JPH0884994A - Treatment of liquid containing oxidizing agent - Google Patents
Treatment of liquid containing oxidizing agentInfo
- Publication number
- JPH0884994A JPH0884994A JP24854994A JP24854994A JPH0884994A JP H0884994 A JPH0884994 A JP H0884994A JP 24854994 A JP24854994 A JP 24854994A JP 24854994 A JP24854994 A JP 24854994A JP H0884994 A JPH0884994 A JP H0884994A
- Authority
- JP
- Japan
- Prior art keywords
- oxidizing agent
- palladium
- molybdenum
- tungsten
- platinum
- 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
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Catalysts (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、酸化剤含有液の処理方
法に係わるもので、特にか過酢酸や過酸化水素等の酸化
剤を含有した廃液の処理方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating an oxidizing agent-containing liquid, and more particularly to a method for treating a waste liquid containing an oxidizing agent such as peracetic acid or hydrogen peroxide.
【0002】[0002]
【従来の技術】現在半導体製造工場排水システムからは
過酢酸や過酸化水素を含む廃液が多量に排出されてお
り、またその他化学工場等からも諸々の酸化剤を含む廃
液が排出されており、その処理が重要問題とされてい
る。従来、これらの酸化剤の分解は、活性炭塔による分
解、亜硫酸ナトリウムの還元剤の添加による分解廃液中
の他の有機物との接触による分解が行われていた。2. Description of the Related Art At present, a large amount of waste liquid containing peracetic acid and hydrogen peroxide is discharged from a drainage system of a semiconductor manufacturing plant, and waste liquid containing various oxidizing agents is also discharged from other chemical plants. The treatment is regarded as an important issue. Heretofore, the decomposition of these oxidizers has been carried out by decomposition with an activated carbon tower and by contact with other organic substances in the decomposition waste liquid by addition of a reducing agent of sodium sulfite.
【0003】ところが上記のような方法をとっても、活
性炭塔による分解では活性炭層内に微生物が多数増殖
し、回収水の水質を悪化させたり、また亜硫酸ナトリウ
ム等の還元剤の添加による処理では還元剤のコストによ
る処理費の増加、還元剤添加量のコントロールが微妙で
あり、還元剤との反応により生じる塩の増加等問題が多
数生じていた。また有機物との反応では処理費の増加や
生成する塩の増加等の問題はないものの、反応速度がゆ
るやかであり、大量に処理しようとすると、分解が間に
合わず、酸化剤が残留したまま排水として放出されてし
まうといった問題が生じていた。However, even if the above method is adopted, a large number of microorganisms grow in the activated carbon layer due to decomposition by the activated carbon tower, deteriorating the water quality of the recovered water, and reducing the reducing agent in the treatment by adding a reducing agent such as sodium sulfite. However, there were many problems such as an increase in processing cost due to the above-mentioned cost, delicate control of the amount of reducing agent added, and an increase in salt generated by the reaction with the reducing agent. In addition, the reaction with organic substances does not cause problems such as increase of treatment cost and increase of generated salt, but the reaction rate is slow, and if a large amount of treatment is attempted, decomposition cannot be done in time and oxidizer remains as waste water. There was a problem that it was released.
【0004】[0004]
【発明が解決しようとする課題】本発明は、従来行われ
ていた上記問題点を解決するためになされたもので、処
理費が易く、簡単な操作で迅速に多量の酸化剤を分解で
きる、酸化剤含有液の処理方法を提供するものである。DISCLOSURE OF THE INVENTION The present invention has been made in order to solve the above-mentioned problems that have hitherto been made, and the treatment cost is easy, and a large amount of oxidizing agent can be decomposed rapidly by a simple operation. A method for treating an oxidant-containing liquid is provided.
