JPH06170386A - Treatment of waste water utilizing excessive sludge of treated water supply equipment line - Google Patents
Treatment of waste water utilizing excessive sludge of treated water supply equipment lineInfo
- Publication number
- JPH06170386A JPH06170386A JP4345511A JP34551192A JPH06170386A JP H06170386 A JPH06170386 A JP H06170386A JP 4345511 A JP4345511 A JP 4345511A JP 34551192 A JP34551192 A JP 34551192A JP H06170386 A JPH06170386 A JP H06170386A
- Authority
- JP
- Japan
- Prior art keywords
- water
- treatment
- tank
- wastewater
- biological treatment
- 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
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Activated Sludge Processes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、中水道設備ラインの余
剰汚泥を利用した廃水処理方法、特に風呂、洗面、厨房
などで使用された、いわゆる厨房廃水を処理するに適し
た廃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 a wastewater treatment method using surplus sludge in a water supply facility line, and more particularly to a wastewater treatment method suitable for treating so-called kitchen wastewater used in baths, washbasins, kitchens and the like. It is a thing.
【0002】[0002]
【従来の技術】一定面積以上の厨房から排出される厨房
廃水については、公共下水道へ流せる廃水水質に法律に
よる規制があり、例えば生物化学的酸素要求量(BO
D)600ppm 以下、浮遊物質量(SS)600ppm以下、油
分(ノルマルヘキサン抽出分) は30ppm 以下の排除基準
が設けられている。排除基準を越える場合には除害措置
を講じなけばならない。ホテル、デパ−ト、一般ビル、
各種会館などでは、厨房廃水について上記規制物質を除
去するために、通常、微細目スクリーンにより廃水中の
夾雑物を除去した後、加圧浮上法、生物処理法などによ
る廃水処理が行われている。2. Description of the Related Art Regarding kitchen wastewater discharged from kitchens with a certain area or more, there are legal restrictions on the quality of wastewater that can be discharged into public sewers, for example, biochemical oxygen demand (BO).
D) Exclusion criteria are set to 600ppm or less, suspended solids (SS) 600ppm or less, and oil (normal hexane extract) 30ppm or less. If the exclusion criteria are exceeded, detrimental measures must be taken. Hotel, department, general building,
In various halls, in order to remove the above-mentioned restricted substances in kitchen wastewater, normally, after removing impurities in the wastewater with a fine screen, the wastewater treatment is carried out by the pressure flotation method, biological treatment method, etc. .
【0003】加圧浮上法は、加圧水中に溶解している空
気を、水圧を下げることにより気泡として発生させ、こ
れに油分を付着させて油分を浮上分離するもので、最も
一般に使用されている除害方法であるが、この方法によ
ると、廃水の変動により処理水質が変動するとともに、
発生するスラッジの処理、臭気対策および廃棄に多大の
費用がかかるという問題点がある。生物処理法は、例え
ば廃水を細菌、カビ、酵母、藻類などの純粋培養あるい
は混合培養した微生物、または下水、産業廃水などの活
性汚泥の微生物と接触させ、廃水をばっ気して有害物質
を酸化、分解させることを基本とするもので、接触酸化
法や回転円板法が実施されている。油分、BOD成分の
除去に有効で、かつスラッジの発生がなく運転が容易で
あり、しかも運転コストが安いため、加圧浮上法に比べ
より有力な廃水処理手段である。特に、微生物をろ材に
固着して行う微生物処理は、活性汚泥を使用する方法
(活性汚泥法)よりSSの発生量も少なく、SS600ppm
以下の規制を確実に達成することが可能な処理方法であ
る。The pressure flotation method is a method in which air dissolved in pressurized water is generated as bubbles by lowering the water pressure, and oil is attached to the air to float and separate the oil, and is most commonly used. This is an abatement method. According to this method, the treated water quality changes due to changes in wastewater,
There is a problem that treatment of sludge generated, odor control, and disposal are very expensive. The biological treatment method includes, for example, contacting wastewater with a pure or mixed culture of bacteria, mold, yeast, algae, etc., or microorganisms of activated sludge such as sewage, industrial wastewater, etc., and aeration of the wastewater to oxidize harmful substances. However, it is basically decomposed, and the catalytic oxidation method and the rotating disk method are used. It is a more effective wastewater treatment means than the pressure flotation method because it is effective in removing oil and BOD components, is easy to operate with no generation of sludge, and has a low operating cost. In particular, microbial treatment performed by fixing microorganisms to the filter medium produces less SS than the method using activated sludge (activated sludge method), and SS600ppm
It is a processing method that can reliably achieve the following regulations.
