JPS61271090A - Treating device for waste water using immobilized microorganism - Google Patents
Treating device for waste water using immobilized microorganismInfo
- Publication number
- JPS61271090A JPS61271090A JP60111655A JP11165585A JPS61271090A JP S61271090 A JPS61271090 A JP S61271090A JP 60111655 A JP60111655 A JP 60111655A JP 11165585 A JP11165585 A JP 11165585A JP S61271090 A JPS61271090 A JP S61271090A
- Authority
- JP
- Japan
- Prior art keywords
- pellets
- immobilized microorganism
- immobilized
- water
- waste water
- 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.)
- Granted
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)
Abstract
Description
【発明の詳細な説明】
主業上皇且里公!
本発明は、廃水中の有機物質及び無機物質を生物学的に
処理する装置に関し、特に、余剰汚泥の発生量の少ない
廃水処理装置に関する。[Detailed description of the invention] Main job is Retired Emperor and Duke! The present invention relates to a device for biologically treating organic and inorganic substances in wastewater, and particularly to a wastewater treatment device that generates a small amount of excess sludge.
従米豊致血
固定化微生物による廃水の処理方法は、余剰汚泥発生量
が少ないこと及び難分解性有機物の分解が可能である等
の利点を有するため注目されている(角野ら著、「固定
化微生物による下水再利用技術」、日本工業用水協会第
19回研究発表会要旨集、昭和59年3月発行、及び特
願昭58−1526号明細書参照)。The wastewater treatment method using blood-immobilized microorganisms has attracted attention because it has advantages such as generating a small amount of surplus sludge and being able to decompose recalcitrant organic matter (Kadono et al., ``Immobilization Methods''). "Sewage Reuse Technology Using Microorganisms," Collection of Abstracts from the 19th Research Presentation of the Japan Industrial Water Association, published in March 1982, and the specification of Japanese Patent Application No. 1526-1983).
この方法を実施する従来の装置は、固定化微生物ペレッ
トと廃水とを接触させる廃水処理槽及び余剰汚泥を処理
水から分離する固液分離槽から成る。Conventional equipment for carrying out this method consists of a wastewater treatment tank in which the immobilized microbial pellets are brought into contact with the wastewater, and a solid-liquid separation tank in which excess sludge is separated from the treated water.
固液分離には、自然沈降分離や膜分離が用いられている
。Natural sedimentation separation and membrane separation are used for solid-liquid separation.
<7しよ゛と る。占
しかしながら、前記の方法では、余剰汚泥発生量が少な
いながらも、汚泥転換率(除去BOD当たりの汚泥発生
量)が7〜12%であり、余剰汚泥が発生する。また、
この余剰汚泥と処理水とを分離するために、大規模な固
液分離装置で必要である。そこで、更に余剰汚泥発生量
が少なく、固液分離が容易な処理方法及び装置の開発が
望まれる。I'll do <7. However, in the above method, although the amount of surplus sludge generated is small, the sludge conversion rate (the amount of sludge generated per removed BOD) is 7 to 12%, and surplus sludge is generated. Also,
A large-scale solid-liquid separator is required to separate this excess sludge from treated water. Therefore, it is desired to develop a treatment method and device that generates less surplus sludge and facilitates solid-liquid separation.
従って、本発明は、前記の従来技術の欠点を解消し、B
OD除去と同時に濁質を除去することができ、余剰汚泥
発生量が少なく、固液分離が容易であり、しかも処理性
能の高い、廃水の処理装置を提供することを目的とする
。Therefore, the present invention overcomes the drawbacks of the prior art mentioned above and provides B.
It is an object of the present invention to provide a wastewater treatment device that can remove turbidity at the same time as OD removal, generate a small amount of surplus sludge, facilitate solid-liquid separation, and have high treatment performance.
ロ 占 ”るための
本発明は、固定化微生物ペレットとして、真比重が1よ
り小さく、水中で浮上するペレットを用い、水中でこの
ペレットによって形成された2過ゾーンの下方に沈降ゾ
ーンを形成させ、−過ゾーンの下方に被処理水供給管、
上方に処理水排出管を設けることによって前記の問題点
を解決したものである。In the present invention, a pellet having a true specific gravity of less than 1 and floating in water is used as an immobilized microorganism pellet, and a settling zone is formed below a two-layer zone formed by the pellet in water. , - a water supply pipe to be treated below the filtration zone;
The above problem is solved by providing a treated water discharge pipe above.
