JPH01171693A - Biomembrane filtration apparatus - Google Patents
Biomembrane filtration apparatusInfo
- Publication number
- JPH01171693A JPH01171693A JP62330981A JP33098187A JPH01171693A JP H01171693 A JPH01171693 A JP H01171693A JP 62330981 A JP62330981 A JP 62330981A JP 33098187 A JP33098187 A JP 33098187A JP H01171693 A JPH01171693 A JP H01171693A
- Authority
- JP
- Japan
- Prior art keywords
- filter medium
- flow path
- tank
- fluidized bed
- 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.)
- Pending
Links
- 238000001914 filtration Methods 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000000926 separation method Methods 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 6
- 230000005484 gravity Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 230000008021 deposition Effects 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 238000000605 extraction Methods 0.000 description 11
- 238000011001 backwashing Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000002265 prevention Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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】 〔産業上の利用分野〕 本発明は生物膜濾過装置に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a biofilm filtration device.
水道水用の原水等の前処理装置として所謂生物膜濾過装
置が用いられている。第3図はその一例を示すもので、
タンク15の中間部に粒状の濾材が充填された濾過層1
6(固定床)を有し、この濾過Rg16によりSS分(
懸濁固形分)の濾過を行うとともに、上記濾材に生物膜
を形成させ、この生物膜により原水を生物学的に浄化す
るようにしたもので、タンク上部から供給された原水を
下向流として濾過層を通過させることにより、生物学的
浄化とび過を行い、通過した処理水を抜出管17から抜
出すようにしている。A so-called biofilm filtration device is used as a pretreatment device for raw water for tap water. Figure 3 shows an example.
A filter layer 1 filled with granular filter media in the middle part of the tank 15
6 (fixed bed), and by this filtration Rg16, SS (
In addition to filtering suspended solids), a biofilm is formed on the filter medium, and the biofilm biologically purifies the raw water. Biological purification is performed by passing through the filter layer, and the treated water that has passed is extracted from the extraction pipe 17.
しかし、このような従来の装置では、一定期間運転する
と、濾材に捕捉されたSS分等により濾過抵抗が増加し
、このため定期的に逆洗処理(逆洗配管18がら空気及
び逆洗水を供給する処理)を行う必要があるが、この逆
洗処理のためには原水の供給、すなわち運転を停止する
必要がある。However, in such conventional devices, when operated for a certain period of time, the filtration resistance increases due to the SS trapped in the filter medium, and therefore, backwashing processing (air and backwash water from the backwash piping 18) is periodically performed. However, for this backwashing process, it is necessary to stop the supply of raw water, that is, to stop the operation.
また、上記逆洗処理においては、SS分を濾材から剥離
するために行われる空洗(空気の供給)時に濾材が上方
に噴き上げられ、トラフ19等から槽外に流出してしま
うという難点がある。In addition, in the above-mentioned backwashing process, there is a drawback that the filter material is blown upward during air washing (air supply) performed to separate the SS from the filter material, and flows out of the tank from the trough 19 etc. .
また、このような濾材流出を防止するため濾材流出防止
ネットを設けた場合、ネットに目詰りを生じてしまう難
点がある。Further, when a filter medium outflow prevention net is provided to prevent such a filter medium outflow, there is a problem that the net becomes clogged.
本発明は、このような従来の問題に鑑みなされたもので
、濾材洗浄のために運転を停止させる必要がなく、また
濾材の槽外への流出や濾材流出防止ネットの目詰り等の
問題を生じることもなく、しかも従来の装置に較べ、特
に生物学的浄化作用に優れた装置を提供せんとするもの
である。The present invention was developed in view of these conventional problems, and eliminates the need to stop operation for cleaning filter media, and also prevents problems such as filter media flowing out of the tank and clogging of the filter media spill prevention net. It is an object of the present invention to provide a device which does not cause the formation of biological purification and which has a particularly excellent biological purification effect compared to conventional devices.
