JPS60209299A - Treatment of waste water coexisting metallic ion and organic material - Google Patents
Treatment of waste water coexisting metallic ion and organic materialInfo
- Publication number
- JPS60209299A JPS60209299A JP59065547A JP6554784A JPS60209299A JP S60209299 A JPS60209299 A JP S60209299A JP 59065547 A JP59065547 A JP 59065547A JP 6554784 A JP6554784 A JP 6554784A JP S60209299 A JPS60209299 A JP S60209299A
- Authority
- JP
- Japan
- Prior art keywords
- water
- treatment
- waste water
- transported
- microorganisms
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は金属イオン及び有機物の共存する廃水の処理方
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for treating wastewater in which metal ions and organic substances coexist.
従来より金属イオン及び有機物の共存する廃水の処理力
法として、燃焼処理、蒸発濃縮処理、生物処理などの方
法が行なわれているが、燃焼処理によれば排ガス中に含
まれる有害ガスの処理及び安全性に問題が有シ、また蒸
発濃縮処理は熱効率の低下、熱分解による臭気の発生、
凝縮水へa■。Conventionally, methods such as combustion treatment, evaporation concentration treatment, and biological treatment have been used to treat wastewater in which metal ions and organic substances coexist. There are safety issues, and the evaporative concentration process reduces thermal efficiency, generates odors due to thermal decomposition,
a■ to the condensed water.
COD成分の流出の問題が有シ、いずれにしても設備費
、ランニング費用等の経済性、安全性及び効率の点で多
くの欠点を有していた。There is a problem of outflow of COD components, and in any case, there are many drawbacks in terms of economy such as equipment cost and running cost, safety, and efficiency.
尚、処理コスト、安全性の面から考慮すれば、微生物処
理、例えば、活性汚泥法が最も有望であるが、微生物に
対し阻害作用を有する金属イオン、有機物等が廃水中に
存在する場合は、微生物処理を適用することは困難な場
合が多い。From the viewpoint of treatment cost and safety, microbial treatment, such as the activated sludge method, is the most promising method, but if metal ions, organic substances, etc. that inhibit microorganisms are present in the wastewater, Applying microbial treatments is often difficult.
本発明は上記諸問題を解決し、金属イオン及び有機物を
共存する廃水を処理し、無害化する方法を提供するもの
である。The present invention solves the above-mentioned problems and provides a method for treating wastewater containing metal ions and organic substances and rendering it harmless.
本発明は金属イオン及び有機物を共存する廃水に酸を添
加し、生成する沈殿物を除去する第1工程と、第1工程
で得られる処理水を電気分解を行なう第2工程と第2工
程で得られる処理水を微生物処理する第3工程とを行う
金属イオン及び有機物の共存する廃水の処理方法である
。The present invention consists of a first step of adding an acid to wastewater containing metal ions and organic substances and removing the generated precipitate, and a second step of electrolyzing the treated water obtained in the first step. This is a method for treating wastewater in which metal ions and organic substances coexist, including a third step of microbially treating the resulting treated water.
本発明は、例えば金属イオンを含有するメッキ廃水、例
えば錯化剤、界面活性剤、光沢剤等のように微生物に対
して限外作用を有する有機物を多量に含有する銅メツキ
廃水の処理において、まず廃水に酸を添加して、例えば
坦を3.0以下にして、生成する沈殿物を除去し、次に
、該除去後の液のpHを3.0以下にしだ後電気分解を
行ない、金属イオン銅を陰極に析出除去し、有機物を分
解処理する。さらに該処理水中の残存有機物の濃度を所
望の濃度に希釈調整し、微生物処理するものである。The present invention relates to the treatment of plating wastewater containing metal ions, for example, copper plating wastewater containing a large amount of organic substances that have an ultraviolet effect on microorganisms, such as complexing agents, surfactants, brighteners, etc. First, acid is added to the waste water to remove the generated precipitate by, for example, adjusting the pH to 3.0 or less, and then electrolysis is performed after the pH of the removed liquid is brought to 3.0 or less. Metal ion copper is deposited on the cathode and removed, and organic matter is decomposed. Furthermore, the concentration of residual organic matter in the treated water is diluted and adjusted to a desired concentration, and treated with microorganisms.