即ち、本発明による廃水の処理装置は、固定化微生物ペ
レットとして真比重が1より小さくて水中で浮上する固
定化微生物ペレットを充填して含むことを特徴とする。That is, the wastewater treatment apparatus according to the present invention is characterized in that it is filled with immobilized microorganism pellets that have a true specific gravity of less than 1 and float in water.
本発明において固定化する微生物は、細菌、放線菌、カ
ビ、酵母等、任意の微生物を純粋培養若しくは混合培養
したもの、活性汚泥又は土壌に付着した微生物であって
よい。The microorganisms to be immobilized in the present invention may be pure cultures or mixed cultures of any microorganisms such as bacteria, actinomycetes, molds, and yeasts, or microorganisms attached to activated sludge or soil.
本発明において、固定化材としては、ポリウレタン、ポ
リアクリルアミド、アルギン酸カルシウム、カラギーナ
ン、メトキシテトラエチレングリコールメタクリレート
、2,2−ビス〔4−(メタクリロキシポリエトキシ)
−フェニル〕−プロパン、ポリエチレングリコールジア
クリレート、ポリプロピレングリコールジアクリレート
等の固定化材又はこの他の公知の固定化材に炭酸ガス、
窒素ガス等の微細気泡又は発泡スチロールの微細片等を
混入したものを用いることができる。In the present invention, the immobilizing materials include polyurethane, polyacrylamide, calcium alginate, carrageenan, methoxytetraethylene glycol methacrylate, 2,2-bis[4-(methacryloxypolyethoxy)]
-Phenyl]-propane, polyethylene glycol diacrylate, polypropylene glycol diacrylate, or other known immobilization material, carbon dioxide gas,
It is possible to use a material mixed with fine bubbles of nitrogen gas or the like or fine pieces of expanded polystyrene.
本発明に使用する固定化微生物ペレットは、微生物を常
法で前記の固定化材に包括固定することによって製造さ
れ、円柱形又は球形等の形で、球相当径0.5〜10鶴
の範囲内で粒径を選択するのが好ましい。The immobilized microorganism pellet used in the present invention is produced by comprehensively immobilizing microorganisms on the above-mentioned immobilization material using a conventional method, and has a cylindrical or spherical shape, and has an equivalent sphere diameter in the range of 0.5 to 10 mm. It is preferable to select the particle size within the range.
作且
本発明により真比重が1より小さい固定化微生物ペレッ
トを充填しておくと、ペレットは水中で浮遊して処理槽
の上部に集まり、を過ゾーンを形成する。この−過ゾー
ンはSS及びBODを除去する作用をする。r過ゾーン
の下方では、ペレットに付着しないSSや余剰汚泥が沈
降する沈降ゾーンが形成する。即ち、一つの処理槽内で
廃水の生物学的処理と固液分離が同時に行われる。According to the present invention, when the immobilized microorganism pellets having a true specific gravity of less than 1 are filled, the pellets float in the water and collect at the upper part of the treatment tank, forming an overflow zone. This permeable zone acts to remove SS and BOD. Below the filtration zone, a settling zone is formed in which SS and excess sludge that do not adhere to the pellets settle. That is, biological treatment of wastewater and solid-liquid separation are performed simultaneously in one treatment tank.
固定化微生物により廃水の処理において、余剰汚泥の発
生原因としては、(1)固定化微生物のペレットからの
微生物の漏れ、及び(2)浮遊している雑菌の増殖が考
えられる。本発明においては、(1)の原因で発生した
余剰汚泥はf過ゾーンで?過されてペレットに付着し、
付着した汚泥は自己消化する。(2)の原因で発生した
余剰汚泥の一部はt過ゾーンでt過され、一部は沈降ゾ
ーンへ沈降する。従って、余剰汚泥の発生量は少なくな
る。In the treatment of wastewater using immobilized microorganisms, the possible causes of excess sludge are (1) leakage of microorganisms from pellets of immobilized microorganisms, and (2) growth of floating bacteria. In the present invention, excess sludge generated due to (1) is stored in the f-filtration zone. is passed through and adheres to the pellet,
The attached sludge will self-extinguish. A part of the surplus sludge generated due to the cause of (2) is passed through the trough zone, and a part of it settles into the settling zone. Therefore, the amount of surplus sludge generated is reduced.
1藻■ 次に、図面に基づいて本発明を詳述する。1 algae■ Next, the present invention will be explained in detail based on the drawings.