(問題点を解決するための手段〕
このため本発明は、特に、濾材として比重が1より小さ
いものを用い、同じ濾材により最初流動床(濾材が原水
中に浮遊した層)を形成させ、次いでSS分の付着によ
り沈降した後その沈降濾材により固定床を形成させるこ
とにより、原水を流動床と固定床の2つの濾過層で処理
するようにし、しかも、前記固定床から順次濾材槽外に
抜き出し、付着したSS分を除去した後。(Means for Solving the Problems) For this reason, the present invention particularly uses a filter medium with a specific gravity of less than 1, first forms a fluidized bed (a layer in which the filter medium is suspended in raw water) with the same filter medium, and then By forming a fixed bed with the settled filter medium after settling due to the adhesion of SS components, raw water is treated with two filtration layers, a fluidized bed and a fixed bed, and moreover, the raw water is sequentially extracted from the fixed bed to the outside of the filter medium tank. , after removing the attached SS.
再び流動床を形成させるべく槽内に返送させるようにし
たものである。The liquid is returned to the tank to form a fluidized bed again.
すなわち、本発明は槽下部で連絡した下向流路と上向流
路とを有し、前記上向流路に処理水排出部が設けられた
処理槽と、前記下向流路に原水を供給する原水供給手段
と、下向流路内に流動床を形成すべく槽内に装入された
比重が1より小さい濾材と、SS分の付着により槽下部
に沈降して固定床を形成した濾材を槽外に抜き出すため
の濾材抜出手段と、抜き出された濾材をSS分を含む汚
水から分離するための分離装置と1分離された濾材を前
記下向流路に返送するための濾材返送手段とからなるこ
とをその基本的特徴とする。That is, the present invention has a treatment tank that has a downward flow path and an upward flow path that are connected to each other at the bottom of the tank, and a treated water discharge section is provided in the upper flow path, and raw water is supplied to the downward flow path. A raw water supply means, a filter material with a specific gravity of less than 1 charged into the tank to form a fluidized bed in the downward flow path, and a fixed bed formed by settling at the bottom of the tank due to the adhesion of SS components. A filter medium extraction means for extracting the filter medium out of the tank, a separation device for separating the extracted filter medium from wastewater containing SS components, and a filter medium for returning the separated filter medium to the downward flow path. Its basic feature is that it consists of a return means.
本発明の装置によれば、原水が供給される下向流路には
濾材による流動床が形成され、原水は濾材の生物膜によ
り浄化処理される。この流動床はSS分の濾過作用はし
ないが、濾材には次第に原水中のSS分が付着して実質
的な比重が増し、槽下部に沈降して固定床(濾過層)を
形成する。この固定床は槽下部の下向流路と上向流路と
の連通部を塞ぐため、下向した原水は固定床を通過した
後、上向流路に入ることになる。そして、原水はこの固
定床において濾材の生物膜により浄化されるとともに、
SS分が濾過される。固定床を出た処理水は上向流路を
上昇した後、処理水排出部から槽外に排出される。According to the device of the present invention, a fluidized bed is formed by the filter medium in the downward channel to which raw water is supplied, and the raw water is purified by the biofilm of the filter medium. Although this fluidized bed does not have a filtration effect on the SS content, the SS content in the raw water gradually adheres to the filter medium, increasing its substantial specific gravity, and settling at the bottom of the tank to form a fixed bed (filtration layer). Since this fixed bed closes the communication part between the downward flow path and the upward flow path at the bottom of the tank, the raw water flowing downward enters the upward flow path after passing through the fixed bed. Then, the raw water is purified by the biofilm of the filter medium in this fixed bed, and
The SS portion is filtered. After leaving the fixed bed, the treated water ascends through the upward flow path and is then discharged from the treated water discharge section to the outside of the tank.
一方、固定床を形成する濾材は、濾材抜出手段により順
次槽外に抜き出され、必要に応じて洗浄された後、分離
装置でSS分を含む汚水から分離される。そして、濾材
返送手段により処理槽の下向流路に返送され、この濾材
は再び流動床を形成する。On the other hand, the filter media forming the fixed bed are sequentially extracted out of the tank by the filter media extracting means, washed if necessary, and then separated from the wastewater containing the SS content by a separation device. Then, the filter medium is returned to the downward flow path of the processing tank by the filter medium return means, and this filter medium forms a fluidized bed again.
