JPH0587320B2 - - Google Patents
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- Publication number
- JPH0587320B2 JPH0587320B2 JP59146624A JP14662484A JPH0587320B2 JP H0587320 B2 JPH0587320 B2 JP H0587320B2 JP 59146624 A JP59146624 A JP 59146624A JP 14662484 A JP14662484 A JP 14662484A JP H0587320 B2 JPH0587320 B2 JP H0587320B2
- Authority
- JP
- Japan
- Prior art keywords
- wastewater
- cod
- treatment
- bod
- discharge
- 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.)
- Expired - Lifetime
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- Water Treatment By Electricity Or Magnetism (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は廃水の処理法、詳しくはパルプ廃液そ
の他各種化学工場例えば石油化学工場や油脂製造
工場等より排出される生物学的処理の難しい
COD成分含有廃水の処理法に関する。[Detailed Description of the Invention] Industrial Application Field The present invention relates to a method for treating wastewater, and more specifically, to wastewater treatment methods that are difficult to biologically treat, such as those discharged from pulp wastewater and other various chemical factories, such as petrochemical factories and oil and fat manufacturing factories.
Concerning methods for treating wastewater containing COD components.
従来の技術
従来この種廃水の処理に於ては、生物学的な処
理のみではCOD成分を除去することができず、
凝集沈殿処理、砂過処理、活性炭処理、オゾン
処理などの三次処理設備を後段に設置することに
より処理基準を満足しているが、これは次の通り
の欠点がある。Conventional technology Conventionally, in the treatment of this type of wastewater, COD components cannot be removed by biological treatment alone.
The treatment standards are satisfied by installing tertiary treatment equipment such as coagulation-sedimentation treatment, sand filter treatment, activated carbon treatment, and ozone treatment at the subsequent stage, but this has the following drawbacks.
(i) 処理過程が多段になり複雑になる。(i) The processing process becomes multi-stage and complicated.
(ii) 広大な敷地が必要となる。(ii) A large area is required.
(iii) 処理コストが高くなる。(iii) Higher processing costs.
発明が解決しようとする問題点
本発明は上記従来の問題を一掃することを目的
としてなされたものである。Problems to be Solved by the Invention The present invention has been made for the purpose of eliminating the above-mentioned conventional problems.
問題点を解決するための手段
本発明者は、上記従来の廃水処理法の問題点を
解消するべく鋭意研究を重ねた結果、前処理とし
てCOD成分含有廃水に水中放電するときは、通
常の生物処理のみで放流可能な処理水質を得るこ
とを見出し、茲に本発明法を完成するに至つたも
のである。Means for Solving the Problems As a result of extensive research in order to solve the problems of the conventional wastewater treatment methods described above, the present inventor found that when discharging COD component-containing wastewater in water as a pretreatment, normal biological organisms It was discovered that treated water quality that can be discharged could be obtained through treatment alone, and this led to the completion of the method of the present invention.
即ち本発明は、COD成分含有廃水を水中放電
により前処理しBOD/COD比を高め生物的に分
解され易い廃水に改善した後、生物的に処理する
ことを特徴とする廃水の処理法に係る。 That is, the present invention relates to a wastewater treatment method characterized by pre-treating COD component-containing wastewater by underwater discharge to improve the BOD/COD ratio and improving it into wastewater that is easily biodegradable, and then biologically treating the wastewater. .
本発明法より処理される廃水としては、パルプ
廃液その他各種化学工場例えば石油化学工場や油
脂製造工場などから排出される廃水を例示でき
る。このような廃水は一般にBOD/COD比が例
えば0.5前後と低く、生物学的に分解されにくい
成分を多量に含んでいる。これを通常の生物学的
処理法、例えば活性汚泥法、回転円板法、散水
床法などで処理するにすぎない場合には、処理水
のCOD成分は殆んど分解されない。又、廃水の
種類により、茶色に着色しているものもある。 Examples of wastewater treated by the method of the present invention include pulp wastewater and wastewater discharged from various chemical factories, such as petrochemical factories and oil and fat manufacturing factories. Such wastewater generally has a low BOD/COD ratio of around 0.5, for example, and contains large amounts of components that are difficult to decompose biologically. If this is simply treated with a normal biological treatment method, such as an activated sludge method, rotating disk method, or sprinkled bed method, the COD components of the treated water will hardly be decomposed. Also, depending on the type of wastewater, some wastewater is colored brown.