第1図は、本発明の一実施態様を示す廃水の処理装置の
略示断面図である。第1図において、廃水処理槽1の内
部には、真比重が1より小さい固定化微生物ペレットが
充填されており、水が送入されたときに、金網2の下に
固定化微生物ベレント層3が形成される。槽上部には、
処理水排出管4及び洗浄水供給管5を設け、槽下部には
洗浄水排出管6を設けている。また、固定化微生物ペレ
ット層3の下方で、槽の中部には、廃水供給管7を設け
た。FIG. 1 is a schematic cross-sectional view of a wastewater treatment device showing one embodiment of the present invention. In FIG. 1, the inside of a wastewater treatment tank 1 is filled with immobilized microorganism pellets whose true specific gravity is less than 1, and when water is introduced, an immobilized microorganism pellet layer 3 is formed under a wire mesh 2. is formed. At the top of the tank,
A treated water discharge pipe 4 and a wash water supply pipe 5 are provided, and a wash water discharge pipe 6 is provided at the bottom of the tank. Further, below the immobilized microorganism pellet layer 3, a waste water supply pipe 7 was provided in the middle of the tank.
この処理装置を用いて廃水を処理する場合、廃水を廃水
供給管7から廃水処理槽1に供給し、まず、沈降速度の
大きな濁質を沈降ゾーンで沈降除去させてから、浮上し
ている固定化微生物ペレツト層3の濾過ゾーンを上向流
で通過させることにより廃水のBOD成分を除去すると
同時に濁1質が除去され、処理水排出管4を経て装置外
へ排出される。処理工程は、一般には、処理水の濁質濃
度が許容限界に達したら終了し、次に、洗浄工程に入る
。When treating wastewater using this treatment device, the wastewater is supplied from the wastewater supply pipe 7 to the wastewater treatment tank 1, and first, turbid substances with a high sedimentation rate are sedimented and removed in the sedimentation zone, and then the floating solids are removed. By passing the wastewater through the filtration zone of the microorganism pellet layer 3 in an upward flow, the BOD components of the wastewater are removed, and at the same time, turbidity is removed, and the wastewater is discharged through the treated water discharge pipe 4 to the outside of the apparatus. The treatment process generally ends when the turbidity concentration of the treated water reaches an acceptable limit, and then the cleaning process begins.
洗浄工程では、洗浄水を洗浄水供給管5から装置内に導
入し、固定化微生物ペレット層3を振動及び攪拌させて
、捕捉した濁質をペレットから剥離させると同時に下向
流で通過する洗浄水に同伴し、沈降ゾーンに入り、沈降
している濁質と一緒に洗浄水排出管6から装置外へ排出
する。この洗浄方式の特徴は、まず、洗浄水の通水方向
が下向流であり、濁質の沈降方向と同一方向であり、上
向流による洗浄に比べて、洗浄水の使用量が少ない。ま
た、下向流の場合、浮上している固定化微生物ペレット
であるからこそ、効果的に振動及び攪拌される。更に、
沈降ゾーンに沈積した濁質は固定化微生物ペレット層の
洗浄水によって排出されるので、新たな洗浄水は不必要
である。In the cleaning process, cleaning water is introduced into the device from the cleaning water supply pipe 5, and the immobilized microorganism pellet layer 3 is vibrated and stirred to separate the captured suspended solids from the pellets, and at the same time, the cleaning water is passed through in a downward flow. It is entrained in water, enters the settling zone, and is discharged from the washing water discharge pipe 6 together with the settled turbidity to the outside of the apparatus. The feature of this cleaning method is that the washing water flows in a downward flow direction, which is the same direction as the sedimentation direction of suspended matter, and the amount of washing water used is smaller than that in an upward flow washing method. Furthermore, in the case of downward flow, the floating immobilized microorganism pellets are effectively vibrated and stirred. Furthermore,
Since the suspended solids deposited in the settling zone are discharged by the washing water of the immobilized microorganism pellet layer, new washing water is unnecessary.
第2図は廃水処理槽1内に曝気部8を設けた実施態様を
示すもので、曝気部8の上方から廃水を供給し、曝気部
8の下部に送気管9を設置する。FIG. 2 shows an embodiment in which an aeration section 8 is provided in the wastewater treatment tank 1. Wastewater is supplied from above the aeration section 8, and an air supply pipe 9 is installed below the aeration section 8.
この実施態様では、廃水は曝気された後、固定化微生物
ペレット層3で浄化及び−過される。In this embodiment, the wastewater is aerated and then purified and filtered through a layer 3 of immobilized microorganism pellets.