【0005】[0005]
【課題を解決するための手段】上記目的は、耐食性金属
基体上に白金−タングステン、白金−モリブデン、パラ
ジウム−タングステン又はパラジウム−モリブデンの合
金被覆を有する触媒と酸化剤含有液を接触させ、酸化剤
を分解することにより達成される。なお、上記触媒と酸
化剤含有液の接触は、触媒収納容器へ酸化剤含有液を循
環供給することにより効率よく達成される。また、上記
合金被覆は電気めっきにより得られた合金被覆であるこ
とが好ましい。さらに、上記耐食性金属基体としてはス
テンレス、チタンなどが好ましいものである。The above object is to bring a catalyst having an alloy coating of platinum-tungsten, platinum-molybdenum, palladium-tungsten, or palladium-molybdenum on a corrosion-resistant metal substrate into contact with an oxidizing agent-containing liquid to form an oxidizing agent. Is achieved by decomposing. The contact between the catalyst and the oxidant-containing liquid is efficiently achieved by circulatingly supplying the oxidant-containing liquid to the catalyst container. The alloy coating is preferably an alloy coating obtained by electroplating. Furthermore, as the above-mentioned corrosion resistant metal substrate, stainless steel, titanium and the like are preferable.
【0006】[0006]
【作用】本発明者らは以前白金−タングステン、白金−
モリブデン、パラジウム−タングステン、パラジウム−
モリブデン等のめっき析出被覆が触媒活性を有し、特に
ヒドラジン等の還元剤を分解するのに有効であることを
見いだした。(特開平6−379号公報、特開平6−3
1167号公報)ところがその後、上記めっきで得られ
た合金触媒は酸化剤を分解する還元触媒能力も有してい
ることがあきらかとなり、過酢酸等の酸化剤の処理が可
能となった。この方法によれば、酸化剤は無害な化合物
に分解されて(例えば過酢酸は水と酢酸)、さらに他の
薬品の投入の必要もなく、反応による副生成物の心配も
ない上、反応速度が速い為、大量処理が可能となる。The present inventors have previously used platinum-tungsten, platinum-
Molybdenum, palladium-tungsten, palladium-
It has been found that a plating deposition coating such as molybdenum has catalytic activity and is particularly effective for decomposing a reducing agent such as hydrazine. (JP-A-6-379, JP-A-6-3
After that, however, it became clear that the alloy catalyst obtained by the above plating also had a reducing catalyst capacity for decomposing the oxidizing agent, and it became possible to treat the oxidizing agent such as peracetic acid. According to this method, the oxidant is decomposed into harmless compounds (for example, peracetic acid is water and acetic acid), there is no need to add other chemicals, there is no fear of by-products from the reaction, and the reaction rate is high. Since it is fast, large-scale processing is possible.
【0007】触媒と酸化剤含有液の接触は、液中へ触媒
を投入するだけでも可能であるが、触媒収納容器を設
け、そこへ酸化剤含有液を巡回供給することにより効率
良く酸化剤が分解できる。なお、上記触媒の基体として
用いられる耐食性金属基体としては、特に限定されるも
のでないが、入手の容易なステンレス、チタン等が用い
られる。The catalyst can be brought into contact with the oxidant-containing liquid simply by introducing the catalyst into the liquid, but by providing a catalyst storage container and circulatingly supplying the oxidant-containing liquid, the oxidant can be efficiently supplied. Can be disassembled. The corrosion-resistant metal substrate used as the catalyst substrate is not particularly limited, but readily available stainless steel, titanium, or the like is used.