このように本発明の装置では、濾材は流動床形成→固定
床形成→槽外抜出・SS分分離槽内返送→流動床形成と
いう経路で槽内外で循環し、このため従来のような逆洗
処理は全く行われない。また原水は、同じ濾材によって
形成される流動床及び固定床を順次通過するため、特に
生物膜による浄化作用が有効に得られることとなる。In this way, in the device of the present invention, the filter medium circulates inside and outside the tank through the following route: fluidized bed formation → fixed bed formation → extraction from the tank, return to the SS separation tank → fluidized bed formation. No washing process is performed. Furthermore, since the raw water passes sequentially through a fluidized bed and a fixed bed formed by the same filter medium, the purification effect of the biofilm can be particularly effectively obtained.
第1図は本発明の一実施例を示すものである。 FIG. 1 shows an embodiment of the present invention.
図において、1は処理槽であり、該処理槽1は仕切壁4
により中央部に下向流路2、その外側に上向流路3がそ
れぞれ形成され、両流路は槽下部において連絡している
。また処理槽1の底部は摺り林状に構成されている。In the figure, 1 is a processing tank, and the processing tank 1 has a partition wall 4.
Thus, a downward flow path 2 is formed in the center, and an upward flow path 3 is formed outside of the downward flow path 2, and both flow paths communicate with each other at the bottom of the tank. Further, the bottom of the treatment tank 1 is configured in a grove shape.
前記上向流路3の上部には、処理水オーバーフロー用の
処理水排出部10が設けられている。A treated water discharge section 10 for overflowing treated water is provided at the upper part of the upward flow path 3.
5は濾材抜出配管であり、その一端が摺り林状の槽底部
に接続されている。この配管5の途中にはポンプ11が
設けられている。Reference numeral 5 denotes a filter medium extraction pipe, one end of which is connected to the bottom of the tank in the form of a forest. A pump 11 is provided in the middle of this piping 5.
7は前記濾材抜出配管5により抜き出された濾材をSS
分を含む汚水から分離するための分離装置である。この
分離装置7としては、例えば振動スクリーン等が用いら
れる。なお、必要に応じて、この分離装置7の上流側に
濾材の洗浄装置6を設けてもよい。7 is a SS for the filter medium extracted by the filter medium extraction pipe 5.
This is a separation device for separating wastewater from contaminated water. As this separation device 7, for example, a vibrating screen or the like is used. Note that, if necessary, a filter medium cleaning device 6 may be provided upstream of this separation device 7.
8は分離装置7により汚水から分離された枦材を処理槽
1の下向流路2に返送するための濾材返送手段である。Reference numeral 8 denotes a filter medium return means for returning the resin separated from the wastewater by the separator 7 to the downward passage 2 of the treatment tank 1.
9は下向流路2に原水を供給するための原水供給配管で
ある。9 is a raw water supply pipe for supplying raw water to the downward flow path 2.
本発明において使用される粒状の濾材(X)は、比重が
1より小さく、この濾材は当初下向流路2に装入され、
原水の下向流によって流動床(A)を形成する。また、
流動床を形成していた濾材は、SS分が付着することに
よって槽下部に沈降し、下向流路2と下向流路3との連
絡部を塞ぐ固定床(B)を形成する。したがって槽内に
は、以上のような流動床(A)及び固定床(B)を形成
し得るだけの量の濾材を装入しておく必要がある。The granular filter medium (X) used in the present invention has a specific gravity of less than 1, and this filter medium is initially charged into the downward flow path 2,
A fluidized bed (A) is formed by the downward flow of raw water. Also,
The filter medium that had formed the fluidized bed settles to the bottom of the tank due to the adhesion of the SS component, and forms a fixed bed (B) that blocks the communication portion between the downward flow path 2 and the downward flow path 3. Therefore, it is necessary to charge the tank with enough filter media to form the fluidized bed (A) and fixed bed (B) as described above.
第2図は本発明の他の実施例であり、第1図の濾材抜出
配管に代えて、仕切壁13によって、下向流路2と上向
流路3との間に、下端が固定床(B)に面して開口した
濾材抜出流路12を設け、この流路12内にエア配管1
4によりエアを供給するようにしたもので、エア供給に
よる上昇流により、濾材(X)を槽外に抜き出すように
しだものである。FIG. 2 shows another embodiment of the present invention, in which the lower end is fixed between the downward flow path 2 and the upward flow path 3 by a partition wall 13 instead of the filter medium extraction pipe shown in FIG. A filter medium extraction channel 12 opened facing the floor (B) is provided, and an air pipe 1 is installed in this channel 12.
