JPS6064688A - Electrolytic oxidation treatment of waste water - Google Patents
Electrolytic oxidation treatment of waste waterInfo
- Publication number
- JPS6064688A JPS6064688A JP58170752A JP17075283A JPS6064688A JP S6064688 A JPS6064688 A JP S6064688A JP 58170752 A JP58170752 A JP 58170752A JP 17075283 A JP17075283 A JP 17075283A JP S6064688 A JPS6064688 A JP S6064688A
- Authority
- JP
- Japan
- Prior art keywords
- raw water
- electrolytic
- concn
- oxidation treatment
- toc
- 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
- 230000003647 oxidation Effects 0.000 title claims abstract description 19
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 19
- 239000002351 wastewater Substances 0.000 title claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000000034 method Methods 0.000 claims abstract description 14
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 5
- 239000003792 electrolyte Substances 0.000 claims description 11
- 239000005416 organic matter Substances 0.000 claims description 6
- 239000008151 electrolyte solution Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 3
- 230000006978 adaptation Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000012028 Fenton's reagent Substances 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 239000008139 complexing agent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- MGZTXXNFBIUONY-UHFFFAOYSA-N hydrogen peroxide;iron(2+);sulfuric acid Chemical compound [Fe+2].OO.OS(O)(=O)=O MGZTXXNFBIUONY-UHFFFAOYSA-N 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【発明の詳細な説明】
本発す]は有機物を含有する廃水の電解酸化処理力法に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for electrolytically oxidizing wastewater containing organic matter.
従来より有機物を含有する廃水処理として、燃焼処理、
蒸発鹸縮処理、電解酸化処理、生物処理などの方法が行
なわれているが、燃焼処理した場合には、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り、また蒸
発碌縮処理は熱効率の低下、熱分解による臭気の発生、
凝縮水へのBOD、 COD成分の留出の問題が有り、
いずれにしても設備費、経済性、安全性及び効率の点で
多くの欠点を有している。又、電解酸化処理により直接
有機物を含有する廃水を低δλ度に分解処理するには処
理に長時間を要し、又電解酸化処理の負荷を減らすため
に電解酸化処理の前処理として、酸化剤、例えば過マン
ガン酸塩、次亜塩素酸ソーダー、フェントン試薬によっ
て酸化処理を行うと、沈澱の発生等により処理工程が煩
雑になるなど十分な処理効果が得られていない。Traditionally, combustion treatment,
Methods such as evaporative condensation treatment, electrolytic oxidation treatment, and biological treatment have been used, but when combustion treatment is used, there are problems with the treatment of harmful gases contained in exhaust gas and safety, and evaporative condensation treatment decreases thermal efficiency, generates odor due to thermal decomposition,
There is a problem with distillation of BOD and COD components into condensed water.
In any case, there are many drawbacks in terms of equipment cost, economy, safety and efficiency. In addition, it takes a long time to directly decompose wastewater containing organic matter to a low δλ degree by electrolytic oxidation treatment, and in order to reduce the load on electrolytic oxidation treatment, an oxidizing agent is used as a pretreatment for electrolytic oxidation treatment. For example, when oxidation treatment is performed using permanganate, sodium hypochlorite, or Fenton's reagent, the treatment process becomes complicated due to the generation of precipitates, etc., and a sufficient treatment effect is not obtained.
面、処理コスト、安全性の面を考慮すれば、生物処理、
例えば活性汚泥法が最も有望ではあるが、廃水中に含ま
れる微生物に対し、阻害作用を有する有機物の存在によ
って、生物処理を適用することは困Ia1.場合が多い
。Considering the aspects of treatment cost, safety, biological treatment,
For example, the activated sludge method is the most promising, but it is difficult to apply biological treatment due to the presence of organic substances that have an inhibitory effect on microorganisms contained in wastewater.Ia1. There are many cases.
本発明の目的は上記諸問題を解決した実用性に優れた処
理方法を提供することにある。An object of the present invention is to provide a highly practical treatment method that solves the above-mentioned problems.
