JPH06136549A - Treatment of hypophosphoric acid ion in aged plating liquid - Google Patents

Treatment of hypophosphoric acid ion in aged plating liquid

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Publication number
JPH06136549A
JPH06136549A JP31290592A JP31290592A JPH06136549A JP H06136549 A JPH06136549 A JP H06136549A JP 31290592 A JP31290592 A JP 31290592A JP 31290592 A JP31290592 A JP 31290592A JP H06136549 A JPH06136549 A JP H06136549A
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JP
Japan
Prior art keywords
liquid
acid ions
ions
titanium dioxide
photocatalyst
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
JP31290592A
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Japanese (ja)
Other versions
JP2603895B2 (en
Inventor
Kunihiko Azuma
邦彦 東
Kenji Otsuka
健治 大塚
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Tokyo Metropolitan Government
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Tokyo Metropolitan Government
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Publication of JPH06136549A publication Critical patent/JPH06136549A/en
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  • Removal Of Specific Substances (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To eliminate the harmfulness of hypophosphoric acid ions as phosphoric acid ions or calcium phosphate by subjecting an aged electroless plating liquid contg. a large amt. of the hypophosphoric acid ions to an oxidation treatment. CONSTITUTION:The aged liquid of the electroless plating liquid, such as electroless Ni plating liquid, contains the hypophosphoric acid ions of a high concn. and is inadequate as waste water in terms of eutrophication and chemical oxygen consumption and, therefore, the powder of TiO2 deposited with a noble metal, such as Pt, is added as a photocatalyst to this aged liquid in the state of maintaining the liquid at a pH 1 to 4 range at a ratio of, for example, 8g/l. While air or oxygen is blown into the liquid, the liquid is irradiated with UV rays by a high-voltage mercury lamp, by which the hypophosphoric acid ions are oxidized to the phosphoric acid ions or a Ca salt is added thereto to form the calcium phosphate. Such liquid is maintained at pH 1 to 3 and is filtered, by which the TiO2 catalyst deposited with the noble metal is recovered. The remaining liquid is reused after the phosphoric acid ions are removed. The remaining liquid is otherwise easily drained as the calcium phosphate-contg. liquid.

Description

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

【0001】[0001]

【産業上の利用分野】 この発明は、めっき老化液中、
詳細には無電解めっき老化液中に還元剤として含まれる
難分解性次亜りん酸イオンを酸化し、りん酸イオンを回
収するか、カルシウム塩を添加してりん酸カルシウムと
して処分するめっき老化液中の次亜りん酸イオンの処理
方法にかかる。
This invention relates to a plating aging solution,
Specifically, a plating aging solution that oxidizes the persistent hypophosphite ion contained as a reducing agent in the electroless plating aging solution and recovers the phosphate ion or disposes it as calcium phosphate by adding a calcium salt. The method of treating hypophosphite ions in the inside.

【0002】[0002]

【従来の技術】 無電解めっきは均一にしかも不導体物
にもめっきができることから、機能めっきとして幅広く
用いられている。無電解めっき液には還元剤として次亜
りん酸イオンを用いているため寿命が短く、多量の老化
液が発生する。この、老化液には高濃度の次亜りん酸イ
オンを含むため、富栄養化、化学的酸素消費量の点から
処理が必要である。
2. Description of the Related Art Electroless plating is widely used as functional plating because it can uniformly and non-conductive material. Since the electroless plating solution uses hypophosphite ions as a reducing agent, its life is short and a large amount of aging solution is generated. Since this aging liquid contains a high concentration of hypophosphite ion, it needs to be treated in terms of eutrophication and chemical oxygen consumption.