第3図は、曝気部8にも、真比重が1より小さい固定化
微生物ペレットを充填した実施態様であり、第2図に示
した装置より処理効率がよい。FIG. 3 shows an embodiment in which the aeration section 8 is also filled with immobilized microorganism pellets having a true specific gravity of less than 1, and the processing efficiency is better than that of the apparatus shown in FIG. 2.
第4図は、曝気部8の底部に金網を取りつけ、曝気部8
内に真比重が1より大きい固定化微生物ペレット11を
充填した実施態様を示す。この実施態様では、曝気部8
内の固定化微生物ペレット層においても一過が行われる
。Figure 4 shows a wire mesh attached to the bottom of the aeration section 8.
An embodiment is shown in which immobilized microorganism pellets 11 having a true specific gravity of more than 1 are filled in the container. In this embodiment, the aeration section 8
A traverse is also carried out in the immobilized microbial pellet layer within.
実施例1
′ ベレ・ の ゛
に下水処理場の活性汚泥をMLS320000■/lに
濃縮した。この濃縮活性汚泥にポリエチレングリコール
とポリプロピレングリコールを主鎖とし、分子ii40
00〜5000で、両末端にイソシアネート基を有する
ウレタンプレポリマーを8%添加し、重合させ、直径1
.5fiのペレットに成形した。得られたペレットの真
比重は0.98であった。Example 1 Activated sludge from a sewage treatment plant was concentrated to an MLS of 320,000 μ/l in Bere. This concentrated activated sludge has polyethylene glycol and polypropylene glycol as main chains, and molecules ii40
00 to 5000, 8% of urethane prepolymer having isocyanate groups at both ends was added, polymerized, and the diameter was 1.
.. It was molded into 5fi pellets. The true specific gravity of the obtained pellets was 0.98.
癩漣J11皿
得られたペレットを第1図に示した廃水処理槽1に30
%の充填率で充填した。The pellets obtained in 11 plates of Leprosy were placed in the wastewater treatment tank 1 shown in Figure 1 for 30 minutes.
% filling rate.
BOD54〜65■/1.5S23〜35■/lの食品
廃水を滞留時間15分で20日間、連続処理したところ
、BOD8〜12■/1ss3■/1以下の処理水が得
られた。When food wastewater with a BOD of 54-65 .mu./1.5S23-35 .mu./l was continuously treated for 20 days with a residence time of 15 minutes, treated water with a BOD of 8-12 .mu./1ss3.mu./1 or less was obtained.
洗浄水排出管6から排出されるSSを余剰汚泥とし、B
OD処理量から次式により汚泥転換率を算出すると5〜
8%であった。The SS discharged from the wash water discharge pipe 6 is treated as surplus sludge, and B
The sludge conversion rate is calculated from the OD treatment amount using the following formula: 5~
It was 8%.
従来法として、活性汚泥法で処理したところ、汚泥転換
率は40〜53%であった。When the activated sludge method was used as a conventional method, the sludge conversion rate was 40 to 53%.
発凱皇処果
前記のように、本発明の処理装置によれば、余剰汚泥の
発生量が少なく、しかも固液分離が容易で、高い処理性
能が達成される。更に、本発明によれば、一つの処理槽
内で廃水の生物学的処理と固液分離が行われ、別に固液
分離槽を設けなくてすむ。As described above, according to the treatment apparatus of the present invention, the amount of surplus sludge generated is small, solid-liquid separation is easy, and high treatment performance is achieved. Furthermore, according to the present invention, biological treatment and solid-liquid separation of wastewater are performed in one treatment tank, making it unnecessary to provide a separate solid-liquid separation tank.
第1図は、本発明の一実施態様を示す廃水の処理装置の
略示断面図、第2図は、本発明の別の実施態様を示す廃
水の処理装置の略示断面図、第3図は、本発明の別の実
施態様を示す廃水の処理装置の略示断面図、第4図は、
本発明の別の実施態様を示す廃水の処理装置の略示断面
図である。FIG. 1 is a schematic cross-sectional view of a waste water treatment device showing one embodiment of the present invention, FIG. 2 is a schematic cross-sectional view of a waste water treatment device showing another embodiment of the present invention, and FIG. 4 is a schematic sectional view of a wastewater treatment device showing another embodiment of the present invention, and FIG.
FIG. 2 is a schematic cross-sectional view of a wastewater treatment device showing another embodiment of the present invention.