本発明は、例えばメッキ工程などで発生する錯化剤等の
微生物に対して限外作用を有する有機物を多量に含有し
た廃水の電解酸化処理において、最初に例えばTOCで
濃度01ppmの廃水の一部を所定の濃度、例えばC,
ppmに希釈し、しかる後、練液を所定の濃度、例えば
Csppmまで電解酸化処理を行ない、次に電解液の一
部を放流し、しかる後、電解液の濃度が電解酸化処理開
始の際の電解液濃1fcC* pPmになるように処理
原水CtPpmの廃水を放流して同量を電解槽に補給し
、再び電解液のGJi[がCmppmになるまで電解酸
化処理を行ない、電解液の初期濃[C! Ppmが終点
濃度Csppmになるように制御しながら処理原水C,
ppmの廃水を一定量づつ電解槽に供給して電解酸化処
理することを特徴とする有機物を含有する廃水の電解酸
化処理方法である。In the electrolytic oxidation treatment of wastewater containing a large amount of organic substances having an ultraviolet effect against microorganisms such as complexing agents generated in the plating process, the present invention first processes a portion of the wastewater with a TOC concentration of 01 ppm. at a predetermined concentration, e.g. C,
After diluting the solution to ppm, the solution is electrolytically oxidized to a predetermined concentration, for example, Csppm, and then a part of the electrolyte is discharged. The treated raw water CtPpm wastewater is discharged so that the electrolyte concentration is 1fcC*pPm, the same amount is replenished into the electrolytic cell, and the electrolytic oxidation treatment is performed again until the electrolyte GJi becomes Cmppm, and the initial concentration of the electrolyte is [C! Treated raw water C while controlling Ppm to reach the end point concentration Csppm,
This is an electrolytic oxidation treatment method for wastewater containing organic matter, characterized in that a fixed amount of ppm wastewater is supplied to an electrolytic cell and subjected to electrolytic oxidation treatment.
以下本発明の実施例を図を用いて詳細に説明する。Embodiments of the present invention will be described in detail below with reference to the drawings.
図は本発明方法を実施する電解酸化処理装置の一例であ
る0図において、処理装置は処理原水の貯留槽1と、該
処理原水を祖給する電解槽5と、電解液の一度を測定す
るTOC計4と、電解液の放流系及び循環系管路と、放
流系、循環系の管路を開閉するバルブ10,9と、TO
C計4よりの指令を受けてバルブ9,10を制御する変
換器3などを備えている。なお、2は処理槽1内の原水
を電解槽5に供給するポンプ、8は循環系放流系に共通
のポンプ、7は電解用電源、6は電解電極である。The figure shows an example of an electrolytic oxidation treatment apparatus for carrying out the method of the present invention. In figure 0, the treatment apparatus has a storage tank 1 for treated raw water, an electrolytic tank 5 that feeds the treated raw water, and a tank for measuring the amount of electrolyte solution. TOC meter 4, electrolyte discharge system and circulation system pipes, valves 10 and 9 for opening and closing the discharge system and circulation system pipes, and TOC meter 4;
It is equipped with a converter 3 and the like that control valves 9 and 10 in response to commands from the C meter 4. In addition, 2 is a pump that supplies the raw water in the treatment tank 1 to the electrolytic tank 5, 8 is a pump common to the circulation system discharge system, 7 is a power source for electrolysis, and 6 is an electrolytic electrode.
まず、第1表に示す廃水の一部を最初に、例えばTOC
濃度で5,000 pprnに希釈し、練液を第2表に
示す電解条件で(解酸化を行ない、図に示したTOC計
4で電解液のTOC濃度を測定する。First, a portion of the wastewater shown in Table 1 is first treated with, for example, TOC.
The solution was diluted to a concentration of 5,000 pprn, the solution was deoxidized under the electrolysis conditions shown in Table 2, and the TOC concentration of the electrolyte was measured using the TOC meter 4 shown in the figure.
〔第1表〕 廃水の水質
〔第2表〕 電解条件
電解液の濃度力i所定の濃度、例えばTOC濃度で1.
500ppm以下になれば、Toe計4空ら゛の信号を
変換器3に入力し、制御指令を発して放流系のバルブl
Oを開け、循環系のバルブ9を閉じ、一定時間ポンプ8
で電解液の一定量Vollを放流する。次に循環系のバ
ルブ9を開け、放流系のノ(ルブ10を閉じ、しかる後
処理原水貯留槽1より処理原水゛の一定量Volを供給
ポンプ2で一定時間電解槽5に供給し、電解液の濃度を
電解開始時の所定のTOC濃度5,000 p pmに
調整する。[Table 1] Water quality of wastewater [Table 2] Electrolytic conditions Electrolyte concentration power i At a predetermined concentration, for example, TOC concentration, 1.