【0003】めっき廃液中のりん酸化合物の排水処理は
一般に薬品添加による処理が行われている。すなわち、
亜りん酸イオン、りん酸イオンにカルシウム塩を添加し
て難溶性の亜りん酸カルシウム、りん酸カルシウムを生
成させ凝集沈澱処理する方法がとられている。しかしな
がら、次亜りん酸イオンはカルシウム塩による沈澱物の
生成がしにくく処理は困難である。そこで、次亜りん酸
イオンを含むりん化合物は一旦りん酸イオンに酸化して
から処理する方法がとられている。
Wastewater treatment of the phosphoric acid compound in the plating waste liquid is generally performed by adding chemicals. That is,
A method of adding a calcium salt to phosphite ions or phosphate ions to form sparingly soluble calcium phosphite or calcium phosphate and subjecting it to coagulation precipitation treatment is used. However, hypophosphite ion is difficult to treat because it is difficult to form a precipitate due to calcium salt. Therefore, a method of treating a phosphorus compound containing hypophosphite ion after once oxidizing it to phosphate ion is adopted.

【0004】この酸化方法には、次亜りん酸イオンを含
む溶液をスチームで90°C以上に上げ、これにニッケ
ルイオンやコバルトイオンなどの金属塩を添加して次亜
りん酸イオンを亜りん酸イオンに酸化し、これにカルシ
ウム塩を添加して亜りん酸カルシウムとして処理する、
いわば次亜りん酸イオンの自己分解による酸化処理法が
ある。
In this oxidation method, a solution containing hypophosphite ions is heated to 90 ° C. or higher by steam, and metal salts such as nickel ions and cobalt ions are added to the solution to make hypophosphite ions phosphorous. Oxidize to acid ions, add calcium salt to this and treat as calcium phosphite,
There is, so to speak, an oxidation treatment method by the autolysis of hypophosphite ions.

【0005】他の酸化方法としては、次亜りん酸イオン
を含む溶液を電解し、陽極で生成した酸素で次亜りん酸
イオンをりん酸イオンに酸化する、電解酸化法がある。
As another oxidation method, there is an electrolytic oxidation method in which a solution containing hypophosphite ions is electrolyzed and the hypophosphite ions are oxidized to phosphate ions by oxygen generated at the anode.

【0006】さらに他の酸化方法としては、次亜りん酸
イオンを含む溶液に過酸化水素を添加して紫外線を照射
し、過酸化水素の分解によって生成した活性酸種で次亜
りん酸イオンをりん酸イオンに酸化する紫外線と過酸化
水素の併用法がある。
As another oxidation method, hydrogen peroxide is added to a solution containing hypophosphite ions and irradiated with ultraviolet rays, and hypophosphite ions are converted into active acid species produced by decomposition of hydrogen peroxide. There is a combined use of hydrogen peroxide and ultraviolet rays that oxidize to phosphate ions.

【0007】[0007]

【発明が解決しようとする課題】 しかしながら、自己
分解法では酸化処理効果が悪く、確実な酸化の管理が行
いにくいという課題を有する。電解酸化法では処理時間
が長くかかるため電力費が高く経済性を欠く課題を有す
る。紫外線と過酸化水素の併用法では、酸化剤としての
過酸化水素の使用量が多いなどの課題を有する。
However, the self-decomposition method has a problem that the oxidation treatment effect is poor and it is difficult to reliably control oxidation. Since the electrolytic oxidation method requires a long processing time, it has a problem of high power cost and lack of economy. The combined use of ultraviolet rays and hydrogen peroxide has problems such as a large amount of hydrogen peroxide used as an oxidizing agent.

【0008】いずれにしても、従来の酸化方法では課題
が多いため、次亜りん酸イオン処理は行われずに海洋投
棄による処理がなされていた。
In any case, since there are many problems in the conventional oxidation method, the hypophosphite ion treatment is not carried out, but the treatment by ocean dumping is performed.

【0009】亜りん酸塩とその塩を含有するめっき廃液
の処理方法としては、特開昭63ー274491が知ら
れている。同方法では、光触媒の正孔での酸化能を利用
して亜りん酸を酸化している。
As a method for treating a plating waste liquid containing phosphite and its salt, Japanese Patent Laid-Open No. 63-274491 is known. In this method, phosphorous acid is oxidized by utilizing the photocatalyst's ability to oxidize holes.

