JPH1090212A - Method to detect end point of hydrogen peroxide decomposition reaction and method to collect sulfuric acid from waste liquid employing this detective method - Google Patents

Method to detect end point of hydrogen peroxide decomposition reaction and method to collect sulfuric acid from waste liquid employing this detective method

Info

Publication number
JPH1090212A
JPH1090212A JP24786296A JP24786296A JPH1090212A JP H1090212 A JPH1090212 A JP H1090212A JP 24786296 A JP24786296 A JP 24786296A JP 24786296 A JP24786296 A JP 24786296A JP H1090212 A JPH1090212 A JP H1090212A
Authority
JP
Japan
Prior art keywords
hydrogen peroxide
sulfuric acid
waste liquid
acid
end point
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
JP24786296A
Other languages
Japanese (ja)
Inventor
Tomomi Suzuki
智巳 鈴木
Satoru Nanba
哲 南場
Akio Yoshida
彰男 吉田
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.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
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 Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP24786296A priority Critical patent/JPH1090212A/en
Publication of JPH1090212A publication Critical patent/JPH1090212A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method to detect an end point of hydrogen peroxide decomposition reaction and a method to collect sulfuric acid from waste liquid employing such detective method. SOLUTION: This is a method to detect the reaction end point, when hydrogen peroxide is decomposed and sulfuric acid is formed by introducing sulfurous acid into a solution containing sulfuric acid and hydrogen peroxide and making the hydrogen peroxide react on the sulfurous acid, from a sudden variation of an oxidation-reduction potential measurement occurred at the time reaction termination caused by an oxidation-reduction potential electrode dipped in the solution. By utilizing this method, hydrogen peroxide is decomposed and sulfuric acid is formed by introducing sulfurous acid into a solution containing sulfuric acid and hydrogen peroxide and making the hydrogen peroxide and the sulfurous acid react on each other.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、硫酸および過酸化
水素を含む廃液から硫酸を回収する際の、亜硫酸の添加
量を酸化還元電位電極(以下ORP電極とも記す)によ
り検出したORP測定値の急激な変化から、制御する方
法に関する。
The present invention relates to an ORP measurement value obtained by detecting the amount of sulfurous acid added by a redox potential electrode (hereinafter also referred to as an ORP electrode) when recovering sulfuric acid from a waste liquid containing sulfuric acid and hydrogen peroxide. It relates to a method of controlling a sudden change.

【0002】[0002]

【従来の技術】硫酸および過酸化水素を含む溶液は、エ
ッチング剤、表面処理剤等として、半導体の製造、プリ
ント配線板の製造、レジスト剥離工程、各種金属の表面
加工などに多用されている。この、硫酸および過酸化水
素を含む溶液(以下、「硫酸−過酸化水素溶液」と記す
こともある)は、硫酸および過酸化水素を含むため、ア
ルカリ剤による酸の中和処理と、過酸化水素の除去処理
をしなければ処分することができない。また、含まれる
硫酸を種々有効利用する場合も、硫酸−過酸化水素溶液
中に含まれる過酸化水素が有害であり、過酸化水素の除
去が必要である。
2. Description of the Related Art Solutions containing sulfuric acid and hydrogen peroxide are frequently used as an etching agent, a surface treatment agent, etc. in the production of semiconductors, the production of printed wiring boards, the resist stripping step, the surface processing of various metals, and the like. Since the solution containing sulfuric acid and hydrogen peroxide (hereinafter sometimes referred to as “sulfuric acid-hydrogen peroxide solution”) contains sulfuric acid and hydrogen peroxide, it is subjected to an acid neutralization treatment with an alkaline agent, It cannot be disposed of without hydrogen removal treatment. Also, in the case where the sulfuric acid contained therein is used variously effectively, the hydrogen peroxide contained in the sulfuric acid-hydrogen peroxide solution is harmful, and it is necessary to remove the hydrogen peroxide.