本発明は、このような廃水を水中放電により前
処理し、生物的処理に適するよう水質改善するこ
とを特徴としている。前処理として廃水に適用さ
れる放電の条件は、広い範囲から選択できるが、
これがあまりに低いと水質改善あまり寄与でき
ず、またあまりに高いと装置面並びに操作面に於
て好ましくない結果を招く虞れがあるので、廃水
1m3当り、1000KJ〜1000000KJ、好ましくは
10000KJ〜500000KJ程度の放電エネルギーを与
えるような放電条件が採用される。また放電電圧
500V以上が好適である。このような水中放電に
よる廃水の前処理は、第1図に示すように廃水を
生物処理槽1に導く供給ライン2の途中に、電極
3a及び3bを具備する放電装置3を備えた前処
理槽4を設置し、該前処理槽4に於て行なうよう
にしてもよい。また第2図及び第3図で示すよう
に、廃水供給ライン2の途中に直接放電装置3を
備えるときは、前処理槽4の設置を省略できる。
図中5は撹拌機である。 The present invention is characterized in that such wastewater is pretreated by underwater discharge to improve water quality so that it is suitable for biological treatment. The discharge conditions applied to the wastewater as a pretreatment can be selected from a wide range;
If this is too low, it will not contribute much to water quality improvement, and if it is too high, it may lead to unfavorable results in terms of equipment and operation.
Discharge conditions are adopted that provide discharge energy of about 10,000 KJ to 500,000 KJ. Also discharge voltage
500V or more is suitable. Such pretreatment of wastewater by underwater discharge is carried out using a pretreatment tank equipped with a discharge device 3 having electrodes 3a and 3b in the middle of a supply line 2 that leads wastewater to a biological treatment tank 1, as shown in FIG. 4 may be installed and the treatment may be carried out in the pretreatment tank 4. Further, as shown in FIGS. 2 and 3, when a direct discharge device 3 is provided in the middle of the wastewater supply line 2, the installation of the pretreatment tank 4 can be omitted.
In the figure, 5 is a stirrer.
作 用
本発明に於ては、廃水を水中放電により前処理
しているので、廃水中のCOD成分、特に生物学
的に分解不可能な高分子物質が、水中放電により
低分子化されることになる。Effect In the present invention, since wastewater is pretreated by underwater discharge, the COD components in the wastewater, especially biologically undegradable polymer substances, are reduced to low molecular weight by underwater discharge. become.
而して水中放電処理水は、生物処理を示す
BOD値が処理前に比べて高くなるが、これを通
常の生物処理すれば処理水はBOD値のみならず
COD値も低下し、よつて下水及び食品廃水等の
処理し易い廃水の処理水性状を得ることができ、
生物処理だけで放流可能になる。 Therefore, underwater discharge treated water indicates biological treatment.
The BOD value will be higher than before treatment, but if this is treated with normal biological treatment, the treated water will not only have a BOD value.
The COD value also decreases, making it possible to obtain treated water properties for wastewater such as sewage and food wastewater that are easy to treat.
It becomes possible to release water only by biological treatment.
実施例 以下に本発明の実施例を掲げる。Example Examples of the present invention are listed below.
原水としてパルブ廃液(リグニンなどの難分解
性の物質を含む)を用いた。
Parv waste liquid (contains difficult-to-decompose substances such as lignin) was used as raw water.
原水の性状は次の通りであり、BOD/COD比
が0.48と低く、生物学的に分解されにくい成分を
含んでいた。 The properties of the raw water were as follows: the BOD/COD ratio was low at 0.48, and it contained components that were difficult to decompose biologically.
原水の性状
COD 1250g/
BOD 600mg/g
PH 8.0に調整したもの
これをBOD汚泥負荷0.5Kg/BOD/kgss.日の
条件で活性汚泥処理した場合、処理水は茶色に着
色しており、そのCOD成分は殆んど分解されな
かつた。 Raw water properties COD 1250g/BOD 600mg/g PH adjusted to 8.0 When this is treated with activated sludge under the conditions of BOD sludge load 0.5Kg/BOD/kgss.day, the treated water is colored brown and its COD The components were hardly decomposed.
処理水性状
COD(COD除去率32.8%) 840mg/
BOD(BOD除去率87.8%) 73mg/
この廃水を第1図に示すように前処理槽4(容
量1.5、滞溜量1、ステンレス製)に於て、
放電電圧1KV、放電エネルギー1KJ、放電間隔3
秒、放電ギヤツプ3C50mm、供給量12/hrの条
件で、水中放電により前処理したところ、その性
状は、COD1250mg/から1700mg/または
BODが600mg/から3000mg/といずれも高く
なり、またBOD/COD比も0.48から1.76と高くな
り、生物的に分解され易い廃水に改善したことが
確認された。 Treated water properties COD (COD removal rate 32.8%) 840mg/ BOD (BOD removal rate 87.8%) 73mg/ This wastewater is transferred to pretreatment tank 4 (capacity 1.5, retention amount 1, made of stainless steel) as shown in Figure 1. At that,
Discharge voltage 1KV, discharge energy 1KJ, discharge interval 3
When pre-treated by underwater discharge under the conditions of 12 seconds, discharge gap 3C50mm, and supply rate 12/hr, the properties of the COD ranged from 1250mg/ to 1700mg/or
The BOD increased from 600mg/ to 3000mg/, and the BOD/COD ratio also increased from 0.48 to 1.76, confirming that the wastewater was improved to be more easily biodegradable.
