JPH0724479A - Treatment of waste water - Google Patents

Treatment of waste water

Info

Publication number
JPH0724479A
JPH0724479A JP17526093A JP17526093A JPH0724479A JP H0724479 A JPH0724479 A JP H0724479A JP 17526093 A JP17526093 A JP 17526093A JP 17526093 A JP17526093 A JP 17526093A JP H0724479 A JPH0724479 A JP H0724479A
Authority
JP
Japan
Prior art keywords
treatment
treated
cod
wastewater
reducing
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
JP17526093A
Other languages
Japanese (ja)
Inventor
Satonori Kujiyou
常 哲 令 久
Yoshikatsu Ozaki
崎 佳 克 尾
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP17526093A priority Critical patent/JPH0724479A/en
Publication of JPH0724479A publication Critical patent/JPH0724479A/en
Pending legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To provide a method for quickly and simply reducing COD in a high COD industrial waste water containing reducing materials such as hydrazine, sodium nitrite. CONSTITUTION:At the time of treating the high COD(chemical oxygen demand) industrial waste water containing the reducing materials such as a reducing corrosion inhibitor, the waste water treating method includes a process for treating a water to be treated with hydrogen peroxide aq. solution and decreasing the pH of the water to be treated.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は排水処理に関し、特に還
元性物質を含有する産業排水を浄化するための方法に関
するものであり、特に高COD産業排水における迅速か
つ簡便なCOD低減処理方法を特徴とする排水処理方法
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to wastewater treatment, and more particularly to a method for purifying industrial wastewater containing reducing substances, which is characterized by a rapid and simple COD reduction treatment method for high COD industrial wastewater. The wastewater treatment method.

【0002】[0002]

【従来の技術】発電プラントの給水配管および軸受冷却
水系統には還元性の防錆剤としてヒドラジン(N
2 4 )あるいは亜硝酸ナトリウム(NaNO2 )が通
常使用されている。このため、これらプラント使用溶液
のような高COD排水の排出の際には公害防止条例等で
定められた一定水質以上への浄化処理が必要となる。
2. Description of the Related Art Hydrazine (N) is used as a reducing rust preventive agent in power supply pipes and bearing cooling water systems of power plants.
2 H 4 ) or sodium nitrite (NaNO 2 ) is usually used. For this reason, when discharging high-COD waste water such as the solution used in these plants, it is necessary to purify it to a certain water quality or higher as determined by the pollution prevention regulations.

【0003】従来、このような排水のCOD処理方法と
しては、次亜塩素酸ナトリウム(NaOCl)を添加す
る処理を行ったり、あるいはN2 4 とNaNO2 とを
二つの槽に分離して、それぞれ異なる薬品で処理する方
法が採用されている。
Conventionally, as a COD treatment method for such waste water, a treatment of adding sodium hypochlorite (NaOCl) has been carried out, or N 2 H 4 and NaNO 2 have been separated into two tanks. The method of treating with different chemicals is adopted.

【0004】[0004]

【発明が解決しようとする課題】従来行われている方
法、たとえばNaOClを添加する処理方法において
は、その添加量の制御が繁雑であり、添加量が過剰にな
ると添加したNaOClから遊離塩素が生成し、これが
排水中に不可避的に残留するという問題がある。そのた
め、CODを低く保つことが困難となる。また、NaO
Clの反応時間は比較的長く、さらに上記のように残留
塩素の生成の問題があるため、一度に多量のNaCOl
を添加できないことから、結局、処理を迅速に行うこと
は困難である。
In the conventional method, for example, the treatment method of adding NaOCl, the control of the addition amount is complicated, and when the addition amount becomes excessive, free chlorine is generated from the added NaOCl. However, there is a problem that this inevitably remains in the wastewater. Therefore, it becomes difficult to keep COD low. In addition, NaO
Since the reaction time of Cl is relatively long and there is a problem of residual chlorine formation as described above, a large amount of NaCO
In the end, it is difficult to carry out the treatment promptly, since it is impossible to add.

【0005】一方、NaCOlを使用しない方法におい
ては、N2 4 ならびにNaNO2成分を各々別個の排
水槽に分類し、異なる薬品処理を施す必要があり、排水
処理工程が繁雑かつ長時間化するという問題がある。
On the other hand, in the method which does not use NaCOl, it is necessary to classify the N 2 H 4 and NaNO 2 components into separate drainage tanks and carry out different chemical treatments, which makes the wastewater treatment process complicated and long. There is a problem.