尚、電気分解処理は、電気分解処理水中に残存する銅イ
オン、もしくは有機物が微生物の増殖に阻害を与えない
濃度になるように調整を行なうものである。In addition, the electrolytic treatment is adjusted so that the concentration of copper ions or organic substances remaining in the electrolyzed water is such that it does not inhibit the growth of microorganisms.
一般に電気分解処理水のBOD、 、 TOCを測定し
、生分解率(生分解率(働−B0D×100)をめ、T
OCxQ、/C
生分解率が40−以上になるように電気分解処理を行え
ば、該処理水は生物処理の適用が可能と言われている(
井上善介:用水と廃水、 14.N(1,2,lo(1
972)) 。In general, the BOD,
OCxQ, /C It is said that biological treatment can be applied to the treated water if electrolysis treatment is performed so that the biodegradation rate is 40- or higher (
Zensuke Inoue: Water and wastewater, 14. N(1,2,lo(1
972)).
以下第1図に基づいて、本発明の詳細な説明する。第1
図中1はメッキ廃水である。このメッキ廃水1を処理槽
2に輸送し、酸として例えば硫酸3を加え、pHを例え
ば3.0以下に調整する。次に該メッキ廃水の上澄水4
を電気分解槽5に輸送し、電解液のpHを3.0以下と
して、電気分解処理を行なう、ここで前記メッキ廃水1
に含まれる銅イオンは陰極に析出し、廃水中から除去さ
れる。また同時に前記メッキ廃水1に含まれる微生物に
対して限外作用を有する有機物は電気分解処理により、
微生物によって分解され易く、且つ微生物に対する阻害
作用の少ないものへと酸化分解される。The present invention will be described in detail below based on FIG. 1st
1 in the figure is plating wastewater. This plating wastewater 1 is transported to a treatment tank 2, and sulfuric acid 3, for example, is added as an acid to adjust the pH to, for example, 3.0 or less. Next, the supernatant water of the plating wastewater 4
The plating wastewater 1 is transported to an electrolytic tank 5, where the pH of the electrolytic solution is adjusted to 3.0 or lower and subjected to electrolysis treatment.
Copper ions contained in the wastewater are deposited on the cathode and removed from the wastewater. At the same time, organic matter having an ultraviolet effect on microorganisms contained in the plating wastewater 1 is removed by electrolysis treatment.
It is easily decomposed by microorganisms and is oxidized and decomposed into something that has little inhibitory effect on microorganisms.
次に、前記電気分解処理槽5において、電気分解処理さ
れた処理水6は、微生物処理調整槽7に輸送し、必要に
応じて返送放流水15を用いて所望の有機物濃度に希釈
調整し、微生物処理流入水8とする。この微生物処理流
入水8を微生物処理槽9へ輸送し、微生物によって残留
有機物を分解処理する。尚、微生物による廃水の処理方
法として、大別して好気性処理と嫌気性処理との2種類
が有るが本発明においては、重金属イオンの流入の恐れ
があるため、比較的重金属イオンの影響を受けにくい好
気性処理が望ましい。さらに、流入水質の変動に対して
影響を受けにくい接触曝気法を用いることがよシ望まし
い。尚、前記微生物処理槽9では、酸、アルカリ等のp
H調整剤lOの添加によシ、槽内のpHを生物の増殖に
適している6〜8に調整する。又必要に応じてリン酸塩
、硝酸アンモニウム等を含む栄養塩11を添加する。分
解処理された微生物処理流入水8は、微生物処理流出水
12として沈降槽13へ輸送する。沈降槽13では、前
記微生物処理流出水12に含まれる生物等が沈殿し、そ
れらは余剰汚泥16として引抜く。また、上澄水は放流
水14として放流する。尚、前記微生物処理調整槽7に
流入する、前記電気分解処理水6を希釈する場合に、前
記放流水14の一部を返送放流水15として前記微生物
処理調整槽7に輸送し、希釈水として用いることも可能
である。Next, in the electrolysis treatment tank 5, the electrolyzed treated water 6 is transported to the microbial treatment adjustment tank 7, and diluted and adjusted to a desired organic matter concentration using return discharge water 15 as necessary. Microbial treatment inflow water 8. This microbial-treated inflow water 8 is transported to a microbial treatment tank 9, and residual organic matter is decomposed by microorganisms. There are two main types of wastewater treatment methods using microorganisms: aerobic treatment and anaerobic treatment, but in the present invention, there is a risk of heavy metal ions flowing in, so the method is relatively less affected by heavy metal ions. Aerobic treatment is preferred. Furthermore, it is highly desirable to use a contact aeration method that is less susceptible to fluctuations in inflow water quality. In addition, in the microbial treatment tank 9, acid, alkali, etc.