【0010】しかしながら、この酸化方法では酸化力は
弱く、この従来例では酸化反応によって処理しているた
め、処理時間が長くなる課題を有する。また、pH範囲
については何等記載がないが、めっき老化液には重金属
類が多く含まれている。これら重金属が光触媒上に析出
すると反応を阻害する点で課題を有する。さらに、使用
した光触媒を回収していないが、再利用しないと経済的
とは言い難く回収再利用の課題を有する。
However, this oxidizing method has a weak oxidizing power, and in this conventional example, since the processing is carried out by an oxidizing reaction, there is a problem that the processing time becomes long. Although no mention is made of the pH range, the plating aging liquid contains a large amount of heavy metals. When these heavy metals are deposited on the photocatalyst, there is a problem in that they hinder the reaction. Further, although the used photocatalyst is not recovered, it is difficult to say that it is economical unless it is reused, and there is a problem of recovery and reuse.

【0011】他方、発明者は、無電解めっき老化液中の
次亜りん酸イオンを効果的に酸化させるには、活性酸素
種をいかに生成し使用するかであり、そこで、酸化薬品
など用いずに効果的に酸化処理を行うことを検討した。
その結果、酸性にした老化液に光触媒と酸素を共存さ
せ、光照射によって短時間に効率良く酸化できることを
知見した。
On the other hand, the inventor wonders how to generate and use active oxygen species in order to effectively oxidize the hypophosphite ion in the electroless plating aging solution. It was examined to effectively oxidize.
As a result, it was found that the photocatalyst and oxygen coexist in the acidified aging liquid, and the light irradiation can efficiently oxidize in a short time.

【0012】[0012]

【課題を解決するための手段】 この発明は、これら知
見に基づくものであって、
Means for Solving the Problems The present invention is based on these findings,

【0013】次亜りん酸イオンを含むめっき老化液をp
H1〜4に保ち、貴金属を担持した二酸化チタン粉末を
光触媒として共存させ、酸素または空気を老化液中に吹
き込みながら光を照射し次亜りん酸イオンを酸化してり
ん酸イオンにし、次いでpHを1〜3に保って濾過して
貴金属を担持した二酸化チタン粉末を回収することを特
徴とするめっき老化液中の次亜りん酸イオンの処理方
法、
A plating aging solution containing hypophosphite ions is added
Keeping H1 to 4 and coexisting with titanium dioxide powder carrying a noble metal as a photocatalyst, irradiating light while blowing oxygen or air into the aging solution to oxidize hypophosphite ions to phosphate ions, and then to adjust pH. A method for treating hypophosphite ions in a plating aging liquid, characterized in that a titanium dioxide powder carrying a noble metal is recovered by keeping it at 1 to 3 and filtering,

【0014】を提供する。[0014]

【0015】[0015]

【実施例】 次亜りん酸イオンを含む無電解めっき老化
液をpH1〜4に保ち、室温で貴金属を担持した二酸化
チタン粉末を光触媒として共存させる。同時に酸素また
は空気を老化液中に吹き込みながら、365nmを主波
長とする高圧水銀灯により紫外線を照射し次亜りん酸イ
オンをりん酸イオンに酸化する。次いで光触媒を含む処
理水のpHを1〜3に保って濾過して、貴金属を担持し
た二酸化チタン粉末を回収し、再利用する。
Example The pH of the electroless plating aging solution containing hypophosphite ions is kept at 1 to 4, and titanium dioxide powder carrying a noble metal is allowed to coexist as a photocatalyst at room temperature. At the same time, while blowing oxygen or air into the aging liquid, ultraviolet rays are irradiated by a high pressure mercury lamp having a main wavelength of 365 nm to oxidize hypophosphite ions into phosphate ions. Next, the pH of the treated water containing the photocatalyst is maintained at 1 to 3 and filtered to recover the titanium dioxide powder carrying the noble metal and reuse it.

【0016】水溶液中の二酸化チタン(TiO2)など
の光触媒にバンドキャップ以上のエネルギーを持つ光を
照射すると、二酸化チタンの価電子帯の電子が励起され
伝導帯に移動し、価電子帯の正孔と伝導帯の電子にわか
れる。そして価電子帯の正孔と水が酸化反応によってヒ
ドロキシルラジカルを生成する。一方伝導帯の電子と水
素イオンが還元反応によって水素を生成する。
When a photocatalyst such as titanium dioxide (TiO 2 ) in an aqueous solution is irradiated with light having energy higher than the band cap, the electrons in the valence band of titanium dioxide are excited and move to the conduction band, and the positive valence band is detected. It is divided into holes and electrons in the conduction band. Then, holes in the valence band and water generate hydroxyl radicals by an oxidation reaction. On the other hand, electrons in the conduction band and hydrogen ions generate hydrogen by a reduction reaction.