【0004】一方、大都市における水の使用量の増加に
よる水の供給能力の問題から、特にデパート、ホテル、
各種会館など、上水道の使用が多いところでは、風呂、
洗面、厨房などで使用された厨房廃水を処理して中水と
し水洗便所用水などの各種雑用水として再利用すること
も実施されており、発明者らも、廃水を活性汚泥法によ
り処理し、処理水を限外濾過することを基本工程とする
中水道設備について検討を行ってきた。デパート、ホテ
ル、各種会館などに中水道設備ラインを設置することは
経済的効果が大きく、水資源節約の観点からもメリット
があるが、この場合、余剰汚泥の発生が避けられず、余
剰汚泥を固液分離して産業廃棄物として投棄しなければ
ならないという問題点がある。また、デパート、ホテ
ル、各種会館などでは、厨房廃水量が中水道を利用でき
る水洗便所用水その他の雑用水の水量を大幅に上回るた
め、厨房廃水を中水道設備ラインの原水として使用し中
水とする場合、余剰の厨房廃水を公共下水道へ放流する
必要があるため、そのための廃水処理ラインを別に設置
せざるを得ない。On the other hand, due to the problem of water supply capacity due to the increase in water usage in large cities, department stores, hotels,
In areas such as various halls where water supply is often used, baths,
It is also practiced to treat kitchen wastewater used in washrooms, kitchens, etc. and recycle it as intermediate water for various miscellaneous water such as flush toilet water.The inventors also treat wastewater by the activated sludge method, We have been studying the water supply system that has the basic process of ultrafiltration of treated water. Installing a sewerage system line in department stores, hotels, various halls, etc. has a great economic effect and is advantageous from the viewpoint of saving water resources, but in this case, generation of excess sludge is unavoidable and excess sludge is There is a problem in that solid-liquid separation must be performed and then discarded as industrial waste. Also, in department stores, hotels, various halls, etc., since the amount of kitchen wastewater greatly exceeds the amount of water for flush toilets and other miscellaneous water that can use the tap water, the kitchen wastewater is used as raw water for the tap water facility line. In that case, it is necessary to discharge the excess kitchen wastewater to the public sewers, and there is no choice but to install a separate wastewater treatment line for that purpose.
【0005】[0005]
【発明が解決しようとする課題】本発明は、微生物処理
によるBOD,SS,油分廃水処理ラインと廃水を活性
汚泥を含む生物反応槽で処理する中水道設備ラインとを
併設した場合、BOD,SS,油分廃水処理ラインの処
理効率を向上させるとともに、中水道設備ラインにおい
て発生する余剰汚泥を有効利用する方策について検討し
ていく過程において、余剰汚泥がBOD,SS,油分廃
水処理ラインの生物処理槽の運転性能を大きく改善する
ことを見出したことに基づいてなされたものであり、そ
の目的は、中水道設備ラインで生じる余剰汚泥を活用し
て、BOD,SS,油分廃水処理ラインの微生物処理に
よる油分、BOD成分の分解効率をさらに高めた中水道
設備ラインの余剰汚泥を利用した廃水処理方法を提供す
ることにある。SUMMARY OF THE INVENTION According to the present invention, when a BOD, SS, oil wastewater treatment line by microbial treatment and a wastewater treatment facility line for treating wastewater in a biological reaction tank containing activated sludge are installed together, BOD, SS , In the process of improving the treatment efficiency of the oil wastewater treatment line and examining the measures to effectively utilize the excess sludge generated in the water supply facility line, the excess sludge is BOD, SS, the biological treatment tank of the oil wastewater treatment line It was made based on the finding that the operating performance of the system was greatly improved, and the purpose was to utilize the excess sludge generated in the sewer system line, and to perform the microbial treatment of the BOD, SS and oil wastewater treatment lines. An object of the present invention is to provide a wastewater treatment method using surplus sludge in a water supply facility line, which further improves the decomposition efficiency of oil and BOD components.
