JPH08252433A - Polluted water treatment device - Google Patents

Polluted water treatment device

Info

Publication number
JPH08252433A
JPH08252433A JP7087333A JP8733395A JPH08252433A JP H08252433 A JPH08252433 A JP H08252433A JP 7087333 A JP7087333 A JP 7087333A JP 8733395 A JP8733395 A JP 8733395A JP H08252433 A JPH08252433 A JP H08252433A
Authority
JP
Japan
Prior art keywords
filter medium
floating filter
solid
water
treatment tank
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
Application number
JP7087333A
Other languages
Japanese (ja)
Inventor
Mitsunori Murakami
光徳 村上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ishigaki Mechanical Industry Co Ltd
Original Assignee
Ishigaki Mechanical Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ishigaki Mechanical Industry Co Ltd filed Critical Ishigaki Mechanical Industry Co Ltd
Priority to JP7087333A priority Critical patent/JPH08252433A/en
Publication of JPH08252433A publication Critical patent/JPH08252433A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE: To efficiently obtain clear water by a combination of a filter device using a floating filter medium and a biological treatment membrane, by mounting the floating filter medium in a treatment tank, and further, a solid-liquid separation membrane in the floating filter medium layer or on the downstream side of a polluted water to be treated. CONSTITUTION: A floating filter medium 2 is mounted in a treatment tank 1, and a solid-liquid separation membrane 3 is provided in the floating filter medium 2 layer or on the downstream side of a polluted water to be treated. In addition, an untreated water feed pipe 4 is opened at the lower part of the treatment tank 1 and the solid-liquid separation membrane 3 of a cylindrical form is suspended from the top of the treatment tank 1 to extract a treated water. Further, air diffusion pipes 6 are arranged respectively in the floating filter medium 2 layer and an untreated water chamber 1a, and at the same time, the opening of a cleaning water pipe 7 for the filter medium is provided to the lateral wall of the treatment tank 1 through the floating filter medium 2 layer. In addition, the opening of a drain pipe 8 for backward washing of the floating filter medium 2 is provided at the bottom of the treatment tank 1. Thus, solid matter is captured and removed during the ascent of the polluted water through the floating filter medium 2 layer. At the same time, organic matter therein is decomposed by microbes in the filter media, and the treated water containing a reduced amount of pollutants is subjected to a separation treatment using the solid-liquid separation membrane.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、下水等の汚水の処理
装置の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of an apparatus for treating wastewater such as sewage.

【0002】[0002]

【従来の技術】浮上ろ材を使用した生物処理装置は公知
であり、また、精密ろ過膜、限外ろ過膜、逆浸透膜など
の固液分離用膜による膜分離装置も公知である。
2. Description of the Related Art A biological treatment apparatus using a floating filter medium is known, and a membrane separation apparatus using a solid-liquid separation membrane such as a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane is also known.

【0003】[0003]

【発明が解決しようとする課題】然しながら、上述の生
物処理装置では、処理水の水質が、従来の生物処理法よ
りも短時間で向上はされるが、未だ十分ではなく、放流
あるいは再利用のために良好な処理水質が要求される場
合には、その後段に別にろ過装置や凝集沈澱装置などを
設けての処理を必要としている。
However, in the above-mentioned biological treatment apparatus, although the quality of treated water is improved in a shorter time than the conventional biological treatment method, it is still not sufficient, and the quality of the discharged or reused water is not improved. Therefore, when a good quality of treated water is required, it is necessary to separately provide a filtration device and a coagulating sedimentation device at the subsequent stage.

【0004】また、上述の生物処理装置においては、浮
上ろ材層中の微生物量を増やして処理能力を高めること
ができるが、微生物量が過剰となると処理水側にリーク
し、これを防止することが困難であった。
Further, in the above-mentioned biological treatment apparatus, although the treatment capacity can be enhanced by increasing the amount of microorganisms in the floating filter medium layer, when the amount of microorganisms becomes excessive, it leaks to the treated water side and must be prevented. Was difficult.