【0017】一般に、正孔の酸化反応で生じたヒドロキ
シルラジカルの活性酸素種を酸化剤として用いるが酸化
力が小さい。それに対し、この実施例では二酸化チタン
に白金や銀などの貴金属を部分的に担持させて電荷分離
を良くし、これに酸素又は空気を吹き込み、伝導帯で酸
素の還元反応によって生じた超酸化水素ラジカルの活性
酸素種を主に酸化剤に用いて次亜りん酸イオンをりん酸
イオンに酸化させる。
Generally, active oxygen species of hydroxyl radicals generated by the oxidation reaction of holes are used as an oxidizing agent, but the oxidizing power is small. On the other hand, in this embodiment, titanium dioxide is partially supported by a noble metal such as platinum or silver to improve charge separation, and oxygen or air is blown into the titanium dioxide to generate hydrogen peroxide in the conduction band due to oxygen reduction reaction. The active oxygen species of radicals are mainly used as an oxidizing agent to oxidize hypophosphite ions to phosphate ions.

【0018】酸化反応は、pH1〜4の範囲でおこな
う。これは、無電解めっき老化液にはニッケルイオンな
ど重金属類を多く含むため、pHが高くなると光触媒の
表面に重金属類が析出して酸化反応を阻害するのを避け
るためである。
The oxidation reaction is carried out in the pH range of 1-4. This is because the electroless plating aging solution contains a large amount of heavy metals such as nickel ions, so that when the pH increases, the heavy metals are prevented from precipitating on the surface of the photocatalyst and inhibiting the oxidation reaction.

【0019】光の照射としては、紫外線照射が望まし
く、更には365nmを主波長とする高圧水銀灯照射が
望ましい。すなわち、250〜260nmを主波長とす
る低圧水銀灯(13W)と、365nmを主波長とする
高圧水銀灯(400W)を使用して、光触媒として二酸
化チタン1g/l添加し、1000mg/lの次亜りん
酸イオンをりん酸イオンに酸化する酸化率と酸化時間の
関係を検討したところ、高圧水銀灯を使用した場合は、
110分程度で100%酸化されたが、低圧水銀灯では
110分で5%の酸化反応しか進まなかった。低圧水銀
灯では、懸濁物質が多くなると短波長のため光が遮断さ
れて酸化効果が落ちたものと考えられる。
The irradiation of light is preferably ultraviolet irradiation, and more preferably irradiation of a high pressure mercury lamp having a main wavelength of 365 nm. That is, using a low-pressure mercury lamp (13 W) having a main wavelength of 250 to 260 nm and a high-pressure mercury lamp (400 W) having a main wavelength of 365 nm, 1 g / l of titanium dioxide was added as a photocatalyst to obtain 1000 mg / l of hypophosphorous acid. When the relationship between the oxidation rate of oxidizing the acid ions to phosphate ions and the oxidation time was examined, it was found that when a high pressure mercury lamp was used,
Although it was oxidized 100% in about 110 minutes, only 5% of the oxidation reaction proceeded in 110 minutes with the low pressure mercury lamp. In a low-pressure mercury lamp, it is considered that when the amount of suspended matter increases, the light is blocked due to the short wavelength and the oxidation effect is reduced.

【0020】酸化には、空気又は酸素を吹き込む。すな
わち、次亜りん酸イオン濃度1000mg/lの無電解
めっき老化液を300mlとり、空気を3l/minで
吹き込みながら、光触媒として二酸化チタンを8g/l
添加して高圧水銀灯を照射した。その結果、100%り
ん酸イオンに酸化するのに70分で完全に酸化した。空
気の代わりに窒素を吹き込んだところ酸化反応は全く示
さなかった。
Air or oxygen is blown into the oxidation. That is, 300 ml of an electroless plating aging solution having a hypophosphite ion concentration of 1000 mg / l was taken and 8 g / l of titanium dioxide was used as a photocatalyst while blowing air at 3 l / min.
It was added and irradiated with a high pressure mercury lamp. As a result, it took 70 minutes to completely oxidize to 100% phosphate ion. When nitrogen was blown in instead of air, no oxidation reaction was shown.

