JPS60166087A - Treatment of waste water containing high-concentration salts, copper and zinc - Google Patents
Treatment of waste water containing high-concentration salts, copper and zincInfo
- Publication number
- JPS60166087A JPS60166087A JP59022274A JP2227484A JPS60166087A JP S60166087 A JPS60166087 A JP S60166087A JP 59022274 A JP59022274 A JP 59022274A JP 2227484 A JP2227484 A JP 2227484A JP S60166087 A JPS60166087 A JP S60166087A
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- waste water
- wastewater
- copper
- added
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Abstract
Description
【発明の詳細な説明】
本発明は、伸銅製造工場等から排出される酸洗い廃水等
、高濃度の塩類、銅、亜鉛を含有する強酸性廃水の浄化
処理方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying strongly acidic wastewater containing high concentrations of salts, copper, and zinc, such as pickling wastewater discharged from copper rolling mills and the like.
伸銅製造工場等からは、高濃度の塩類、銅、亜鉛を含む
強酸性廃水が排出される。近年、排出規制が厳しくなり
、特に排出先が農業用水である場合、塩類も除去しなけ
ればならないため、廃水を系外に排出しないで、再利用
するクローズドシステムを採ることが多くなってきてい
る。従来、この種の廃水を処理するには、廃水を苛性ソ
ーダで中和し、金属を水酸化物として凝集沈澱させ、こ
れを分離した後、逆浸透圧装置で脱塩処理する方法が採
用されている。しかし、金属含有廃水を中和処理した場
合、フロックの沈降性が悪くなり、処理水質の悪化及び
膜汚染が起こる。この場合、高分子凝集剤を添加して沈
降性を改善する方法があるが、逆浸透圧装置で脱塩処理
する場合に、処理水中に残存、する高分子凝集剤が膜汚
染を起こすので、活性炭処理、オゾン酸化等を併用して
高分子凝集剤を除去しなければならず、操作が複雑にな
るという欠点があった。Strongly acidic wastewater containing highly concentrated salts, copper, and zinc is discharged from copper rolling mills. In recent years, discharge regulations have become stricter, and salts must also be removed, especially when the wastewater is used for agricultural purposes, so closed systems are increasingly being adopted in which the wastewater is reused without being discharged outside the system. . Conventionally, the method used to treat this type of wastewater was to neutralize the wastewater with caustic soda, coagulate and precipitate metals as hydroxides, separate them, and then desalinate them using a reverse osmosis device. There is. However, when metal-containing wastewater is subjected to neutralization treatment, the sedimentation properties of flocs deteriorate, resulting in deterioration of treated water quality and membrane contamination. In this case, there is a method to improve sedimentation by adding a polymer flocculant, but when desalting with a reverse osmosis device, the polymer flocculant remaining in the treated water causes membrane contamination. The polymer flocculant must be removed using activated carbon treatment, ozone oxidation, etc., which has the disadvantage of complicating the operation.
本発明の目的は、前記の従来技術の欠点を解消し、高分
子凝集剤を用いることなく、簡単な操作で凝集性を改善
し、膜汚染を起こさない高濃度塩類、銅、亜鉛含有廃水
の処理方法を提供することにある。この目的は、本発明
によれば亜鉛塩を添加することによって達成される。The purpose of the present invention is to solve the above-mentioned drawbacks of the prior art, to improve the flocculating property with a simple operation without using a polymer flocculant, and to produce wastewater containing high concentration salts, copper, and zinc that does not cause membrane contamination. The purpose is to provide a processing method. This objective is achieved according to the invention by adding zinc salts.
即ち、本発明による廃水の処理方法は、高濃度の塩類、
銅、亜鉛を含む強酸性廃水廃水に亜鉛塩を添加し、攪拌
後、アルカリ剤を添加して廃水をptt9〜11に調整
し、次いで固液分離し、処理水を逆浸透法により脱塩処
理し、生じた亜鉛含有スラッジを回収して原廃水の処理
に再利用することを特徴とする。That is, the method for treating wastewater according to the present invention can treat highly concentrated salts,
Zinc salts are added to strongly acidic wastewater containing copper and zinc, and after stirring, an alkali agent is added to adjust the wastewater to a PTT of 9 to 11, followed by solid-liquid separation, and the treated water is desalted by reverse osmosis. The feature is that the resulting zinc-containing sludge is recovered and reused for the treatment of raw wastewater.
