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JPH03164428A - Method for purifying cyanoaurate - Google Patents

Method for purifying cyanoaurate

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Publication number
JPH03164428A
JPH03164428A JP30233189A JP30233189A JPH03164428A JP H03164428 A JPH03164428 A JP H03164428A JP 30233189 A JP30233189 A JP 30233189A JP 30233189 A JP30233189 A JP 30233189A JP H03164428 A JPH03164428 A JP H03164428A
Authority
JP
Japan
Prior art keywords
cyanauric
cyanoaurate
acetone
potassium
acid
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.)
Granted
Application number
JP30233189A
Other languages
Japanese (ja)
Other versions
JP2879582B2 (en
Inventor
Kazuhisa Shiomi
塩見 和久
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.)
DOWA CHEM KK
Original Assignee
DOWA CHEM 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 DOWA CHEM KK filed Critical DOWA CHEM KK
Priority to JP30233189A priority Critical patent/JP2879582B2/en
Publication of JPH03164428A publication Critical patent/JPH03164428A/en
Application granted granted Critical
Publication of JP2879582B2 publication Critical patent/JP2879582B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To produce high purity cyanoaurate in a high yield by dissolving cyanoaurate contg. impurity in acetone, separating the impurity as solid matter and removing the acetone from the resulting soln. by evaporation. CONSTITUTION:Potassium cyanoaurate contg. KCl as impurity (or sodium cyanoaurate contg. NaCl as impurity) is dissolved in acetone, solid-liq. separation is carried out and the impurity is removed as solid matter. The acetone is then removed from the resulting soln. by evaporation. High purity potassium cyanoaurate (or sodium cyanoaurate) nearly free from impurities is obtd. in a high yield.

Description

【発明の詳細な説明】 [産業上の利用分野J 本発明は、金メッキ工程で採用される金メッキ浴の金源
として使用されているシアン化第2金酸カリウムやシア
ン化第2金酸ナトリウム等のシアン化第2金酸塩、すな
わちテトラシアノ金(m)酸塩M’  [Au (CN
)4コ (M’は1価陽イオン)の粗製品の精製方法に
関する。
Detailed Description of the Invention [Industrial Application Field J] The present invention is directed to potassium cyanauric acid, sodium cyanauric acid, etc., which are used as a gold source in a gold plating bath employed in a gold plating process. cyanauric acid salt, i.e., tetracyanoauric acid salt M' [Au (CN
) 4 (M' is a monovalent cation) Relating to a method for purifying a crude product.

〔従来の技術] シアン化第2金酸カリウムは塩化第2金酸カリウムをシ
アン化カリウムで置換して得られている。
[Prior Art] Potassium cyanauric acid is obtained by replacing potassium cyanauric acid with potassium cyanide.

また、シアン化第2金酸ナトリウムは、塩化第2金酸ナ
トリウムをシアン化ナトリウムで置換して得られている
。これらの反応は次の式で表わすことができる。
Moreover, sodium cyanauric acid is obtained by replacing sodium cyanauric acid with sodium cyanide. These reactions can be expressed by the following equations.

M  CA u Cl  4  コ 千4MCN   
→MA u ( C N ) 4 + 4 M Cρ(
式中のMはKまたはNaを表わす。)・・・・ω0式か
らわかるように、この反応の副生成物として、塩化カリ
ウムまたは塩化ナトリウムが生或する。これらの副生成
物を除去するために、水溶液中でシアン化第2金酸カリ
ウムKAu(CN)4またはシアン化第2金酸ナトリウ
ムNaAu (CN)4を晶折させて固液分離する方法
や正タノールでシアン化第2金酸カリウムまたはシアン
化第2金酸ナ1・リウムを溶媒抽出する方法などが行わ
れている。
M CA u Cl 4 ko 1,4MCN
→MA u (CN) 4 + 4 MCρ(
M in the formula represents K or Na. )...As can be seen from the ω0 equation, potassium chloride or sodium chloride is produced as a byproduct of this reaction. In order to remove these by-products, a method of solid-liquid separation by crystallizing potassium cyanauric acid KAu(CN)4 or sodium cyanauric acid NaAu(CN)4 in an aqueous solution, A method of solvent extraction of potassium cyanauric acid or sodium diauric cyanide using normal ethanol has been used.