【0021】さらに、空気吹込み量の変化と酸化終了時
間を求めた。その結果、空気吹き込み量が多い方が酸化
時間が短いことが解った。尚、3l/min以上では酸
化反応時間がそれほど短縮できない。これは、実験装置
の構造上二酸化チタンが効果的に拡散できず、酸化反応
が進行しなかったためと考えられる。
Further, the change in the amount of air blown and the oxidation end time were determined. As a result, it was found that the oxidation time was shorter when the amount of air blown was larger. If it is 3 l / min or more, the oxidation reaction time cannot be shortened so much. This is probably because titanium dioxide could not be effectively diffused due to the structure of the experimental apparatus, and the oxidation reaction did not proceed.

【0022】光触媒としては、二酸化チタンを使用す
る。すなわち、次亜りん酸イオン濃度1000mg/l
の無電解めっき老化液を300mlとり、空気を3l/
minで吹き込みながら高圧水銀灯のみの照射の場合
と、光触媒として二酸化チタンを8g/l添加して同様
に照射した場合の酸化反応時間と反応によって生成する
各種りん酸イオンの存在比率を調べた。その結果、高圧
水銀灯照射のみの場合は、100%りん酸イオンに酸化
するのに3時間20分を要した。他方、光触媒として二
酸化チタンを共存させて照射した場合は70分で完全に
酸化した。
Titanium dioxide is used as the photocatalyst. That is, the hypophosphite ion concentration is 1000 mg / l
300ml of electroless plating aging liquid of
The oxidation reaction time and the abundance ratios of various phosphate ions produced by the reaction were investigated in the case of irradiation with only a high-pressure mercury lamp while blowing at min, and in the case of irradiation with titanium dioxide of 8 g / l as a photocatalyst. As a result, it took 3 hours and 20 minutes to oxidize to 100% phosphate ions when only high-pressure mercury lamp irradiation was performed. On the other hand, when titanium dioxide was coexisted as a photocatalyst for irradiation, it was completely oxidized in 70 minutes.

【0023】また、次亜りん酸イオンからりん酸イオン
に酸化される過程で亜りん酸イオンを生成してりん酸イ
オンに酸化されることがわかった。酸素および二酸化チ
タンの共存下で高圧水銀灯を照射すれば効果的に酸化反
応が進むことから次亜りん酸イオンがりん酸イオンに酸
化する。
It was also found that in the course of oxidation of hypophosphite ion to phosphate ion, phosphite ion is produced and oxidized to phosphate ion. When a high-pressure mercury lamp is irradiated in the presence of oxygen and titanium dioxide, the oxidation reaction proceeds effectively, so that hypophosphite ion is oxidized to phosphate ion.

【0024】光触媒の添加量については以下、判明し
た。すなわち、1000mg/lの次亜りん酸イオン濃
度(pH5.2)を含む溶液に光触媒として二酸化チタ
ンのみ用いた場合と白金担持の二酸化チタンを用いた場
合、それぞれの添加量と酸化終了時間との関係を調べ
た。二酸化チタンのみの場合、白金担持の二酸化チタン
の場合共に添加量が多い方が短時間に酸化反応が進み、
最適添加量が両者とも8g/lであった。二酸化チタン
のみの場合の酸化終了時間が70分、白金担持の二酸化
チタンで45分と白金担持の二酸化チタンを用いる方が
短時間に酸化処理することができた。なお、両者とも8
g/l以上添加しても酸化終了時間はほぼ一定であっ
た。これは、二酸化チタンの比重が3.9と重く、攪拌
はしているが一部が分散せずに反応器の底に沈澱するた
めと考えられる。
The amount of the photocatalyst added was found out below. That is, when only titanium dioxide was used as a photocatalyst in a solution containing a hypophosphite ion concentration (pH 5.2) of 1000 mg / l, and when platinum-supported titanium dioxide was used, the addition amount and the oxidation completion time of each were determined. I investigated the relationship. In the case of titanium dioxide alone, or in the case of platinum-supported titanium dioxide, the larger the added amount, the shorter the oxidation reaction proceeds,
The optimum addition amount was 8 g / l for both. When titanium dioxide alone was used, the oxidation completion time was 70 minutes, and when platinum-supported titanium dioxide was used for 45 minutes, it was possible to perform the oxidation treatment in a shorter time using platinum-supported titanium dioxide. Both are 8
The oxidation completion time was almost constant even if g / l or more was added. It is considered that this is because titanium dioxide has a high specific gravity of 3.9, and while stirring, a part of the titanium dioxide does not disperse and precipitates at the bottom of the reactor.