【0003】過酸化水素を除去するための方法として
は、過酸化水素分解触媒へ水素を供給しながら過酸化水
素を分解処理する方法(特開昭61−186208号公
報)、無電解銅メッキ触媒用のキャタリスト溶液を使用
する方法(特開平3−86298号公報)、炭素質物質
へ温度を上げた廃液を通じて過酸化水素を分解処理する
方法(特開平5−345188号公報)が知られてい
る。しかし、過酸化水素分解触媒へ水素を供給しながら
過酸化水素を分解する方法では、非常に可燃性の高い水
素ガスを使用する必要があり、また触媒の活性低下の問
題もある。無電解銅メッキ触媒用のキャタリスト溶液を
使用する方法では、無電解銅メッキ触媒用のキャタリス
ト溶液が必要であり、この溶液が入手できない場面では
使用できない問題がある。炭素質物質へ温度を上げた廃
液を通じて過酸化水素を分解処理する方法では、過酸化
水素を含む強酸性の溶液を加熱処理することに伴う危険
性があり、さらに加熱のためのエネルギーも必要となる
問題がある。
As a method for removing hydrogen peroxide, a method of decomposing hydrogen peroxide while supplying hydrogen to a hydrogen peroxide decomposition catalyst (Japanese Patent Laid-Open No. 61-186208), an electroless copper plating catalyst (JP-A-3-86298) and a method of decomposing hydrogen peroxide through a waste liquid having a raised temperature to a carbonaceous material (JP-A-5-345188). I have. However, in the method of decomposing hydrogen peroxide while supplying hydrogen to the hydrogen peroxide decomposition catalyst, it is necessary to use extremely flammable hydrogen gas, and there is a problem that the activity of the catalyst is reduced. The method using a catalyst solution for an electroless copper plating catalyst requires a catalyst solution for an electroless copper plating catalyst, and has a problem that it cannot be used when this solution is not available. In the method of decomposing hydrogen peroxide through a waste liquid at an elevated temperature to a carbonaceous substance, there is a risk associated with heating a strongly acidic solution containing hydrogen peroxide, and furthermore, energy for heating is also required. There is a problem.

【0004】そして、これらの方法を実施するために過
酸化水素の濃度の測定が必要であり、従来は容量分析
法、比色分析法、ORP電極による分析方法(特開平3
−216544号公報)が知られていた。ORP電極に
よる分析方法は、容量分析法や比色分析法に比べて測定
が簡易であることから、過酸化水素を含む水溶液と還元
物との酸化還元反応で特に利用されてきた。しかし、例
えば、過マンガン酸カリウムと過酸化水素の酸化還元反
応を利用した、ORP電極を用いる特開平3−2165
44号公報記載の方法では、測定による誤差が多く、正
確に反応の終点を検出することが出来なかった。
In order to carry out these methods, it is necessary to measure the concentration of hydrogen peroxide. Conventionally, a capacitance analysis method, a colorimetric analysis method, and an analysis method using an ORP electrode (Japanese Unexamined Patent Application Publication No.
-216544) was known. The analysis method using an ORP electrode has been particularly used in the oxidation-reduction reaction between an aqueous solution containing hydrogen peroxide and a reduced product because the measurement method is simpler than the capacitance analysis method and the colorimetric analysis method. However, for example, JP-A-3-2165 using an ORP electrode utilizing an oxidation-reduction reaction between potassium permanganate and hydrogen peroxide.
In the method described in Japanese Patent No. 44-44, there are many errors due to measurement, and the end point of the reaction cannot be detected accurately.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、従来
の過酸化水素濃度測定法の欠点を克服した測定法を提供
するとともに該測定法を用いた硫酸および過酸化水素を
含む廃液からの硫酸の回収方法を提供することである。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a measuring method which overcomes the drawbacks of the conventional hydrogen peroxide concentration measuring method, and to use the measuring method to remove sulfuric acid and hydrogen peroxide from a waste liquid. It is to provide a method for recovering sulfuric acid.