【0006】本発明は上述した従来技術の問題点に鑑み
てなされたものであって、ヒドラジン、亜硝酸ナトリウ
ムなどの還元性物質を含有する高COD産業排水におけ
る迅速かつ簡便なCOD低減処理方法を提供することを
目的とするものである。
The present invention has been made in view of the above-mentioned problems of the prior art, and provides a rapid and simple COD reduction treatment method for high COD industrial wastewater containing a reducing substance such as hydrazine and sodium nitrite. It is intended to be provided.

【0007】[0007]

【課題を解決するための手段】本発明による排水処理方
法は、還元性の防錆剤のような還元性物質を含有する高
COD(化学的酸素消費量)の産業用排水を処理するに
際し、被処理排水を過酸化水素水によって処理し被処理
排水のpHを低下させる工程を含むことを特徴とするも
のである。
The method for treating wastewater according to the present invention, in treating industrial wastewater having a high COD (chemical oxygen consumption) containing a reducing substance such as a reducing rust preventive agent, The method is characterized by including a step of treating the wastewater to be treated with hydrogen peroxide water to reduce the pH of the wastewater to be treated.

【0008】以下、本発明を好ましい具体例にしたがっ
て詳細に説明する。
The present invention will be described in detail below with reference to preferred embodiments.

【0009】図1は本発明による排水処理工程の一例を
示すフローチャート図である。図示のように、通常、防
錆剤であるヒドラジン(N2 4 )ならびに亜硝酸ナト
リウム(NaNO2 )を含有する発電プラントの給水配
管および軸受冷却水系廃液を処理槽へ一時的に貯留し、
これにH2 2 を添加して、処理溶液のpHをpH2.
5以下とする。この処理によって、亜硝酸ナトリウム
(NaNO2 )が有するCOD低減化のための反応が生
じる。
FIG. 1 is a flow chart showing an example of a wastewater treatment process according to the present invention. As shown in the figure, usually, the water supply pipe and bearing cooling water system waste liquid of a power plant containing hydrazine (N 2 H 4 ) and sodium nitrite (NaNO 2 ) which are rust preventives are temporarily stored in a treatment tank,
H 2 O 2 was added thereto to adjust the pH of the treatment solution to pH 2.
It should be 5 or less. This treatment causes a reaction of sodium nitrite (NaNO 2 ) for reducing COD.

【0010】上記の反応に際しては、反応触媒として硫
酸銅のような金属硫酸塩を添加することが好ましい。
In the above reaction, it is preferable to add a metal sulfate such as copper sulfate as a reaction catalyst.

【0011】本発明においては、さらに主として残留ヒ
ドラジン成分を処理するために、上記処理物に対して、
適宜攪拌を行いながら、水酸化ナトリウムなどのpHを
上昇させるアルカリ性化成分を添加して、pHを11.
5に上昇させる。
In the present invention, in order to mainly treat the residual hydrazine component, the above treated product is
While appropriately agitating, add an alkalizing component such as sodium hydroxide that raises the pH to adjust the pH to 11.
Increase to 5.

【0012】[0012]

【作用】このように、本発明による方法においてはN2
4 やNaNO2 のような還元性成分を残留化学種とし
て含有する排水のCOD処理に際して、H2 2 を加え
てpHを低下させる処理を含むことによって、N2 4
およびNaNO2 を分解し、これによりCODを迅速に
低減化することが可能となる。したがって、単一の処理
槽において迅速かつ連続的なCOD低減化処理が可能と
なる。
Thus, in the method according to the present invention, N 2
In COD treatment of wastewater containing a reducing component such as H 4 and NaNO 2 as residual chemical species, N 2 H 4 is added by including treatment for reducing pH by adding H 2 O 2.
And NaNO 2 are decomposed, which makes it possible to rapidly reduce COD. Therefore, COD reduction treatment can be performed quickly and continuously in a single treatment tank.