【0006】[0006]
【課題を解決するための手段】上記の目的を達成するた
めの本発明の中水道設備ラインの余剰汚泥を利用した廃
水処理方法は、廃水を活性汚泥を含む生物反応槽により
処理して中水道とする中水道設備ラインから排出される
余剰汚泥を、別のBOD,SS,油分廃水処理ラインの
生物処理槽および/または該生物処理槽での微生物処理
の前工程に加えることにより、廃水中の油分、BOD成
分を効率的に分解することを構成上の基本的特徴とし、
生物処理槽での微生物処理が接触酸化法または回転円板
法により行われること、および生物処理槽への廃水が厨
房廃水であり、生物処理槽での微生物処理が下水道放流
前の中間処理であることを発明構成上の第2、第3の特
徴とする。[Means for Solving the Problems] A method for treating wastewater using surplus sludge in a water supply facility line of the present invention for achieving the above object is a method for treating wastewater by a biological reaction tank containing activated sludge. By adding the excess sludge discharged from the water treatment facility line to a biological treatment tank of another BOD, SS, oil wastewater treatment line and / or a pretreatment step of microbial treatment in the biological treatment tank, Efficiently decomposing oil and BOD components is the basic characteristic of the structure,
The microbial treatment in the biological treatment tank is carried out by the catalytic oxidation method or the rotating disk method, and the wastewater to the biological treatment tank is the kitchen wastewater, and the microbial treatment in the biological treatment tank is the intermediate treatment before the sewer discharge. These are the second and third characteristics of the invention structure.
【0007】厨房廃水を下水道へ放流するにあたり、前
記のようにBOD,SSおよび油分を排除基準以下にす
るために廃水処理ラインを設置し、生物処理槽での微生
物処理を中心とする除害のための中間処理を行うが、本
発明は、併設される中水道設備ラインの限外濾過膜から
の排除水、すなわち余剰汚泥を含む濃縮水を、BOD,
SS,油分廃水処理ラインの生物処理槽に加えて中間処
理水の油分、BOD成分の除害効果を高め、排除基準を
確実に下回るようにするものである。When the kitchen wastewater is discharged to the sewer, a wastewater treatment line is installed to keep the BOD, SS and oil content below the exclusion standard as described above, and the microbial treatment in the biological treatment tank is mainly used for the removal of harmful substances. In the present invention, an intermediate treatment is carried out for removing the water removed from the ultrafiltration membrane of the attached water supply facility line, that is, the concentrated water containing the excess sludge by BOD,
In addition to the biological treatment tanks of the SS and oil wastewater treatment lines, the effect of removing oil and BOD components in the intermediate treated water is enhanced to ensure that the exclusion standard is met.
【0008】[0008]
【作用】本発明の中水道設備ラインの余剰汚泥を利用し
た廃水処理方法は、上記の構成および機能を有するか
ら、中水道設備ラインから排出される余剰汚泥をBO
D,SS,油分廃水処理ラインの生物処理槽中に加える
ことにより、生物処理槽での油分、BOD成分の捕捉、
分解が、余剰汚泥を添加しない場合に比較して著しく促
進される。Since the wastewater treatment method using the excess sludge in the water supply system line of the present invention has the above-mentioned constitution and function, the excess sludge discharged from the water supply facility line is BO.
D, SS, by adding to the biological treatment tank of the oil wastewater treatment line, capture of oil and BOD components in the biological treatment tank,
Decomposition is significantly accelerated compared to the case where excess sludge is not added.