【0005】また、前述の膜分離装置では、溶解性有機
物などの固体でない物質の除去が不充分であり、このた
め、膜分離装置での処理水をさらに処理する必要があっ
た。
Further, in the above-mentioned membrane separation device, the removal of non-solid substances such as soluble organic substances is insufficient, so that it is necessary to further treat the treated water in the membrane separation device.

【0006】また、上述の膜分離装置では、固液分離膜
表面付近の濃度が濃くなったり、固形物の積層などが生
じ、短時間での通水量が低下するので、この対策として
通水方向と直角に高速流を生ぜしめるいわゆるクロスフ
ロー方式などを採用しなければならず、膜分離のための
エネルギーの他に余分なエネルギーを必要としている。
Further, in the above-mentioned membrane separation device, the concentration near the surface of the solid-liquid separation membrane becomes thicker, solids are stacked, etc., and the water flow rate decreases in a short time. A so-called cross-flow method that produces a high-speed flow at a right angle must be adopted, and extra energy is required in addition to the energy for membrane separation.

【0007】[0007]

【課題を解決するための手段】この発明は、上述のよう
な課題を解決し得るものであって、その要旨とするとこ
ろは、処理槽内に浮上ろ材を装入し、その浮上ろ材層中
またはその処理水の流動下位側に固液分離膜を設けると
ともに、処理槽の下部には、原水の供給口を、処理槽の
上部には、処理水の取出口を設けたものである。
SUMMARY OF THE INVENTION The present invention is capable of solving the above-mentioned problems, and the gist of the present invention is to install a floating filter medium in a processing tank and to remove the floating filter medium in the floating filter layer. Alternatively, a solid-liquid separation membrane is provided on the lower flow side of the treated water, a raw water supply port is provided at the lower part of the treatment tank, and a treated water outlet is provided at the upper part of the treatment tank.

【0008】[0008]

【作用】この発明に係る装置は、上述のように構成して
あるので、汚水は浮上ろ材層内を上昇する間に、その夾
雑物(固形物)が捕捉除去されるとともに、ろ材層中の
微生物によって有機物が分解される。そして、この汚水
がろ材層中を通過する際に、固形物が捕捉される結果、
ろ過水中への固形物のリークが抑制される。同時に、ろ
材層中の微生物量を高濃度に維持して運転することが可
能となり、処理能力を向上させることができる。
Since the apparatus according to the present invention is configured as described above, while the wastewater rises in the floating filter medium layer, its contaminants (solid matter) are captured and removed, and the wastewater in the filter medium layer is removed. Organic matter is decomposed by microorganisms. Then, when this sewage passes through the filter medium layer, as a result of capturing solids,
Leakage of solids into filtered water is suppressed. At the same time, it becomes possible to operate while maintaining the amount of microorganisms in the filter medium layer at a high concentration, and the processing capacity can be improved.

【0009】次いで、このようにして汚濁量が減少した
処理水が固液分離膜で、分離処理されることとなり、こ
の二段階に処理された処理水は、固形物および溶解物と
もに除去されており、再利用するために問題のない清浄
水である。
Next, the treated water whose polluted amount is reduced in this way is separated by the solid-liquid separation membrane, and the treated water treated in these two stages is removed from both the solid matter and the dissolved matter. It is clean water that can be reused without problems.

【0010】なお、上述のような処理操作において、浮
上ろ材層中に散気管を設置して曝気を行なうと、ろ材層
中の微生物を活性化して増殖することができるととも
に、固液分離膜の表面の水や浮上ろ材を振動させ、固液
分離膜への固形物の積層や過度の濃度の上昇を防止する
ことができる。すなわち、固液分離膜の汚濁負荷を軽減
することができるとともに、固液分離膜の表面の洗浄効
果もあり、その通水量や通水寿命を改善し、装置能力を
向上せめることができる。以下、図面に基づいて、この
発明を具体的に説明する。
In the above-mentioned processing operation, if a diffusing pipe is installed in the floating filter medium layer for aeration, microorganisms in the filter medium layer can be activated and proliferated, and the solid-liquid separation membrane By vibrating the surface water or the floating filter medium, it is possible to prevent the solids from being stacked on the solid-liquid separation membrane or from excessively increasing the concentration. That is, the pollution load on the solid-liquid separation membrane can be reduced, and the surface of the solid-liquid separation membrane can be cleaned, so that the amount of water flow and the life of water passage can be improved and the device capability can be improved. Hereinafter, the present invention will be specifically described with reference to the drawings.