【0013】[0013]

【実施例】バブリング装置を有する排水槽にて約40μ
g/l濃度のN2 4 水溶液のCOD低減化処理を行な
った。ここで、この被処理液中にはNaNO2 を含む廃
液が残留しておりN2 4 +NaNO2 混合廃液とし
て、図1と同様の方法に従ってCOD処理を実施した。
Example: About 40μ in a drainage tank with a bubbling device
COD reduction treatment was performed on an aqueous N 2 H 4 solution having a concentration of g / l. Here, the waste liquid containing NaNO 2 remained in this liquid to be treated, and COD treatment was carried out as a mixed waste liquid of N 2 H 4 + NaNO 2 according to the same method as in FIG.

【0014】下記表−1に処理前、処理後の水質結果を
示す。表から明らかなように、処理後ではその過程で有
害成分を発生することなく、NaOClの処理では10
μg/l前後までした低減できなかったCODも約6μ
g/l以下となり、処理時間についても300m3 当り
1〜2日間かかっていたものが約6時間の短時間でCO
D低減化処理することが可能となった。
Table 1 below shows water quality results before and after treatment. As is clear from the table, no harmful components were generated in the process after the treatment, and 10
COD that could not be reduced to around μg / l was about 6μ
It was less than g / l, and the processing time was about 1 to 2 days per 300 m 3, but CO was short in about 6 hours.
D reduction processing has become possible.

【0015】[0015]

【表1】 *約750m3 の廃水を約300m3 処理槽を用いて3
日間に分けて処理を行った。
[Table 1] * Approximately 750 m 3 of wastewater is processed in a 300 m 3 treatment tank.
The treatment was divided into days.

【0016】[0016]

【発明の効果】本発明の方法によれば、従来、次亜塩素
酸ナトリウムの添加により長時間かつ繁雑な処理により
COD低減化処理していた廃液、あるいはN2 4 処理
用およびNaNO2 処理用の2槽に分離した繁雑な処理
が必要であった廃液を、迅速かつ簡便に処理することが
可能となる。
EFFECTS OF THE INVENTION According to the method of the present invention, a COD-reducing waste liquid, which has been conventionally treated by adding sodium hypochlorite for a long time and complicated treatment, or N 2 H 4 treatment and NaNO 2 treatment is used. It becomes possible to quickly and simply treat the waste liquid that has been required to be complicatedly treated and separated into two tanks for use.

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

【図1】本発明による排水処理工程の一例を示すフロー
チャート図。
FIG. 1 is a flowchart showing an example of a wastewater treatment process according to the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】還元性の防錆剤のような還元性物質を含有
する高COD(化学的酸素消費量)の産業用排水を処理
するに際し、被処理排水を過酸化水素水によって処理し
被処理排水のpHを低下させる工程を含むことを特徴と
する排水処理方法。
1. When treating industrial wastewater having a high COD (chemical oxygen consumption) containing a reducing substance such as a reducing rust preventive agent, the wastewater to be treated is treated with hydrogen peroxide solution and treated. A wastewater treatment method comprising the step of lowering the pH of the treated wastewater.
【請求項2】前記過酸化水素水による処理後において、
さらにpHを上昇させる処理を含む、請求項1に記載の
方法。
2. After the treatment with the hydrogen peroxide solution,
The method according to claim 1, further comprising a treatment for increasing pH.
JP17526093A 1993-07-15 1993-07-15 Treatment of waste water Pending JPH0724479A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17526093A JPH0724479A (en) 1993-07-15 1993-07-15 Treatment of waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17526093A JPH0724479A (en) 1993-07-15 1993-07-15 Treatment of waste water

Publications (1)

Publication Number Publication Date
JPH0724479A true JPH0724479A (en) 1995-01-27

Family

ID=15993054

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17526093A Pending JPH0724479A (en) 1993-07-15 1993-07-15 Treatment of waste water

Country Status (1)

Country Link
JP (1) JPH0724479A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1152094A (en) * 1997-07-30 1999-02-26 Mitsubishi Heavy Ind Ltd Method for treating drain containing ethanolamine
DE102007036617A1 (en) * 2007-08-02 2009-02-05 Epc Engineering Consulting Gmbh Process for the safe and efficient degradation of hydrazine and hydrazine sulfate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1152094A (en) * 1997-07-30 1999-02-26 Mitsubishi Heavy Ind Ltd Method for treating drain containing ethanolamine
DE102007036617A1 (en) * 2007-08-02 2009-02-05 Epc Engineering Consulting Gmbh Process for the safe and efficient degradation of hydrazine and hydrazine sulfate

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