By adding the H regulator IO, the pH in the tank is adjusted to 6 to 8, which is suitable for the growth of organisms. Further, a nutrient salt 11 containing phosphate, ammonium nitrate, etc. is added as necessary. The decomposed microbially treated inflow water 8 is transported to the sedimentation tank 13 as microbially treated effluent 12 . In the sedimentation tank 13, organisms contained in the microbially treated effluent 12 are precipitated, and they are extracted as surplus sludge 16. Further, the supernatant water is discharged as discharge water 14. In addition, when diluting the electrolyzed water 6 flowing into the microbial treatment adjustment tank 7, a part of the discharge water 14 is transported to the microbial treatment adjustment tank 7 as return discharge water 15, and used as dilution water. It is also possible to use
以下に本発明の実施例を示す。Examples of the present invention are shown below.
(実施例)
第1表に示す銅メツキ廃水に硫酸を添加してpHを3.
0以下とし、生成した沈殿物を除去した。次に該処理水
を第2表に示す電解条件で電解処理を行なった。(Example) Sulfuric acid was added to the copper plating wastewater shown in Table 1 to adjust the pH to 3.
0 or less, and the generated precipitate was removed. Next, the treated water was electrolytically treated under the electrolytic conditions shown in Table 2.
〔第1表〕廃水の水質
〔第2表〕電気分解条件
電気分解処理後の処理水の残存銅イオン濃度はlppm
以下、COD濃度は2,501)p声以下であった。[Table 1] Water quality of wastewater [Table 2] Electrolysis conditions Residual copper ion concentration in treated water after electrolysis treatment is lppm
Hereinafter, the COD concentration was below 2,501)p voice.
次に前記電気分解処理水中の残存有機物を接触曝気法に
より処理した。接触曝気法の条件を〔第3表〕に、電気
分解処理水の生分解率、及び微生物処理の結果を〔第4
表〕に示す。尚、本実施例で用いた微生物は、種汚泥と
して生活排水を処理している活性汚泥を用いて馴養した
。Next, residual organic matter in the electrolyzed water was treated by a contact aeration method. The conditions of the contact aeration method are shown in [Table 3], and the biodegradation rate of electrolyzed water and the results of microbial treatment are shown in [Table 4].
Table]. The microorganisms used in this example were acclimatized using activated sludge treated with domestic wastewater as seed sludge.
〔第3表〕接触曝気条件
〔第4表〕生分解率と生物処理の結果
向、本発明の効果を明らかにするために、本発明によら
ないで電解処理した際の生分解率及び生物処理した結果
を併せて〔第4表〕に示した。[Table 3] Contact aeration conditions [Table 4] Biodegradation rate and biological treatment results In order to clarify the effects of the present invention, the biodegradation rate and biological treatment when electrolytically treated without using the present invention were The results of the treatment are also shown in [Table 4].