【0011】[0011]

【実施例】図1は、処理槽1に、浮上ろ材2と固液分離
膜3を装入した事例であり、処理槽1の下部に原水の供
給管4を開口させ、処理槽1の上部から円筒状の固液分
離膜3を垂下して処理水を取出すようにしている。ま
た、浮上ろ材層中および原水室1aに散気管6を設置す
るとともに、処理槽1の側壁に浮上ろ材層中にろ材の洗
浄水管7を開口させている。
EXAMPLE FIG. 1 shows an example in which a flotation filter 2 and a solid-liquid separation membrane 3 are loaded in a treatment tank 1, a raw water supply pipe 4 is opened in the lower portion of the treatment tank 1, and an upper portion of the treatment tank 1 is opened. A cylindrical solid-liquid separation membrane 3 is hung from there to take out the treated water. Further, an air diffuser 6 is installed in the floating filter medium layer and in the raw water chamber 1a, and a washing water pipe 7 for filter medium is opened in the floating filter medium layer on the side wall of the treatment tank 1.

【0012】また、処理槽1の底部には、浮上ろ材2の
逆洗水等の排水管8が開口させてあり、この排水管8は
U字状に立上らせてある。処理槽1の天井壁には、排気
孔を設けて、その排気管9を立上らせて水頭Hの定圧ろ
過ができるようにしてある。尚、図1において符号10
は処理水の取出管、11は、浮上ろ材2係止用のスクリ
ーンである。
A drain pipe 8 for backwashing water of the floating filter medium 2 is opened at the bottom of the treatment tank 1, and the drain pipe 8 is raised in a U-shape. An exhaust hole is provided in the ceiling wall of the processing tank 1, and an exhaust pipe 9 thereof is raised to enable constant pressure filtration of the water head H. In FIG. 1, reference numeral 10
Is a treated water extraction pipe, and 11 is a screen for locking the floating filter material 2.

【0013】上述のように構成した処理装置では、処理
槽1の下部から供給した原水は、浮上ろ材2の層内を上
昇する間に、その夾雑物(固形物)が捕捉されるととも
に、浮上ろ材2に接触し、その表面の微生物によって含
有する有機物が分解される。
In the treatment apparatus constructed as described above, the raw water supplied from the lower portion of the treatment tank 1 is trapped in the impurities (solid matter) while rising in the layer of the floating filter medium 2 and is floated. When the filter medium 2 is contacted with it, microorganisms on the surface decompose organic compounds contained therein.

【0014】そして、処理槽1内をさらに上昇して固液
分離膜3によって微細な固形物までも分離され、清澄な
ろ液を取出管10から取出すことができる。この間、散
気管6から処理槽1内に通気することによって、浮上ろ
材2の表面の微生物を活性化させることができる。そし
て、この通気は排気管9から槽外に排出される。
Then, the inside of the processing tank 1 is further raised, and even the fine solid matter is separated by the solid-liquid separation membrane 3, and the clear filtrate can be taken out from the take-out pipe 10. During this period, the microorganisms on the surface of the floating filter medium 2 can be activated by ventilating the inside of the treatment tank 1 through the air diffuser 6. Then, this ventilation is discharged from the exhaust pipe 9 to the outside of the tank.