Claims (4)
ペレットを用いた、廃水の処理装置において、固定化微
生物ペレットとして真比重が1より小さくて水中で浮上
する固定化微生物ペレットを充填して含むことを特徴と
する固定化微生物による廃水の処理装置。(1) In a wastewater treatment device using immobilized microorganism pellets in which microorganisms are encased and immobilized in a polymeric substance, the immobilized microorganism pellets are filled with immobilized microorganism pellets that have a true specific gravity of less than 1 and float in water. A wastewater treatment device using immobilized microorganisms, comprising:
成されたろ過ゾーンの下方に、被処理水供給管と洗浄廃
水排出管を設け、ろ過ゾーンの上方に処理水排出管と洗
浄水供給管を設けた特許請求の範囲第1項記載の廃水の
処理装置。(2) A treated water supply pipe and a washing wastewater discharge pipe are provided below the filtration zone formed by the immobilized microbial pellets floating in the water, and a treated water discharge pipe and a washing water supply pipe are provided above the filtration zone. A wastewater treatment device according to claim 1.
給装置を設けた特許請求の範囲第1項又は第2項記載の
廃水の処理装置。(3) The wastewater treatment device according to claim 1 or 2, wherein an aeration section is provided in the device, and an oxygen supply device is provided at a lower part of the aeration section.
求の範囲第1項、第2項又は第3項記載の廃水の処理装
置。(4) The wastewater treatment device according to claim 1, 2 or 3, wherein the aeration section is also filled with immobilized microorganisms.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60111655A JPS61271090A (en) | 1985-05-25 | 1985-05-25 | Treating device for waste water using immobilized microorganism |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60111655A JPS61271090A (en) | 1985-05-25 | 1985-05-25 | Treating device for waste water using immobilized microorganism |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61271090A true JPS61271090A (en) | 1986-12-01 |
JPH0210717B2 JPH0210717B2 (en) | 1990-03-09 |
Family
ID=14566828
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60111655A Granted JPS61271090A (en) | 1985-05-25 | 1985-05-25 | Treating device for waste water using immobilized microorganism |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61271090A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63252591A (en) * | 1987-04-10 | 1988-10-19 | Nkk Corp | Treatment of sewage |
US4931183A (en) * | 1988-06-24 | 1990-06-05 | Klein Hans U | Process and apparatus for the biological purification of water |
US5030353A (en) * | 1989-01-13 | 1991-07-09 | Stuth William L | Secondary sewage treatment system |
JPH0394998U (en) * | 1990-01-12 | 1991-09-27 | ||
JPH03115098U (en) * | 1990-03-02 | 1991-11-27 | ||
US5200081A (en) * | 1989-01-13 | 1993-04-06 | Stuth William L | Secondary sewage treatment system |
US5609754A (en) * | 1995-09-07 | 1997-03-11 | Stuth; William L. | Secondary sewage treatment system |
WO2007077577A3 (en) * | 2006-01-03 | 2008-01-03 | Narendra Ghorpade | A floating ball bio-filter |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5532439A (en) * | 1978-08-28 | 1980-03-07 | Tokyo Shibaura Electric Co | Leaked current detector |
JPS6054790A (en) * | 1983-09-05 | 1985-03-29 | Hitachi Plant Eng & Constr Co Ltd | Water treating apparatus |
-
1985
- 1985-05-25 JP JP60111655A patent/JPS61271090A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5532439A (en) * | 1978-08-28 | 1980-03-07 | Tokyo Shibaura Electric Co | Leaked current detector |
JPS6054790A (en) * | 1983-09-05 | 1985-03-29 | Hitachi Plant Eng & Constr Co Ltd | Water treating apparatus |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63252591A (en) * | 1987-04-10 | 1988-10-19 | Nkk Corp | Treatment of sewage |
US4931183A (en) * | 1988-06-24 | 1990-06-05 | Klein Hans U | Process and apparatus for the biological purification of water |
US5030353A (en) * | 1989-01-13 | 1991-07-09 | Stuth William L | Secondary sewage treatment system |
US5200081A (en) * | 1989-01-13 | 1993-04-06 | Stuth William L | Secondary sewage treatment system |
JPH0394998U (en) * | 1990-01-12 | 1991-09-27 | ||
JPH03115098U (en) * | 1990-03-02 | 1991-11-27 | ||
US5609754A (en) * | 1995-09-07 | 1997-03-11 | Stuth; William L. | Secondary sewage treatment system |
WO2007077577A3 (en) * | 2006-01-03 | 2008-01-03 | Narendra Ghorpade | A floating ball bio-filter |
Also Published As
Publication number | Publication date |
---|---|
JPH0210717B2 (en) | 1990-03-09 |
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