【0009】[0009]
【実施例】以下、本発明の実施例について説明する。 実施例1 図1に示すように、厨房廃水を処理する廃水処理ライン
の生物処理槽1に、原水6として、BOD成分110 〜20
0ppm、SS成分90〜150ppm、油分45〜80ppm を含有する
pH6.5 〜8.6 の水を150 l/hrの流入量で導入し、ばっ
気空気量7.2 m3/hr 、槽内滞留時間6hr の条件で微生物
処理を行った。この場合、併設された中水道設備ライン
の活性汚泥を含む生物反応槽2により処理した処理水5
を限外濾過膜(UF膜)3で濾過し、濃縮した濃縮水(M
LSS 5000ppm)4の一部を、6 l/hrの割合で廃水処理ライ
ンの生物処理槽1へ加える。7、8はそれぞれ各ライン
に設置された油水分離槽および調整槽である。生物処理
槽1に余剰汚泥を含む濃縮水4を添加して微生物処理を
行った場合と、濃縮水を添加することなしに微生物処理
を行った場合における中間処理水中のBOD、SSおよ
び油分の分析値を表1に示す。EXAMPLES Examples of the present invention will be described below. Example 1 As shown in FIG. 1, BOD components 110 to 20 were used as raw water 6 in a biological treatment tank 1 of a wastewater treatment line for treating kitchen wastewater.
Water of pH 6.5 to 8.6 containing 0 ppm, SS component 90 to 150 ppm, oil content 45 to 80 ppm was introduced at an inflow rate of 150 l / hr, and the amount of aeration air was 7.2 m 3 / hr and the residence time in the tank was 6 hr. Microbial treatment was performed under the conditions. In this case, treated water 5 treated by the biological reaction tank 2 containing activated sludge in the attached water supply facility line
Filtered through an ultrafiltration membrane (UF membrane) 3 and concentrated water (M
Part of LSS 5000ppm) 4 is added to biological treatment tank 1 of the wastewater treatment line at a rate of 6 l / hr. Reference numerals 7 and 8 are an oil / water separation tank and an adjustment tank installed in each line. Analysis of BOD, SS and oil content in the intermediate treated water when the concentrated water 4 containing excess sludge is added to the biological treatment tank 1 to perform the microbial treatment and when the microbial treatment is performed without adding the concentrated water The values are shown in Table 1.
【0010】表1から明らかなように、廃水処理ライン
の生物反応槽に中水道設備ラインの余剰汚泥を含む濃縮
水を加えた場合は、油分およびBOD成分の除去効率が
大幅に向上しているのが認められる。SSは上昇する
が、放流基準値を大幅に下回っている。As is clear from Table 1, when the concentrated water containing the excess sludge in the water supply facility line is added to the biological reaction tank of the wastewater treatment line, the efficiency of removing oil and BOD components is greatly improved. Is recognized. SS increases, but is well below the discharge standard.
【0011】[0011]
【表1】 [Table 1]
【0012】[0012]
【発明の効果】以上のとおり、本発明により提供される
中水道設備ラインの余剰汚泥を利用した廃水処理方法に
よれば、油分、BOD成分の分解効果が高められ、排出
基準を確実に下回る規制物質の除害を行うことができ、
中水道設備ラインから排出される余剰汚泥も全量処理す
ることができる。As described above, according to the wastewater treatment method using the excess sludge in the water supply facility line provided by the present invention, the effect of decomposing oil and BOD components is enhanced, and the regulation is surely lower than the emission standard. Can remove substances,
Excess sludge discharged from the sewer system line can be completely treated.
【図1】本発明の廃水処理方法に使用される装置構成の
要部の実施例を示す説明図である。FIG. 1 is an explanatory diagram showing an example of a main part of an apparatus configuration used in a wastewater treatment method of the present invention.
1 生物処理槽 2 生物反応槽 3 限外濾過膜 4 濃縮水 5 処理水 6 原水 7 油水分離槽 8 調整槽 1 Biological treatment tank 2 Biological reaction tank 3 Ultrafiltration membrane 4 Concentrated water 5 Treated water 6 Raw water 7 Oil-water separation tank 8 Adjustment tank
───────────────────────────────────────────────────── フロントページの続き (72)発明者 戸田 正志 千葉県市原市姉崎海岸131番地 住友ケミ カルエンジニアリング株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Masashi Toda 131 Izumizaki, Ichihara, Chiba Sumitomo Chemical Engineering Co., Ltd.