【0025】酸化終了後処理水と光触媒をpH3以下で
濾過を用いて分離して光触媒を再利用する。pH3以下
にすると光触媒の凝集性が良くなり、分離がおこない易
くなる。なお、光触媒をくり返し使用してもその効果は
同じである。
After the completion of the oxidation, the treated water and the photocatalyst are separated at a pH of 3 or less by filtration to reuse the photocatalyst. When the pH is 3 or less, the photocatalyst has good cohesiveness, and separation is easy to occur. The effect is the same even if the photocatalyst is repeatedly used.

【0026】実施例1Example 1

【0027】次亜りん酸イオン1000mg/lを含む
次亜りん酸ナトリウム溶液に金属塩として硫酸ニッケル
82.2mmol/1加えた溶液をpH3に保ち酸化処
理した。溶液300mlを容量300ml用の内部照射
型光化学反応装置に入れ、これに白金担持した二酸化チ
タン粉末を8g/l共存させ、空気を31/minの割
合で吹き込みながら高圧水銀灯で照射した結果、55分
で100%りん酸イオンに酸化できた。
A solution prepared by adding 82.2 mmol / 1 of nickel sulfate as a metal salt to a sodium hypophosphite solution containing 1000 mg / l of hypophosphite ion was kept at pH 3 for oxidation treatment. 300 ml of the solution was placed in an internal irradiation type photochemical reaction device for a volume of 300 ml, and 8 g / l of platinum-supported titanium dioxide powder was allowed to coexist in this, and irradiation with a high pressure mercury lamp was performed while blowing air at a rate of 31 / min. Was able to oxidize to 100% phosphate ion.

【0028】実施例2Example 2

【0029】市販の無電解ニッケルめっき液を用い、次
亜りん酸イオン1000mg/lになるように希釈した
液をpH2.5に保ち酸化処理した。溶液300mlを
容量300ml用の内部照射型光化学反応装置に入れ、
これに白金担持した二酸化チタン粉末を8g/l共存さ
せ、空気を31/minの割合で吹き込みながら高圧水
銀灯で照射した結果、120分で100%りん酸イオン
に酸化できた。
Using a commercially available electroless nickel plating solution, a solution diluted to a hypophosphite ion concentration of 1000 mg / l was maintained at pH 2.5 for oxidation treatment. Put 300 ml of the solution into the internal irradiation type photochemical reactor for the volume of 300 ml,
Platinum-supported titanium dioxide powder was allowed to coexist therewith in an amount of 8 g / l, and irradiation with a high-pressure mercury lamp was performed while blowing air at a rate of 31 / min. As a result, it was possible to oxidize to 100% phosphate ions in 120 minutes.