この前処理した廃水を生物処理槽1に導き前記
条件と同じBOD汚泥負荷で廃水処理した所直接
に河川海域に放流可能な水質に処理することがで
きた。この処理水の性状は次の通りである。 This pretreated wastewater was led to the biological treatment tank 1 and treated with the same BOD sludge load as the conditions described above, making it possible to treat the water to a quality that could be directly discharged into rivers and sea areas. The properties of this treated water are as follows.
処理水性状
COD(COD除去率98%) 25mg/
BOD(BOD除去率97.7%) 14mg/
色 無色
効 果
本発明処理法によれば、廃水の生物処理に際
し、水中放電にる前処理を施すだけで、処理水を
そのまま放流することができ、活性炭などの三次
処理による後処理は一切不要となり、その分、装
置面並びに操作面の簡潔化を計り得るのみならず
敷地の減少化を計り得られ、全体として処理コス
トを低減し得る特徴がある。 Treated water properties COD (COD removal rate 98%) 25 mg / BOD (BOD removal rate 97.7%) 14 mg / Color Colorless effect According to the treatment method of the present invention, when biologically treating wastewater, pretreatment by submerged discharge is only required. The treated water can be discharged as is, and there is no need for any post-treatment using tertiary treatment such as activated carbon, which not only simplifies the equipment and operations, but also reduces the amount of land required. , which has the feature of reducing processing costs as a whole.
第1図は本発明処理法の一例を示すフローチヤ
ート、第2図は本発明処理法の他の一例を示すフ
ローチヤート、第3図は第2図の放電装置部分の
拡大詳細図である。
図に於て、1は生物処理槽、2は廃水供給ライ
ン、3は放電装置、3a,3bはその電極、4は
前処理槽、5は撹拌機である。
FIG. 1 is a flow chart showing one example of the treatment method of the present invention, FIG. 2 is a flow chart showing another example of the treatment method of the present invention, and FIG. 3 is an enlarged detailed view of the discharge device portion of FIG. 2. In the figure, 1 is a biological treatment tank, 2 is a wastewater supply line, 3 is a discharge device, 3a and 3b are its electrodes, 4 is a pretreatment tank, and 5 is a stirrer.
Claims (1)
しBOD/COD比を高め生物的に分解され易い廃
水に改善した後、生物的に処理することを特徴と
する廃水の処理法。1. A wastewater treatment method characterized by pre-treating COD component-containing wastewater by underwater discharge to increase the BOD/COD ratio and improving it into wastewater that is easily biodegradable, and then biologically treating the wastewater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59146624A JPS6125698A (en) | 1984-07-13 | 1984-07-13 | Treatment of waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59146624A JPS6125698A (en) | 1984-07-13 | 1984-07-13 | Treatment of waste water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6125698A JPS6125698A (en) | 1986-02-04 |
| JPH0587320B2 true JPH0587320B2 (en) | 1993-12-16 |
Family
ID=15411941
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59146624A Granted JPS6125698A (en) | 1984-07-13 | 1984-07-13 | Treatment of waste water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6125698A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006247632A (en) * | 2005-03-10 | 2006-09-21 | Ehime Univ | Liquid processing apparatus and liquid processing method |
| CN104649378B (en) | 2013-11-18 | 2018-12-07 | 松下知识产权经营株式会社 | Liquid handling device and method for treating liquids |
| JP5884065B2 (en) | 2013-11-18 | 2016-03-15 | パナソニックIpマネジメント株式会社 | Liquid processing unit, toilet seat, washing machine and liquid processing apparatus |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS586279A (en) * | 1981-07-04 | 1983-01-13 | Haruno Takenaka | Purifying method for water quality utilizing pumping-up power station |
| JPS586298A (en) * | 1981-07-05 | 1983-01-13 | Haruno Takenaka | Production of clean water utilizing pumping-up power generation |
-
1984
- 1984-07-13 JP JP59146624A patent/JPS6125698A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6125698A (en) | 1986-02-04 |
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