水相に回収されていた。尚、オクチル−6ク
ロロブテニルーメチルアミンを使用した場合、抽残水溶
液中σ)パラジウムイオンは70 ppmであつ1こ0
 。
Next, the above θ・organic phase and 100 mi″ of the acid-resistant water bath solution were
Shake and separate for 0 minutes (pt+=1.OKi'ltl
(adjustment). Analysis of palladium ions in the water bath solution revealed that they were collected in the water phase in a consistent manner. In addition, when octyl-6chlorobutenyl-methylamine is used, the content of σ) palladium ions in the raffinate aqueous solution is 70 ppm and 1 0%.
.

笑施例2 名神の金綽化合物の[J、1+no7!俗液を調製し、
トリス−2クロロブテニルアミンσ)20%)ルエン浴
液で実施?l11と1=じ操作で抽出した。抽出率を表
−1に示す。この結果、銅、銀、金、白金方、水銀がと
くによく抽出されることが判明しTこ。
LOL Example 2 [J, 1+no7! Prepare common liquid,
Tris-2chlorobutenylamine σ) 20%) Performed in toluene bath solution? Extraction was performed in the same manner as 111 and 1. The extraction rate is shown in Table-1. As a result, it was found that copper, silver, gold, platinum, and mercury were particularly well extracted.

夾m?lJ3 銀イオン0.1係、水銀イオン0.05優、銀イオン1
.0%、ナトリウムイオン5.0%、カルシウムイオン
1.O%’r言む水浴液100 m/’rpH= 3.
5 テベンジルー2クロロブテニルーメチルアミン20
dで抽出した結果、抽残水ff+液中a・♀祠イオンの
濃度は銀= 80 ppm、水銀= 20 ppm、鉄
= 0.86係ナトリウム=5.1%、カルンウムニ(
1,98%であった。
夾m? lJ3 Silver ion 0.1, mercury ion 0.05, silver ion 1
.. 0%, sodium ion 5.0%, calcium ion 1. O%'r water bath liquid 100 m/'rpH=3.
5 Thebenzyl-2chlorobutenyl-methylamine 20
As a result of extraction with d, the concentration of raffinate water ff + a.
It was 1,98%.

特許出願人 電気化学工業株式会社 (9) 手続補正書(方式) %式% 1 事件の表示 昭和56年特許願第186924月 2 発明の名称 金属イオンの抽出剤及びその方法 ろ 補正をする者 事件との関係  特許出願人 住 所〒100  東京都千代田)メ有楽町1丁目4番
1号昭和57年3月60日 (発送日) 5補正の対象 明細書 6 補正の内容 明細書の浄書(内容に変更なし)
Patent applicant Denki Kagaku Kogyo Co., Ltd. (9) Procedural amendment (method) % formula % 1 Display of case 1982 Patent application No. 186924 April 2 Name of invention Metal ion extractant and its method Case of person making amendment Relationship with Patent Applicant Address: 1-4-1 Yurakucho, Chiyoda, Tokyo 100 March 60, 1982 (Delivery date) 5. Specification subject to amendment 6. Engraving of the description of the contents of the amendment (in the content) No change)

Claims (1)

【特許請求の範囲】 1)卸・、銀、金、プラチナ族及T>/又は水銀イオン
を含有する水性溶液と、PI′12〜6の虐1III5
で、式%式% (こXで、YはcH,、ccにCHCH2−及び/又)
j cH3COH:ec1cH2−基を示し、R1及び
R2は同一のあるいは相異なる炭f数1乃至20のアル
ギル基、アルケニル基、アルコキシアルキル基、アラル
キル基、1tIllf−11をりしまたはセしないフェ
ニル基層ひ7クロアルキル基、並びにYで規定したりO
ロブゝテニル基である)を含有する罐水浴性相とケ接触
させろこ×を詩伝とする藷金極イオンσ佃出方法。 2)距1、銀、釜、プラチナ族及び/又は水域イオン、
丑ひに、鉄族、緬、紺、亜鉛、アルカル金嶋及び/又は
アルカル釜槁イオンヶ浮■する水f1:俗准、1: リ
−PH2〜8σ)特定範囲で1式〔1〕に下すクロロフ
゛デニル了ミンを含有する1水溶性相とV接触させて、
鞄°、嫁、金、7°ラチナ族及び水銀イオンを抽出する
ことを特徴とする抽出分割方法。 3)式〔1〕に示すクロpプテニルアミンヶ含有すせる
ことを特徴とする、鉋1、銀、金、プラチナ族及び水銀
イオンの抽出剤。
[Claims] 1) an aqueous solution containing silver, gold, platinum group and/or mercury ions;
, the formula % formula % (in this X, Y is cH, cc is CHCH2- and/or)
j cH3COH: ec1cH2- group, R1 and R2 are the same or different argyl group, alkenyl group, alkoxyalkyl group, aralkyl group, phenyl base layer with or without 1tIllf-11, and 7 chloroalkyl group, as well as Y or O
A method for deriving gold metal ions by bringing them into contact with a water bathing phase containing a (robutenyl group). 2) Range 1, silver, cauldron, platinum group and/or water ion,
Oxygen, iron group, Burmese, navy blue, zinc, alkal Kanejima and/or alkal pot ion floating water f1: General, 1: Li-PH2~8σ) Chlorophdenyl added to formula 1 [1] in a specific range V contact with a water-soluble phase containing Ryomin,
An extraction and division method characterized by extracting baggage, bride, gold, 7° latina group, and mercury ions. 3) An extractant for silver, gold, platinum group and mercury ions, characterized by containing cloptenylamine represented by formula [1].
JP18692481A 1981-11-24 1981-11-24 Metallic ion extracting reagent and extracting method Pending JPS5891035A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18692481A JPS5891035A (en) 1981-11-24 1981-11-24 Metallic ion extracting reagent and extracting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18692481A JPS5891035A (en) 1981-11-24 1981-11-24 Metallic ion extracting reagent and extracting method

Publications (1)

Publication Number Publication Date
JPS5891035A true JPS5891035A (en) 1983-05-30

Family

ID=16197084

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18692481A Pending JPS5891035A (en) 1981-11-24 1981-11-24 Metallic ion extracting reagent and extracting method

Country Status (1)

Country Link
JP (1) JPS5891035A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5477366A (en) * 1989-03-16 1995-12-19 British Telecommunications Public Limited Company Optical transmission system
JP2007232195A (en) * 2006-03-03 2007-09-13 Nohmi Bosai Ltd Timer valve

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5477366A (en) * 1989-03-16 1995-12-19 British Telecommunications Public Limited Company Optical transmission system
JP2007232195A (en) * 2006-03-03 2007-09-13 Nohmi Bosai Ltd Timer valve

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