When it becomes 500 ppm or less, a signal indicating that the Toe meter 4 is empty is input to the converter 3, a control command is issued, and the valve l of the discharge system is activated.
0, close the circulation system valve 9, and pump 8 for a certain period of time.
A certain amount of electrolyte Vol. is discharged. Next, the valve 9 of the circulation system is opened, the valve 10 of the discharge system is closed, and a certain amount of treated raw water (Vol) is supplied from the post-treated raw water storage tank 1 to the electrolytic cell 5 for a certain period of time using the supply pump 2, and electrolyzed. The concentration of the solution is adjusted to a predetermined TOC concentration of 5,000 ppm at the start of electrolysis.
以下同様に、処理原水貯留槽1の処理原水を電解液の濃
度変化に従って、一定量づつ′電解槽5に供給して電解
酸化処理するものである。Similarly, the treated raw water in the treated raw water storage tank 1 is supplied in fixed amounts to the electrolytic tank 5 in accordance with changes in the concentration of the electrolytic solution for electrolytic oxidation treatment.
本発明の電解酸化処理方法によれば、有機物を含有する
廃水を低濃度にまで短時間で分解処理でき、処理液は生
物処理の適用が可能で、残存有機l 物を容易に除去す
ることができる。According to the electrolytic oxidation treatment method of the present invention, wastewater containing organic matter can be decomposed to a low concentration in a short time, and the treated liquid can be subjected to biological treatment, so that residual organic matter can be easily removed. can.
尚、実施例の電解酸化処理装置では、濃度測定計として
TOC計を用いたが、TOC計の代りにCOD計を用い
ても効果は変らない。In the electrolytic oxidation treatment apparatus of the example, a TOC meter was used as the concentration meter, but the effect remains the same even if a COD meter is used in place of the TOC meter.
図は本発明の電解酸化処理要領の説明図である。
図中1は処理原水貯留槽、2は処理原水供給ポンプ、3
は変換器、4はTOC計、5は電解槽、8は循環ポンプ
、9はバルブ(循環)、10はバルブ(放流)をそれぞ
れ示す。
特許出願人 日本電気株式会社The figure is an explanatory diagram of the electrolytic oxidation treatment procedure of the present invention. In the figure, 1 is treated raw water storage tank, 2 is treated raw water supply pump, 3
4 is a converter, 4 is a TOC meter, 5 is an electrolytic cell, 8 is a circulation pump, 9 is a valve (circulation), and 10 is a valve (discharge). Patent applicant: NEC Corporation
Claims (1)
で所定の濃度になるまで電解酸化処理を行ない、その電
解液が所定の罰度に達したら電解液の一部を放流し、し
かる後、放流した量と同前の処理原水を原水貯留槽より
電解槽に供給して電解液の濃度な電解開始時の濃度に調
整し、再び電解処理する工程を繰返すことを特徴とする
有機物を含有する廃水の電解酸化処理方法。(1) Part of the treated raw water is diluted to a predetermined concentration and subjected to electrolytic oxidation treatment in an electrolytic solution until the predetermined concentration is reached, and when the electrolyte reaches a predetermined level of punishment, a portion of the electrolyte is discharged. Then, the same amount of treated raw water as the discharged amount is supplied from the raw water storage tank to the electrolytic tank, the concentration of the electrolyte is adjusted to the concentration at the start of electrolysis, and the process of electrolytic treatment is repeated again. A method for electrolytic oxidation treatment of wastewater containing organic matter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58170752A JPS6064688A (en) | 1983-09-16 | 1983-09-16 | Electrolytic oxidation treatment of waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58170752A JPS6064688A (en) | 1983-09-16 | 1983-09-16 | Electrolytic oxidation treatment of waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6064688A true JPS6064688A (en) | 1985-04-13 |
Family
ID=15910728
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58170752A Pending JPS6064688A (en) | 1983-09-16 | 1983-09-16 | Electrolytic oxidation treatment of waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6064688A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007243785A (en) * | 2006-03-10 | 2007-09-20 | Aisin Seiki Co Ltd | Optical coupling controller |
-
1983
- 1983-09-16 JP JP58170752A patent/JPS6064688A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007243785A (en) * | 2006-03-10 | 2007-09-20 | Aisin Seiki Co Ltd | Optical coupling controller |
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