【0006】[0006]

【課題を解決するための手段】本願発明者らは上記目的
を達成すべく鋭意研究した結果、本発明に到達した。即
ち本発明は、(1)硫酸及び過酸化水素を含む溶液へ亜
硫酸を導入し、過酸化水素と亜硫酸を反応させ、過酸化
水素を分解すると共に硫酸を生成させる際、該溶液に浸
漬した酸化還元電位電極によって、反応終了時に起こる
酸化還元電位測定値の急激な変化から、該反応の終点を
検出する方法、及び(2)硫酸及び過酸化水素を含む廃
液へ亜硫酸を導入し、過酸化水素と亜硫酸を反応させ、
過酸化水素を分解すると共に硫酸を生成させ、該反応の
終点を上記(1)記載の方法により測定することを特徴
とする硫酸および過酸化水素を含む廃液からの硫酸の回
収方法、に関するものである。
Means for Solving the Problems The present inventors have made intensive studies to achieve the above object, and as a result, have reached the present invention. That is, the present invention relates to (1) introducing sulfurous acid into a solution containing sulfuric acid and hydrogen peroxide, reacting the hydrogen peroxide with sulfurous acid to decompose hydrogen peroxide and generate sulfuric acid; A method for detecting the end point of the reaction from a sudden change in the measured oxidation-reduction potential at the end of the reaction by a reduction potential electrode, and (2) introducing sulfurous acid into a waste liquid containing sulfuric acid and hydrogen peroxide, With sulfurous acid,
A method for recovering sulfuric acid from a waste liquid containing sulfuric acid and hydrogen peroxide, wherein hydrogen peroxide is decomposed and sulfuric acid is generated, and the end point of the reaction is measured by the method described in (1) above. is there.

【0007】[0007]

【発明の実施の形態】本発明が対象とする硫酸及び過酸
化水素を含む水溶液及び廃水中には硫酸及び過酸化水素
のほかに重金属イオンや無機塩等の無機物、有機酸塩等
の有機物が共存していても問題ない。硫酸及び過酸化水
素を含む水溶液及び廃水中の硫酸濃度は特に限定されな
いが、好ましくは30%以上である。硫酸及び過酸化水
素を含む水溶液及び廃水中の過酸化水素濃度には限定は
ない。本発明に使用することのできる亜硫酸としては亜
硫酸ガス、液体亜硫酸、亜硫酸水溶液等が挙げられる。
本発明を実施する場合の反応温度は特に限定されない
が、好ましくは0〜290℃である。本発明によれば、
硫酸及び過酸化水素含有廃液中の過酸化水素のみを分解
除去することができ、処理後の溶液を硫酸溶液として再
使用したり、排水処理のPH調製などに利用することも
可能となる。次に本発明を実施例により説明するが、本
発明はこれに限定されない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In addition to sulfuric acid and hydrogen peroxide, inorganic substances such as heavy metal ions and inorganic salts, and organic substances such as organic acid salts are contained in the aqueous solution and wastewater containing sulfuric acid and hydrogen peroxide which are the object of the present invention. There is no problem if they coexist. The concentration of sulfuric acid in the aqueous solution containing sulfuric acid and hydrogen peroxide and the wastewater is not particularly limited, but is preferably 30% or more. The concentration of hydrogen peroxide in the aqueous solution containing sulfuric acid and hydrogen peroxide and the wastewater is not limited. Examples of the sulfurous acid that can be used in the present invention include sulfurous acid gas, liquid sulfurous acid, and an aqueous solution of sulfurous acid.
The reaction temperature for carrying out the present invention is not particularly limited, but is preferably 0 to 290 ° C. According to the present invention,
Only the hydrogen peroxide in the sulfuric acid and hydrogen peroxide-containing waste liquid can be decomposed and removed, and the treated solution can be reused as a sulfuric acid solution or used for pH adjustment of wastewater treatment. Next, the present invention will be described with reference to examples, but the present invention is not limited thereto.