〔第4表〕に明らかなように、本発明によれば金属イオ
ン及び有機物を共存する廃水を効率よく処理することが
できる。As is clear from Table 4, according to the present invention, wastewater containing metal ions and organic substances can be efficiently treated.
以上のように本発明によれば金属イオン及び有機物の共
存するメッキ廃水中の有価物である金属の回収が可能で
あり、また最終的には微生物処理によって無害化処理を
実現できる効果を有するものである。As described above, according to the present invention, it is possible to recover metals, which are valuable substances, from plating wastewater in which metal ions and organic substances coexist, and finally, it has the effect of realizing detoxification treatment by microbial treatment. It is.
第1図は本発明による処理フロー図である。
図中1はメッキ廃水、2は処理槽、3は硫酸、4は上澄
水、5は電気分解槽、6は電気分解処理水、7は微生物
処理調整槽、8は微生物処理流入水、9は生物処理槽、
lOはpH調整剤、11は栄養塩、12は微生物処理流
出水、13は沈降槽、14は放流水、15は返送放流水
、16は余剰汚泥である。
特許出願人 日本電気株式会社FIG. 1 is a processing flow diagram according to the present invention. In the figure, 1 is plating wastewater, 2 is a treatment tank, 3 is sulfuric acid, 4 is supernatant water, 5 is an electrolysis tank, 6 is electrolyzed water, 7 is a microbial treatment adjustment tank, 8 is microbial treatment inflow water, and 9 is biological treatment tank,
10 is a pH adjuster, 11 is a nutrient salt, 12 is a microbial treatment effluent, 13 is a settling tank, 14 is effluent, 15 is return effluent, and 16 is excess sludge. Patent applicant: NEC Corporation
Claims (1)
方法において、該廃水に酸を添加して、生成する沈殿物
を除去する第1工程と、第1工程で得られる処理水をp
ua 、0以下で電気分解を行なう第2工程と、第2工
程で得られる処理水を微生物処理する第3工程とを行う
ことを特徴とする金属イオン及び有機物の共存する廃水
の処理方法。(1) A method for treating wastewater in which metal ions and organic substances coexist, which includes a first step of adding an acid to the wastewater and removing the generated precipitate, and a method of treating wastewater in which metal ions and organic substances coexist.
A method for treating wastewater in which metal ions and organic substances coexist, characterized by carrying out a second step of performing electrolysis at ua of 0 or less, and a third step of treating the treated water obtained in the second step with microorganisms.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59065547A JPS60209299A (en) | 1984-04-02 | 1984-04-02 | Treatment of waste water coexisting metallic ion and organic material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59065547A JPS60209299A (en) | 1984-04-02 | 1984-04-02 | Treatment of waste water coexisting metallic ion and organic material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60209299A true JPS60209299A (en) | 1985-10-21 |
Family
ID=13290145
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59065547A Pending JPS60209299A (en) | 1984-04-02 | 1984-04-02 | Treatment of waste water coexisting metallic ion and organic material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60209299A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05192662A (en) * | 1991-07-22 | 1993-08-03 | Internatl Business Mach Corp <Ibm> | Electrolytic method and device for reducing amount of organic substance contained in aqueous composition |
KR20010035183A (en) * | 2001-01-12 | 2001-05-07 | 박덕영 | Pathway circulating treatment system for waste water by electrocoagulation and biofilteration |
JP2008049343A (en) * | 2007-11-09 | 2008-03-06 | Nishihara Environment Technology Inc | Organic waste water treatment device |
-
1984
- 1984-04-02 JP JP59065547A patent/JPS60209299A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05192662A (en) * | 1991-07-22 | 1993-08-03 | Internatl Business Mach Corp <Ibm> | Electrolytic method and device for reducing amount of organic substance contained in aqueous composition |
KR20010035183A (en) * | 2001-01-12 | 2001-05-07 | 박덕영 | Pathway circulating treatment system for waste water by electrocoagulation and biofilteration |
JP2008049343A (en) * | 2007-11-09 | 2008-03-06 | Nishihara Environment Technology Inc | Organic waste water treatment device |
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