【0015】このような運転をして、固液分離膜3から
の通水量(処理水)が減少したときには、逆洗エアー管
5から送気することによって固液分離膜3を洗浄再生す
ることができる。このとき、逆洗エアーは排気管9から
槽外に取出される。このような操作を繰り返すうちに、
浮上ろ材部の目詰りも進行する。
When the amount of water passing through the solid-liquid separation membrane 3 (treated water) is reduced by such an operation, the solid-liquid separation membrane 3 is washed and regenerated by supplying air from the backwash air pipe 5. You can At this time, the backwash air is taken out of the tank through the exhaust pipe 9. While repeating such operations,
The clogging of the floating filter material also progresses.

【0016】この浮上ろ材層の目詰りの進行状態は、槽
内の圧力が上昇することでキャッチできる。(圧力計は
図示省略)圧力上昇をキャッチしたときには、洗浄水管
7より洗浄水を注入することによって、目詰りした浮上
ろ材2を洗浄再生することができる。その洗浄汚水は排
水管8で槽外に取り出せる。このとき、散気管6からの
通気量を多くすると浮上ろ材2の撹拌を助長できて効果
的である。また、排出管をU字状の立上りさせることに
よって浮上ろ材2の流失を防止することができる。
The progress of the clogging of the floating filter material layer can be caught by increasing the pressure in the tank. (The pressure gauge is not shown.) When the rise in pressure is caught, the cleaning water can be injected from the cleaning water pipe 7 to clean and regenerate the clogged floating filter material 2. The cleaning wastewater can be taken out of the tank by the drainage pipe 8. At this time, it is effective to increase the aeration amount from the air diffusing tube 6 because the stirring of the floating filter material 2 can be promoted. Further, by raising the discharge pipe in a U-shape, the floating filter medium 2 can be prevented from flowing away.

【0017】次に、図2に示す事例は、図1に示す事例
と比較して固液分離膜3をろ材層中に埋没し、散気管6
を原液室1aのみに設けた点が異なるのみで、運転操作
およびその作用効果は、図1の事例と同様である。ま
た、図3に示す事例は、図2の事例に比較して開放型の
処理槽1としたものである。
Next, in the case shown in FIG. 2, compared with the case shown in FIG. 1, the solid-liquid separation membrane 3 is buried in the filter medium layer, and the air diffuser 6
The operation is the same as in the case of FIG. 1, except that only the stock solution chamber 1a is provided. Further, the case shown in FIG. 3 is an open type processing tank 1 as compared with the case shown in FIG.

【0018】さらに、図4〜図6に示す事例は、図1〜
図3に示す事例が、水頭Hの加圧ろ過装置としたのに対
して、処理水側からの吸引ろ過を採用している。固液分
離膜3および浮上ろ材2の洗浄再生装置および作用効果
は図1〜図3のものと同様である。
Further, the cases shown in FIGS.
While the case shown in FIG. 3 is a pressure filtration device for the water head H, suction filtration from the treated water side is adopted. The cleaning / reproducing device for the solid-liquid separation membrane 3 and the floating filter medium 2 and the effects thereof are the same as those in FIGS.

【0019】[0019]

【発明の効果】このように、この発明は、処理槽内に生
物処理機能を有する浮上ろ材層と処理原水の流動下位側
に固液分離膜とを設けることによって、浮上ろ材層で原
水中の固形物を捕捉すると同時に物理的に捕捉できない
有機物を分解し、次いで、固液分離膜で微細な固形物ま
で捕捉して清澄な処理水が得られるものであり、従来、
固形物の分離と生物処理とを別々に行なっていたのを一
槽内で処理できるものであり、特に、浮上ろ材層で固形
物が捕捉除去されるので、固液分離膜部の汚濁負荷が低
くなり、長時間の連続ろ過運転が可能で、ろ過効率を格
段に向上させ得るものである。
As described above, according to the present invention, by providing a floating filter medium layer having a biological treatment function in the treatment tank and a solid-liquid separation membrane on the lower flow side of the treated raw water, the floating filter medium layer in the raw water can be treated. At the same time as capturing solids, organic substances that cannot be physically captured are decomposed, and then fine solids are captured by a solid-liquid separation membrane to obtain clear treated water.
The separation of solids and the biological treatment were carried out separately, but it is possible to treat them in one tank. In particular, since the solids are captured and removed by the floating filter material layer, the pollution load of the solid-liquid separation membrane part is reduced. It is low, and continuous filtration operation for a long time is possible, and the filtration efficiency can be significantly improved.