高濃度の塩類、銅、亜鉛を含む強酸性廃水を処理する場
合、アルミニウム系凝集剤や鉄系凝集剤を添加してもフ
ロックを形成し難い。しかし、亜鉛塩を添加すると、良
好にフロックが形成され、凝集沈降性が著しく改善され
ることが判明した。When treating strongly acidic wastewater containing high concentrations of salts, copper, and zinc, it is difficult to form flocs even if aluminum-based flocculants or iron-based flocculants are added. However, it was found that when zinc salt was added, flocs were formed well and flocculation and sedimentation properties were significantly improved.
この沈降性の改善は、恐らく、亜鉛塩の添加によって生
じたフロックが母フロックとして作用し、pit調整後
に生じる金属水酸化物フロックを共沈させるためと思わ
れる。This improvement in sedimentation is probably due to the fact that the flocs produced by the addition of the zinc salt act as a mother floc and coprecipitate the metal hydroxide flocs produced after the pit adjustment.
本発明方法において、亜鉛塩としては、例えば硫酸亜鉛
、塩化亜鉛、硝酸亜鉛等を使用することができる。その
添加量は通常、原水中の亜鉛濃度の0.25倍以上であ
る。In the method of the present invention, as the zinc salt, for example, zinc sulfate, zinc chloride, zinc nitrate, etc. can be used. The amount added is usually 0.25 times or more the zinc concentration in the raw water.
廃水に亜鉛塩を添加し、攪拌後、常用のアルカリ剤、例
えば水酸化ナトリウム等によりpI(を9〜11に調整
すると、廃水中に溶存していた金属はフロックを形成し
、前記の母フロックと共に共沈する。従って、フロック
の凝集、沈降性が良くなり、フロックは容易に固液分離
される。When zinc salt is added to wastewater and stirred, the pI (pI) is adjusted to 9 to 11 with a commonly used alkaline agent such as sodium hydroxide, and the metals dissolved in the wastewater form flocs, and the above-mentioned mother floc Therefore, the flocs have good flocculation and sedimentation properties, and the flocs are easily separated into solid and liquid.
こうして得られた処理液を逆浸透法により脱塩処理する
。The treatment liquid thus obtained is desalted by reverse osmosis.
本発明方法によれば、高分子凝集剤を使用せずに、溶存
金属の凝集、沈降を良好に達成できるので、逆浸透圧装
置における膜汚染を著しく低減することができる。また
、固液分離された回収スラッジを原廃水の処理に再利用
することによって同様に溶存金属の凝集、沈降性を改善
することができるので、亜鉛塩の添加量を節減しながら
、廃水の浄化処理を効果的に行うことができる。According to the method of the present invention, it is possible to successfully achieve flocculation and precipitation of dissolved metals without using a polymer flocculant, so that membrane contamination in a reverse osmosis device can be significantly reduced. In addition, by reusing the collected sludge that has been separated into solid and liquid for the treatment of raw wastewater, it is possible to similarly improve the flocculation and sedimentation of dissolved metals, thereby reducing the amount of zinc salt added and purifying wastewater. Processing can be performed effectively.
次に、実施例に基づいて本発明を詳述するが、本発明は
これに限定されるものではない。Next, the present invention will be described in detail based on Examples, but the present invention is not limited thereto.
実施例 下記の水質の廃水を試料とした。Example The samples were wastewater with the following water quality.
pH1,94
SO41830■/P
= NO3866mg/β
Cu 163IT1g//!
Zn 578mg/β
電導度 7740μS / cm
前記の試料1j2に硫酸亜鉛をZnとして0.3g添加
し、かきまぜ装置で1100rpで5分間攪拌した。次
に、水酸化ナトリウムを添加してpIIIOに調整した
後、5分間攪拌し、40rpmで10分間攪拌し、静置
した。pH1,94 SO41830■/P = NO3866mg/β Cu 163IT1g//! Zn 578 mg/β Electrical conductivity 7740 μS/cm 0.3 g of zinc sulfate as Zn was added to the sample 1j2 and stirred for 5 minutes at 1100 rpm using a stirring device. Next, after adjusting to pIIIO by adding sodium hydroxide, the mixture was stirred for 5 minutes, stirred at 40 rpm for 10 minutes, and left to stand.