E発四が解決しようとする課題] 前記(1)式に従って行う従来技術の、水溶液中でシア
ン化第2金酸カリウムまたはシアン化第2金酸ナ1・リ
ウムを晶析させる方法においては、これらの第2金酸塩
が水に易溶であるため、晶析しないで水溶液中に残存す
る金が柑当量ある。そこで、晶析後固液分ML.で得た
液を前記0〕式に従う置換反応系に戻して再使用するこ
とが行われるが、これを何回も繰り返すと溶戚中に塩化
カリウムまたは塩化ナl・リウムが蓄積される結果、晶
析した製品中に混入する塩化カリウムまたは塩化ナトリ
ウムの量が増加1,てくるため、製品が本来のIll的
にそぐわない純度の低いものLなってしまう。このため
、上記従来の方法においては、晶折工程終了後の溶液を
常に前記置換反応工程に戻1,て再使用するわけにはい
かず、少なくともこの溶液の一部を別途処理して液中の
金を回収する工程を設けることがどうしても必要となる
。このような副次的回収工程の増加と、該回収工程にお
りる金の収率の低さと、これによる金の直接歩留りの低
下等が製品コス1・を高める重要な原因の一つとなって
いる。
Problems to be Solved by E-Hatsushi] In the prior art method of crystallizing potassium cyanauric acid or sodium chloride cyanide in an aqueous solution, which is carried out according to the above formula (1), Since these auric acid salts are easily soluble in water, there is an equivalent amount of gold remaining in the aqueous solution without crystallizing. Therefore, the solid-liquid fraction ML after crystallization. The solution obtained in step 0 is returned to the substitution reaction system according to formula 0 and reused, but if this is repeated many times, potassium chloride or sodium/lium chloride will accumulate in the molten phase. Since the amount of potassium chloride or sodium chloride mixed into the crystallized product increases, the product becomes a product of low purity that does not meet the original characteristics. For this reason, in the conventional method described above, the solution after the crystallization step cannot always be returned to the substitution reaction step 1 and reused, and at least a part of this solution must be separately processed to remove the It is absolutely necessary to set up a process to recover the gold. The increase in the number of secondary recovery processes, the low yield of gold in the recovery process, and the resulting decrease in the direct yield of gold are among the important causes of increasing product cost. There is.

一方、従来技術のエタノールで溶媒抽出する方法は、エ
タノールへの塩化カリウムの溶解度が0,08gKCf
t/(,2 Hs OHIOO−という比較的高い値で
あるため(Atherton Seldell.”So
lubilities−. 1953. D・Van 
NosthrandCompany p.77B. p
.780) 、塩化カリウムの除去を完全に行うことは
困難である。
On the other hand, in the conventional method of solvent extraction with ethanol, the solubility of potassium chloride in ethanol is 0.08 gKCf.
t/(,2 Hs OHIOO-, which is a relatively high value (Atherton Seldell."So
lubilities-. 1953. D.Van
Nothrand Company p. 77B. p
.. 780), it is difficult to completely remove potassium chloride.

[課題を解決するための手段] 上記課題を角q決するため鋭意研究1,た或果として、
本発明者は、アセ1・ンをシアン化第2金酸カリウムま
たはシアン化第2金酸ナトリウムの溶媒εして使用する
こεにより、それらシアン化第2金酸塩の精製を有利に
実施できることを見出(7、本発明に到達した。
[Means for solving the problem] In order to solve the above problem, we conducted intensive research 1, and as a result,
The present inventor has advantageously carried out the purification of potassium cyanauric acid salts or sodium cyanauric acid salts by using acetin as a solvent ε for potassium cyanauric acid salts or sodium cyanauric acid salts. We have discovered what we can do (7) and have arrived at the present invention.

[作 用] 本発明者の研究により、次のことが見い出された。[Work] Through research conducted by the present inventor, the following was discovered.

シアン化第2金酸カリウム[KA u (CN) a 
]およびシアン化第2金酸ナ1・リウム[N a A 
u(CN)4]は、いずれもアセトンへの溶解が容易で
あり、その溶解度も大きい。一方塩化カリウム(KCL
)および塩化ナトリウム(NaCff)のアセトンへの
溶解度はいずれも極めて小さく、ほとんとOに近い。し
たがって、アセトンの持つこの特性を利用すれば、KC
Iを不純物たしてaむ粗製KAu (CN)4 、また
はNaCf!を不純物としてaむ粗製NaAu (CN
)4をアセトンに溶jl9Lて固液分が{7、得られた
液分がらアセトンを減圧等の手段で蒸発除去することに
より、容易に純度の高いKAu(CN)4またはNaA
u(CN).を得ることができる。
Potassium cyanide [KA u (CN) a
] and sodium 1.lium cyanide [N a A
u(CN)4] are both easily dissolved in acetone and have high solubility. On the other hand, potassium chloride (KCL)
) and sodium chloride (NaCff) have extremely low solubility in acetone, almost close to O. Therefore, by utilizing this property of acetone, KC
Crude KAu (CN)4 with impurity I, or NaCf! Crude NaAu (CN
) 4 in acetone to give a solid-liquid content of
u(CN). can be obtained.