【0008】[0008]
【実施例1】直径 0.3mmのステンレス鋼線よりなる35メ
ッシュの網(50mm×50mm)を、電解脱脂剤(日本エレク
トロプレイティング・エンジニヤース社製:イートレッ
クス♯12)の5%水溶液中において60℃、電圧5V、で
60秒間電解脱脂をおこない、水洗ののち6規定塩酸水溶
液に30秒間浸漬、さらに水洗ののち、金ストライクメッ
キ浴(日本エレクトロプレイティング・エンジニヤース
社製:オーロボンドTCL)により50℃、電圧2Vで60
秒間金メッキを行った。その後、水洗し、5%硫酸水溶
液に30秒間浸漬、水洗の工程を経て以下に示すパラジウ
ム−モリブデン合金メッキ浴にて、下記条件でメッキを
行い、所望のパラジウム−モリブデン共析メッキ被覆3
gのついた触媒を得た。 (メッキ浴) 塩化パラジウム 1.5g モリブデン酸ナトリウム 60g リン酸緩衝液 少々 リン酸アンモニウム塩 少々[Example 1] A 35-mesh net (50 mm x 50 mm) made of stainless steel wire having a diameter of 0.3 mm was placed in a 5% aqueous solution of an electrolytic degreasing agent (manufactured by Nippon Electroplating Engineers: Eatrex # 12). At 60 ℃, voltage 5V
Electrolyte degreasing is performed for 60 seconds, followed by washing with water, dipping in 6N hydrochloric acid solution for 30 seconds, further washing with water, and then using a gold strike plating bath (Nippon Electroplating Engineers: Aurobond TCL) at 50 ° C, voltage 2V 60
Gold plated for seconds. Then, after washing with water, immersing in a 5% sulfuric acid aqueous solution for 30 seconds, and washing with water, plating is performed in the following palladium-molybdenum alloy plating bath under the following conditions, and the desired palladium-molybdenum eutectoid coating 3
A catalyst with g was obtained. (Plating bath) Palladium chloride 1.5 g Sodium molybdate 60 g Phosphate buffer solution Ammonium phosphate salt
【0009】以上を 800mlの水に溶解した後、 0.5N水
酸化ナトリウム水溶液にてpHを調整し、最終的に水で
1000mlに希釈した。 (メッキ条件) 温度 60℃ 電流密度 0.3A/dm2 メッキ時間 6.5分間 得られたメッキ被覆は、モリブデン13.1重量%、パラジ
ウム86.9重量%の共析メッキ被覆であった。After the above was dissolved in 800 ml of water, the pH was adjusted with 0.5N sodium hydroxide aqueous solution and finally with water.
Diluted to 1000 ml. (Plating conditions) Temperature 60 ° C. Current density 0.3 A / dm 2 Plating time 6.5 minutes The obtained plating coating was 13.1% by weight of molybdenum and 86.9% by weight of palladium.
【0010】得られたパラジウム−モリブデン合金被覆
の触媒を用いて過酢酸の分解を行った。10lの反応容器
に過酢酸 4,000ppm を含有した廃液を用意し、上記触媒
を収納した容器に循環供給した。(常温・常圧)1時間
循環を続けた後、廃液を採取し過酢酸の濃度を測定した
ところ、ほぼ6ppm であった。さらに循環を続け2時間
経過後再度廃液を採取し過酢酸の濃度を測定したとこ
ろ、ほぼ0ppm であった。Decomposition of peracetic acid was carried out using the obtained catalyst coated with a palladium-molybdenum alloy. A waste liquid containing 4,000 ppm of peracetic acid was prepared in a 10-liter reaction container and circulated and supplied to the container containing the above catalyst. After circulating for 1 hour (at room temperature and atmospheric pressure), the waste liquid was collected and the concentration of peracetic acid was measured and found to be about 6 ppm. The circulation was further continued, and after 2 hours, the waste liquid was collected again and the concentration of peracetic acid was measured, and it was found to be almost 0 ppm.
【0011】[0011]
【従来例1】実施例1で用いたのと同じ廃液10lを用意
し、亜硫酸ナトリウムを添加して分解を試みた。亜硫酸
ナトリウム10gを添加し、2時間撹拌したが、過酢酸は
1,000ppmにしか下がらず、さらに亜硫酸ナトリウムを10
g添加して6時間撹拌したところ、過酢酸の分解は完了
したが、亜硫酸ナトリウムの入れ過ぎのためCODが 1
2,000ppmとなり排水への放流が不可能となってしまっ
た。Conventional Example 1 10 l of the same waste liquid as that used in Example 1 was prepared, and sodium sulfite was added thereto to try to decompose it. Sodium sulfite (10 g) was added and stirred for 2 hours.
It only drops to 1,000ppm, and 10% of sodium sulfite is added.
When g was added and the mixture was stirred for 6 hours, the decomposition of peracetic acid was completed, but COD was 1 due to the excessive addition of sodium sulfite.
It became 2,000 ppm, and it became impossible to discharge it to wastewater.