静置時間を変動させて、SV、Fl値を測定した。Fl
値は水中のコロイド濃度の指標となるもので、ホローフ
ァイバー・スパイラル型ROに対し、Fl〈3の場合、
トラブルなし、3<l”l<6の場合、徐々にトラブル
が起こり、F I > 6の場合、運転不能と言われて
いる。The SV and Fl values were measured while varying the standing time. Fl
The value is an index of colloid concentration in water, and for hollow fiber spiral RO, in the case of Fl<3,
If there is no trouble, if 3<l"l<6, then trouble will gradually occur, and if F I > 6, it is said to be impossible to operate.
比較のため、従来法として、硫酸亜鉛を添加しない以外
は、同し操作を行い、処理水のSV及びFl値を測定し
た。For comparison, the same operation as the conventional method was performed except that zinc sulfate was not added, and the SV and Fl values of the treated water were measured.
結果を下記の表に示す。The results are shown in the table below.
この表から明らかなとおり、本発明方法によれば、従来
法に比べて、はるかに短時間に沈降分離を行うことがで
きる。As is clear from this table, according to the method of the present invention, sedimentation separation can be performed in a much shorter time than the conventional method.
沈降分離後の処理水を逆浸透圧装置で効率良く脱塩処理
することができ、長期間にわたって膜の汚染は起こらな
かった。The treated water after sedimentation separation could be efficiently desalinated using a reverse osmosis device, and membrane contamination did not occur over a long period of time.
また、分離したスラッジを原廃水の処理に再利用しても
同様に良好な結果が得られた。Similar good results were also obtained when the separated sludge was reused to treat raw wastewater.
特許出願人 日立プラント建設株式会社patent applicant Hitachi Plant Construction Co., Ltd.
Claims (1)
め、廃水に亜鉛塩を添加し、攪拌後、アルカリ剤を添加
して廃水をpH9〜11に調整し、次いで固液分離し、
処理水を逆浸透法により脱塩処理し、生じた亜鉛含有ス
ラッジを回収して原廃水の処理に再利用することを特徴
とする高濃度塩類、銅、亜鉛含有廃水の処理方法。In order to purify strongly acidic wastewater containing high concentrations of salts, copper, and zinc, zinc salts are added to the wastewater, and after stirring, an alkali agent is added to adjust the wastewater to pH 9 to 11, followed by solid-liquid separation.
A method for treating wastewater containing highly concentrated salts, copper, and zinc, characterized in that treated water is desalinated by reverse osmosis, and the resulting zinc-containing sludge is recovered and reused for the treatment of raw wastewater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59022274A JPS60166087A (en) | 1984-02-09 | 1984-02-09 | Treatment of waste water containing high-concentration salts, copper and zinc |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59022274A JPS60166087A (en) | 1984-02-09 | 1984-02-09 | Treatment of waste water containing high-concentration salts, copper and zinc |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60166087A true JPS60166087A (en) | 1985-08-29 |
Family
ID=12078178
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59022274A Pending JPS60166087A (en) | 1984-02-09 | 1984-02-09 | Treatment of waste water containing high-concentration salts, copper and zinc |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60166087A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5300229A (en) * | 1992-02-14 | 1994-04-05 | Japan Exlan Company Limited | Process for removing colored components from solvent for polyacrylonitrile |
JP2000117270A (en) * | 1998-10-09 | 2000-04-25 | Nippon Steel Corp | Treatment of metal-containing waste water and method for recovering valuable metal |
JP2002045871A (en) * | 2000-07-31 | 2002-02-12 | Ngk Spark Plug Co Ltd | Treating method for waste chromate liquid |
-
1984
- 1984-02-09 JP JP59022274A patent/JPS60166087A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5300229A (en) * | 1992-02-14 | 1994-04-05 | Japan Exlan Company Limited | Process for removing colored components from solvent for polyacrylonitrile |
JP2000117270A (en) * | 1998-10-09 | 2000-04-25 | Nippon Steel Corp | Treatment of metal-containing waste water and method for recovering valuable metal |
JP2002045871A (en) * | 2000-07-31 | 2002-02-12 | Ngk Spark Plug Co Ltd | Treating method for waste chromate liquid |
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