Claims (3)
処理して中水道とする中水道設備ラインから排出される
余剰汚泥を、別の廃水処理ラインの生物処理槽および/
または該生物処理槽での微生物処理の前工程に加えるこ
とにより、廃水中の油分、BOD成分を効率的に分解す
ることを特徴とする中水道設備ラインの余剰汚泥を利用
した廃水処理方法。1. Excess sludge discharged from a water supply facility line for treating wastewater by a bioreaction tank containing activated sludge to form a tap water, and a biological treatment tank of another waste water treatment line and / or
Alternatively, a wastewater treatment method using surplus sludge in a water supply facility line, which is characterized by efficiently decomposing oil components and BOD components in wastewater by adding it to a preceding step of microbial treatment in the biological treatment tank.
または回転円板法により行われることを特徴とする請求
項1記載の中水道設備ラインの余剰汚泥を利用した廃水
処理方法。2. A method for treating wastewater using surplus sludge in a water supply facility line according to claim 1, wherein the treatment of microorganisms in the biological treatment tank is performed by a catalytic oxidation method or a rotating disk method.
生物処理槽での微生物処理が下水道放流前の中間処理で
あることを特徴とする請求項1または請求項2記載の中
水道設備ラインの余剰汚泥を利用した廃水処理方法。3. The wastewater to the biological treatment tank is kitchen wastewater,
The method for treating wastewater using surplus sludge in a water supply facility line according to claim 1 or 2, wherein the microbial treatment in the biological treatment tank is an intermediate treatment before the discharge of the sewer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4345511A JPH06170386A (en) | 1992-12-01 | 1992-12-01 | Treatment of waste water utilizing excessive sludge of treated water supply equipment line |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4345511A JPH06170386A (en) | 1992-12-01 | 1992-12-01 | Treatment of waste water utilizing excessive sludge of treated water supply equipment line |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06170386A true JPH06170386A (en) | 1994-06-21 |
Family
ID=18377078
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4345511A Pending JPH06170386A (en) | 1992-12-01 | 1992-12-01 | Treatment of waste water utilizing excessive sludge of treated water supply equipment line |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06170386A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008142632A (en) * | 2006-12-11 | 2008-06-26 | Unitika Ltd | Method for treating waste water biologically |
KR101238475B1 (en) * | 2011-01-07 | 2013-03-04 | (주) 부경이엔지 | Nonpoint source removal treatment system combined with advanced wastewater treatment process |
CN107352747A (en) * | 2017-08-11 | 2017-11-17 | 四川奥恒环保科技有限公司 | Catering sewage treatment device |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5648293A (en) * | 1979-09-26 | 1981-05-01 | Nissin Electric Co Ltd | Treatment of organic waste water |
JPS57165094A (en) * | 1981-04-06 | 1982-10-09 | Mitsui Eng & Shipbuild Co Ltd | Purification of oil-contng. waste water |
-
1992
- 1992-12-01 JP JP4345511A patent/JPH06170386A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5648293A (en) * | 1979-09-26 | 1981-05-01 | Nissin Electric Co Ltd | Treatment of organic waste water |
JPS57165094A (en) * | 1981-04-06 | 1982-10-09 | Mitsui Eng & Shipbuild Co Ltd | Purification of oil-contng. waste water |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008142632A (en) * | 2006-12-11 | 2008-06-26 | Unitika Ltd | Method for treating waste water biologically |
KR101238475B1 (en) * | 2011-01-07 | 2013-03-04 | (주) 부경이엔지 | Nonpoint source removal treatment system combined with advanced wastewater treatment process |
CN107352747A (en) * | 2017-08-11 | 2017-11-17 | 四川奥恒环保科技有限公司 | Catering sewage treatment device |
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