【0008】[0008]

【実施例】【Example】

実施例1 液温22℃、過酸化水素濃度2.5%、硫酸濃度85.
0%の硫酸及び過酸化水素含有廃液100mlを密閉容
器に入れ、下部より亜硫酸ガスを100ml/分の流量
で導入して、逐次残留過酸化水素濃度、硫酸濃度、OR
P値を測定した。また溶液中の亜硫酸イオン濃度も必要
に応じて測定した。反応終点時における液温は47℃で
あった。その結果を図1に示した。
Example 1 Liquid temperature 22 ° C., hydrogen peroxide concentration 2.5%, sulfuric acid concentration 85.
100 ml of 0% sulfuric acid and hydrogen peroxide-containing waste liquid is placed in a closed container, and sulfurous acid gas is introduced from the bottom at a flow rate of 100 ml / min, and the residual hydrogen peroxide concentration, sulfuric acid concentration, OR
The P value was measured. Also, the sulfite ion concentration in the solution was measured as necessary. The liquid temperature at the end of the reaction was 47 ° C. The result is shown in FIG.

【0009】[0009]

【発明の効果】本発明のORP測定値による亜硫酸の制
御を利用した硫酸および過酸化水素を含む廃液からの硫
酸の回収方法によれば、従来有効利用できなかった硫酸
および過酸化水素を含む廃液中の過酸化水素のみを除去
し、処理後の溶液を硫酸溶液として再使用したり排水処
理のpH調整剤として有効利用することができる。
According to the method of the present invention for recovering sulfuric acid from a waste liquid containing sulfuric acid and hydrogen peroxide utilizing the control of sulfurous acid based on the measured ORP value, the waste liquid containing sulfuric acid and hydrogen peroxide which could not be effectively used conventionally. Only hydrogen peroxide in the solution is removed, and the treated solution can be reused as a sulfuric acid solution or effectively used as a pH adjuster for wastewater treatment.

【0010】[0010]

【図面の簡単な説明】[Brief description of the drawings]

【図1】硫酸及び過酸化水素を含む廃液へ亜硫酸を導入
し、過酸化水素と亜硫酸を反応させ、過酸化水素を分解
すると共に硫酸を生成させた場合の溶液のORP電位及
び過酸化水素濃度の経時変化を示す。
FIG. 1 shows the ORP potential and hydrogen peroxide concentration of a solution in which sulfurous acid is introduced into a waste liquid containing sulfuric acid and hydrogen peroxide, the hydrogen peroxide reacts with sulfurous acid to decompose hydrogen peroxide and generate sulfuric acid. Shows the change over time.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 硫酸及び過酸化水素を含む溶液へ亜硫酸
を導入し、過酸化水素と亜硫酸を反応させ、過酸化水素
を分解すると共に硫酸を生成させる際、該溶液に浸漬し
た酸化還元電位電極によって、反応終了時に起こる酸化
還元電位測定値の急激な変化から、該反応の終点を検出
する方法。
1. An oxidation-reduction potential electrode immersed in a solution containing sulfuric acid and hydrogen peroxide when the sulfuric acid is introduced into the solution and the hydrogen peroxide reacts with the sulfurous acid to decompose the hydrogen peroxide and generate sulfuric acid. A method of detecting the end point of the reaction from a sudden change in the measured value of the oxidation-reduction potential at the end of the reaction.
【請求項2】 硫酸及び過酸化水素を含む廃液へ亜硫酸
を導入し、過酸化水素と亜硫酸を反応させ、過酸化水素
を分解すると共に硫酸を生成させ、該反応の終点を請求
項1記載の方法により測定することを特徴とする硫酸お
よび過酸化水素を含む廃液からの硫酸の回収方法。
2. The method according to claim 1, wherein sulfurous acid is introduced into a waste liquid containing sulfuric acid and hydrogen peroxide, and the hydrogen peroxide and sulfurous acid are reacted to decompose hydrogen peroxide and generate sulfuric acid. A method for recovering sulfuric acid from a waste liquid containing sulfuric acid and hydrogen peroxide, which is measured by a method.
JP24786296A 1996-09-19 1996-09-19 Method to detect end point of hydrogen peroxide decomposition reaction and method to collect sulfuric acid from waste liquid employing this detective method Pending JPH1090212A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24786296A JPH1090212A (en) 1996-09-19 1996-09-19 Method to detect end point of hydrogen peroxide decomposition reaction and method to collect sulfuric acid from waste liquid employing this detective method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24786296A JPH1090212A (en) 1996-09-19 1996-09-19 Method to detect end point of hydrogen peroxide decomposition reaction and method to collect sulfuric acid from waste liquid employing this detective method