【図面の簡単な説明】[Brief description of drawings]

【図1】この発明に係る汚水の処理装置の模式的縦断面
図である。
FIG. 1 is a schematic vertical sectional view of a sewage treatment apparatus according to the present invention.

【図2】同じく、他の実施例の模式的縦断面図である。FIG. 2 is likewise a schematic vertical sectional view of another embodiment.

【図3】同じく、他の実施例の模式的縦断面図である。FIG. 3 is likewise a schematic vertical cross-sectional view of another embodiment.

【図4】同じく、他の実施例の模式的縦断面図である。FIG. 4 is likewise a schematic vertical cross-sectional view of another embodiment.

【図5】同じく、他の実施例の模式的縦断面図である。FIG. 5 is a schematic vertical sectional view of another embodiment of the present invention.

【図6】同じく、他の実施例の模式的縦断面図である。FIG. 6 is likewise a schematic vertical cross-sectional view of another embodiment.

【符号の説明】[Explanation of symbols]

1 処理槽 2 浮上ろ材 3 固液分離膜 1 Processing tank 2 Floating filter medium 3 Solid-liquid separation membrane

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 3/06 B01D 23/10 Z ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C02F 3/06 B01D 23/10 Z

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 処理槽1内に浮上ろ材2を装入し、その
浮上ろ材層中またはその処理水の流動下位側に固液分離
膜3を設けるとともに、処理槽1の下部には、原水の供
給口を、処理槽1の上部には、処理水の取出口を設けて
なる汚水の処理装置。
1. A flotation filter 2 is loaded into a treatment tank 1, and a solid-liquid separation membrane 3 is provided in the flotation filter layer or on the lower flow side of the treated water. And a treatment water take-out port in the upper part of the treatment tank 1.
JP7087333A 1995-03-20 1995-03-20 Polluted water treatment device Pending JPH08252433A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7087333A JPH08252433A (en) 1995-03-20 1995-03-20 Polluted water treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7087333A JPH08252433A (en) 1995-03-20 1995-03-20 Polluted water treatment device

Publications (1)

Publication Number Publication Date
JPH08252433A true JPH08252433A (en) 1996-10-01

Family

ID=13911954

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7087333A Pending JPH08252433A (en) 1995-03-20 1995-03-20 Polluted water treatment device

Country Status (1)

Country Link
JP (1) JPH08252433A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002292254A (en) * 2001-03-29 2002-10-08 Yuasa Corp Dip type membrane filtration apparatus
JP2002336660A (en) * 2001-05-18 2002-11-26 Yuasa Corp Immersion type membrane filtration equipment and immersion type membrane filtration method
JP2002336854A (en) * 2001-05-18 2002-11-26 Yuasa Corp Immersion type membrane filtration apparatus for septic tank
JP2006101805A (en) * 2004-10-07 2006-04-20 Japan Organo Co Ltd Hollow fiber membrane type bioreactor and liquid treatment method using the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002292254A (en) * 2001-03-29 2002-10-08 Yuasa Corp Dip type membrane filtration apparatus
JP2002336660A (en) * 2001-05-18 2002-11-26 Yuasa Corp Immersion type membrane filtration equipment and immersion type membrane filtration method
JP2002336854A (en) * 2001-05-18 2002-11-26 Yuasa Corp Immersion type membrane filtration apparatus for septic tank
JP2006101805A (en) * 2004-10-07 2006-04-20 Japan Organo Co Ltd Hollow fiber membrane type bioreactor and liquid treatment method using the same

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