【0012】[0012]
【発明の効果】以上の通り、本発明の酸化剤含有液の処
理方法によれば、安い処理費、簡単な操作で迅速に多量
の酸化剤を分解処理することができ廃水処理コストの低
減に大いに役立つものである。As described above, according to the method for treating an oxidant-containing liquid of the present invention, a large amount of oxidant can be decomposed rapidly with a low treatment cost and a simple operation, and the wastewater treatment cost can be reduced. It is very useful.
Claims (5)
ン、白金−モリブデン、パラジウム−タングステン又は
パラジウム−モリブデンの合金被覆を有する触媒を触媒
収納容器に入れ酸化剤含有液を触媒収納容器へ循環供給
することにより酸化剤を分解する、酸化剤含有液の処理
方法。1. A catalyst having a platinum-tungsten, platinum-molybdenum, palladium-tungsten, or palladium-molybdenum alloy coating on a corrosion-resistant metal substrate is placed in a catalyst storage container, and an oxidant-containing liquid is circulated and supplied to the catalyst storage container. A method for treating an oxidant-containing liquid, which comprises decomposing the oxidant with.
た合金被覆である請求項1記載の酸化剤含有液の処理方
法。2. The method for treating an oxidizing agent-containing liquid according to claim 1, wherein the alloy coating is an alloy coating obtained by electroplating.
ングステン、白金−モリブデン、パラジウム−タングス
テン又はパラジウム−モリブデンとの間に金めっきの中
間層を有している。請求項2記載の酸化剤含有液の処理
方法。3. The catalyst has a gold-plated intermediate layer between a corrosion resistant metal substrate and platinum-tungsten, platinum-molybdenum, palladium-tungsten or palladium-molybdenum. The method for treating an oxidizing agent-containing liquid according to claim 2.
る請求項1、2又は3記載の酸化剤含有液の処理方法。4. The method for treating an oxidizing agent-containing liquid according to claim 1, 2 or 3, wherein the corrosion-resistant metal substrate is stainless steel.
求項1、2又は3記載の酸化剤含有液の処理方法。5. The method for treating an oxidant-containing solution according to claim 1, 2 or 3, wherein the corrosion-resistant metal substrate is titanium.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24854994A JPH0884994A (en) | 1994-09-17 | 1994-09-17 | Treatment of liquid containing oxidizing agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24854994A JPH0884994A (en) | 1994-09-17 | 1994-09-17 | Treatment of liquid containing oxidizing agent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0884994A true JPH0884994A (en) | 1996-04-02 |
Family
ID=17179834
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24854994A Pending JPH0884994A (en) | 1994-09-17 | 1994-09-17 | Treatment of liquid containing oxidizing agent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0884994A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014064971A (en) * | 2012-09-25 | 2014-04-17 | Japan Organo Co Ltd | Treatment apparatus of peracetic acid-containing effluent and treatment method of peracetic acid-containing effluent |
CN104961273A (en) * | 2015-06-16 | 2015-10-07 | 广州超邦化工有限公司 | Method for treating alkaline zinc-nickel alloy electroplating wastewater |
JP2016059901A (en) * | 2014-09-19 | 2016-04-25 | カーリットホールディングス株式会社 | Catalyst cartridge and peroxide-containing aqueous solution treatment apparatus equipped with the same |
JP2016107216A (en) * | 2014-12-08 | 2016-06-20 | 栗田工業株式会社 | Apparatus and method for treating waste water containing peracetic acid |
-
1994
- 1994-09-17 JP JP24854994A patent/JPH0884994A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014064971A (en) * | 2012-09-25 | 2014-04-17 | Japan Organo Co Ltd | Treatment apparatus of peracetic acid-containing effluent and treatment method of peracetic acid-containing effluent |
JP2016059901A (en) * | 2014-09-19 | 2016-04-25 | カーリットホールディングス株式会社 | Catalyst cartridge and peroxide-containing aqueous solution treatment apparatus equipped with the same |
JP2016107216A (en) * | 2014-12-08 | 2016-06-20 | 栗田工業株式会社 | Apparatus and method for treating waste water containing peracetic acid |
CN104961273A (en) * | 2015-06-16 | 2015-10-07 | 广州超邦化工有限公司 | Method for treating alkaline zinc-nickel alloy electroplating wastewater |
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