Publications (1)

Publication Number Publication Date
JPH1090212A true JPH1090212A (en) 1998-04-10

Family

ID=17169753

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24786296A Pending JPH1090212A (en) 1996-09-19 1996-09-19 Method to detect end point of hydrogen peroxide decomposition reaction and method to collect sulfuric acid from waste liquid employing this detective method

Country Status (1)

Country Link
JP (1) JPH1090212A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011065257A1 (en) * 2009-11-30 2011-06-03 三菱重工業株式会社 Desalting system and method of desalting

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011065257A1 (en) * 2009-11-30 2011-06-03 三菱重工業株式会社 Desalting system and method of desalting
JP2011110531A (en) * 2009-11-30 2011-06-09 Mitsubishi Heavy Ind Ltd Desalination apparatus and desalination method
US8920653B2 (en) 2009-11-30 2014-12-30 Mitsubishi Heavy Industries, Ltd. Desalination apparatus and desalination method

Similar Documents

Publication Publication Date Title
CA1275378C (en) Method of controlling an aluminum surface cleaning composition
GB2027004A (en) Method of treating nitrate-containing waste water
JP5284196B2 (en) Method for quantitative analysis of selenium
JP2021535998A (en) Systems and methods for measuring water composition
JPH1090212A (en) Method to detect end point of hydrogen peroxide decomposition reaction and method to collect sulfuric acid from waste liquid employing this detective method
JPH1028982A (en) Treatment of waste liquid containing ammonia-state nitrogen
US6733679B2 (en) Method of treating an electroless plating waste
JP4603128B2 (en) Cupric chloride / sodium chlorate etching system
JP2001276619A (en) Method of decomposing hydrogen peroxide and pretreatment method for electrochemical analysis of liquid to be inspected containing hydrogen peroxide
JPH0336598B2 (en)
RU2696381C2 (en) Reagent method for regeneration of copper-ammonia solution of copper etching
JP4423734B2 (en) Cyanide wastewater treatment method
JPH078971A (en) Treatment of ammonium fluoride-containing water
JPH0551326B2 (en)
KR100467266B1 (en) A treatment method of high concentrated phenolsulfonic acid containing tin-plated wastewaters
JPH09315806A (en) Recovering method of sulfuric acid from waste solution containing sulfuric acid and hydrogen peroxide
JP3549951B2 (en) Ultra-trace nitrogen component measurement device
JPH06304581A (en) Treatment of waste solution
JPH0780482A (en) Treatment of waste liquid
MXPA06012988A (en) Method and apparatus utilising hydrogen peroxyde to reduce sox, nox and heavy metal emissions.
JPH04176385A (en) Method for decomposing organic chlorine compound
RU2139593C1 (en) Method for continuous chemical liquid cleaning of polymer-covered surfaces of parts, primarily semiconductor plates
SU973671A1 (en) Method for regenerating non-aqueous liquors for pickling copper
JP6379777B2 (en) Method for treating hydrogen peroxide-containing water
Korolczuk Application of cold vapor differential pulse voltammetric method for determination of mercury in urine samples

Legal Events

Date Code Title Description
A977 Report on retrieval

Effective date: 20050414

Free format text: JAPANESE INTERMEDIATE CODE: A971007

A131 Notification of reasons for refusal

Effective date: 20050607

Free format text: JAPANESE INTERMEDIATE CODE: A131

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20051102