【0030】実施例3Example 3

【0031】次亜りん酸イオン10.4g/l、亜りん
酸イオン52.8g/l、りん酸イオン0.6g/l、
および有機酸が有機体炭素量(TOC)として9.1g
/l含む実際の無電解ニッケルめっき老化液をpH3.
0に保ち酸化処理した。溶液300mlを容量300m
l用の内部照射型光化学反応装置に入れ、これに白金担
持した二酸化チタン粉末を8g/l共存させ、空気を3
1/minの割合で吹き込みながら高圧水銀灯で照射し
た結果、50時間で100%りん酸イオンに酸化され、
55時間でTOCが50mg/l以下になった。
Hypophosphite ion 10.4 g / l, phosphite ion 52.8 g / l, phosphate ion 0.6 g / l,
And organic acid has an organic carbon content (TOC) of 9.1 g
PH of the actual electroless nickel plating aging liquid containing 1 / l.
It was kept at 0 and subjected to oxidation treatment. 300 ml of solution with a volume of 300 m
It was placed in an internal irradiation type photochemical reaction device for 1 l, and 8 g / l of platinum-supported titanium dioxide powder was made to coexist therein, and air was added to
As a result of irradiation with a high pressure mercury lamp while blowing at a rate of 1 / min, it was oxidized to 100% phosphate ions in 50 hours,
The TOC became 50 mg / l or less in 55 hours.

【0032】[0032]

【発明の効果】 したがってこの方法では、めっき老化
液から短時間に効率よく、しかも酸化処理薬品を使用せ
ずに経済的に次亜りん酸イオンをりん酸イオンに酸化さ
せ、りん酸イオンとしての再利用やりん酸カルシウムと
して処理しやすくする。また、使用した光触媒も回収再
利用する。
Therefore, according to this method, the hypophosphite ion is efficiently oxidized from the plating aging solution in a short time and economically without using an oxidizing chemical, and the phosphate ion is converted into the phosphate ion. Make it easy to reuse or process as calcium phosphate. Also, the used photocatalyst is recovered and reused.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 次亜りん酸イオンを含むめっき老化液を
pH1〜4に保ち、貴金属を担持した二酸化チタン粉末
を光触媒として共存させ、酸素または空気を老化液中に
吹き込みながら光を照射し次亜りん酸イオンを酸化して
りん酸イオンにし、次いでpHを1〜3に保って濾過し
て貴金属を担持した二酸化チタン粉末を回収することを
特徴とするめっき老化液中の次亜りん酸イオンの処理方
法。
1. A plating aging solution containing hypophosphite ions is maintained at pH 1 to 4, titanium dioxide powder carrying a noble metal is allowed to coexist as a photocatalyst, and oxygen or air is blown into the aging solution to irradiate light. A hypophosphite ion in a plating aging solution, characterized in that the phosphite ion is oxidized to a phosphate ion, and the titanium dioxide powder carrying a noble metal is recovered by filtering while maintaining the pH at 1 to 3. Processing method.
JP31290592A 1992-10-28 1992-10-28 Treatment of hypophosphite ions in plating aging solution Expired - Fee Related JP2603895B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
JP31290592A JP2603895B2 (en) 1992-10-28 1992-10-28 Treatment of hypophosphite ions in plating aging solution

Publications (2)

Publication Number Publication Date
JPH06136549A true JPH06136549A (en) 1994-05-17
JP2603895B2 JP2603895B2 (en) 1997-04-23

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Country Status (1)

Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0729436A1 (en) * 1993-10-22 1996-09-04 Crc For Waste Management And Pollution Control Limited Photoassisted oxidation of species in solution
JP2010179214A (en) * 2009-02-04 2010-08-19 Eco Earth Engineering Kk Waste liquid treatment method
CN102644070A (en) * 2012-05-18 2012-08-22 濮阳市海林特种设备制造防护有限公司 Tube pass-plating method for air cooler
CN104045189A (en) * 2014-07-04 2014-09-17 安徽安纳达钛业股份有限公司 Comprehensive treatment method of phosphorous production wastewater

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0729436A1 (en) * 1993-10-22 1996-09-04 Crc For Waste Management And Pollution Control Limited Photoassisted oxidation of species in solution
EP0729436A4 (en) * 1993-10-22 1996-10-09
JP2010179214A (en) * 2009-02-04 2010-08-19 Eco Earth Engineering Kk Waste liquid treatment method
CN102644070A (en) * 2012-05-18 2012-08-22 濮阳市海林特种设备制造防护有限公司 Tube pass-plating method for air cooler
CN104045189A (en) * 2014-07-04 2014-09-17 安徽安纳达钛业股份有限公司 Comprehensive treatment method of phosphorous production wastewater

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