上記のアセトンを14m相として用いる溶媒抽出法を利
用すれば、前記(D式の置換反応系に戻すここのできな
いシアン化第2金酸塩を含む置換終了後の液から、シア
ン化第2金酸塩を容易に回収することかできる。
By using the above-mentioned solvent extraction method using acetone as the 14m phase, it is possible to extract ferric cyanide from the liquid containing ferric cyanide, which cannot be returned to the substitution reaction system of formula D. The acid salt can be easily recovered.

[実施例1] 試薬のシアン化第2金酸カリウム、KAIJ(CN)4
 ・ Q.5H2 0 (金員で300.0g)と試薬
の塩化カリウム、KCN  (300g)とを混合した
試f4を用いて、下記の手順により該混合試料の精製試
験を行った。
[Example 1] Reagent potassium cyanauric acid, KAIJ(CN)4
・Q. Using test f4, which is a mixture of 5H2 0 (300.0 g in gold) and reagents potassium chloride and KCN (300 g), a purification test was conducted on the mixed sample according to the following procedure.

混合試料を試薬特級のアセl・ン2gに溶解させ、不溶
分であるKCjを濾過により除去した。さらにこの不溶
分をアセトンで充分に洗浄し、洗浄液は先の濾液に合体
させた。この濾液をエバボレータに移1,減圧してアセ
トンを蒸発除去した。残留した固形分を80℃で数分間
かけて重量が一定になるまで乾燥したものを精製シアン
化第2金酸カリウムとし、分析して下記第1表に示す結
果を得た。
The mixed sample was dissolved in 2 g of reagent grade Acerol, and insoluble KCj was removed by filtration. Furthermore, this insoluble matter was thoroughly washed with acetone, and the washing liquid was combined with the previous filtrate. This filtrate was transferred to an evaporator (1) and the pressure was reduced to remove acetone by evaporation. The remaining solid content was dried at 80° C. for several minutes until the weight became constant, and purified potassium cyanaurate was obtained.The resulting product was analyzed to obtain the results shown in Table 1 below.

(以下余白.) 第 1 表 [発明の効果] 実施例1の結果から明らかであるように、粗製シアン化
第2金酸塩の精製においては金の直接歩留りがほぼ10
0%に近く、不純物の塩素分はほぼ0である。アセトン
がシアン化第2金酸カリウムまたはシアン化第2金酸ナ
トリウムの精製用溶媒として極めて優れていることは明
白である。
(Margin below.) Table 1 [Effects of the invention] As is clear from the results of Example 1, in the purification of crude cyanauric acid salt, the direct yield of gold was approximately 10%.
It is close to 0%, and the chlorine content of impurities is almost 0. It is clear that acetone is an excellent solvent for purifying potassium cyanauric acid or sodium cyanauric acid.

Claims (3)

【特許請求の範囲】[Claims] (1)不純物を含むシアン化第2金酸塩をアセトンで溶
解した後、固液分離して不純物を固形物として除き、得
られた液分からアセトンを蒸発除去することを特徴とす
るシアン化第2金酸塩の精製方法。
(1) A cyanide solution containing impurities is dissolved in acetone, followed by solid-liquid separation to remove impurities as a solid substance, and acetone is removed by evaporation from the resulting liquid. Method for purifying diaurate.
(2)前記シアン化第2金酸塩がシアン化第2金酸カリ
ウム、KAu(CN)_4であり、主たる不純物がKC
lである請求項1記載の方法。
(2) The cyanauric acid salt is potassium cyanauric acid acid, KAu(CN)_4, and the main impurity is KC.
2. The method according to claim 1, wherein: l.
(3)前記シアン化第2金酸塩がシアン化第2金酸ナト
リウム、NaAu(CN)_4であり、主たる不純物が
NaClである請求項1記載の方法。
(3) The method according to claim 1, wherein the cyanauric acid salt is sodium cyanauric acid salt, NaAu(CN)_4, and the main impurity is NaCl.
JP30233189A 1989-11-21 1989-11-21 Purification method of cyanuric diaurate Expired - Fee Related JP2879582B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30233189A JP2879582B2 (en) 1989-11-21 1989-11-21 Purification method of cyanuric diaurate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30233189A JP2879582B2 (en) 1989-11-21 1989-11-21 Purification method of cyanuric diaurate

Publications (2)

Publication Number Publication Date
JPH03164428A true JPH03164428A (en) 1991-07-16
JP2879582B2 JP2879582B2 (en) 1999-04-05

Family

ID=17907652

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30233189A Expired - Fee Related JP2879582B2 (en) 1989-11-21 1989-11-21 Purification method of cyanuric diaurate

Country Status (1)

Country Link
JP (1) JP2879582B2 (en)

Also Published As

Publication number Publication date
JP2879582B2 (en) 1999-04-05

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