4, and the filter medium (X) is drawn out of the tank by the upward flow caused by the air supply.
以上のような本発明の装置によれば、原水供給配管9か
ら下向流路2に供給された原水は、流動床(A)を通っ
て濾材の生物膜により浄化された後、固定床(B)を通
過することにより、生物膜による浄化とSS分の濾過が
なされ、しかる後上向流路3を上昇して、処理水排出部
10から処理水として排出される。According to the apparatus of the present invention as described above, the raw water supplied from the raw water supply pipe 9 to the downward flow path 2 passes through the fluidized bed (A) and is purified by the biofilm of the filter medium, and then passes through the fixed bed (A). By passing through B), the water is purified by biofilm and the SS content is filtered, and then ascends through the upward flow path 3 and is discharged from the treated water discharge section 10 as treated water.
また、濾材のほうは、当初流動床(A)を形成するが、
SS分の付着により順次下方に沈降して固定床(B)を
形成する。固定床(B)の濾材(X)は、濾材抜出配管
5または濾材抜出流路12を通じて槽外に抜き出され、
分離装置7でSS分を含む汚水と分離された後、濾材返
送手段8を通じ下向流路2に返送され、再び流動床(A
)を形成する。In addition, the filter medium initially forms a fluidized bed (A), but
Due to the adhesion of the SS component, it gradually settles downward to form a fixed bed (B). The filter medium (X) in the fixed bed (B) is extracted to the outside of the tank through the filter medium extraction pipe 5 or the filter medium extraction channel 12,
After being separated from wastewater containing SS in the separator 7, it is returned to the downward flow path 2 through the filter medium return means 8, and then returned to the fluidized bed (A
) to form.
以上述べた本発明によれば、次のような利点がある。 According to the present invention described above, there are the following advantages.
■運転中に濾材を順次槽外に抜き出し、洗浄した後、槽
内に返送することができるため、運転を停止して逆洗を
行うような必要がなく、運転を長時間連続的に行うこと
ができる。■During operation, the filter media can be taken out of the tank one by one, washed, and then returned to the tank, so there is no need to stop the operation and perform backwashing, allowing continuous operation for long periods of time. Can be done.
■逆洗工程がないため、濾材流出や流出防止ネットの目
詰り等の問題を生じることがない。■Since there is no backwashing process, problems such as leakage of filter media and clogging of the leakage prevention net do not occur.
■同じ濾材が槽内で流動床と固定床とを形成し、原水は
この2つの濾材層により処理されるため、特に生物膜に
よる効果的な浄化作用が受けられる。■The same filter media forms a fluidized bed and a fixed bed in the tank, and raw water is treated by these two layers of filter media, so that particularly effective purification by biofilm can be achieved.
第1図は本発明の一実施例を示す説明図である。第2図
は本発明の他の実施例を示す説明図である。第3図は従
来装置の説明図である。
図において、1は処理槽、2は下向流路、3は上向流路
、5は濾材抜出配管、7は分離装置。
8は濾材返送手段、9は原水供給配管、lOは処理水排
出部、12は濾材抜出流路、(A)は流動床。
(B)は固定床、(X)は濾材である。
第1図FIG. 1 is an explanatory diagram showing one embodiment of the present invention. FIG. 2 is an explanatory diagram showing another embodiment of the present invention. FIG. 3 is an explanatory diagram of a conventional device. In the figure, 1 is a processing tank, 2 is a downward flow path, 3 is an upward flow path, 5 is a filter medium extraction pipe, and 7 is a separation device. 8 is a filter medium return means, 9 is a raw water supply pipe, IO is a treated water discharge section, 12 is a filter medium extraction channel, and (A) is a fluidized bed. (B) is a fixed bed, and (X) is a filter medium. Figure 1
Claims (1)
向流路に処理水排出部が設けられた処理槽と、前記下向
流路に原水を供給する原水供給手段と、下向流路内に流
動床を形成すべく槽内に装入された比重が1より小さい
濾材と、SS分の付着により槽下部に沈降して固定床を
形成した濾材を槽外に抜き出すための濾材抜出手段と、
抜き出された濾材をSS分を含む汚水から分離するため
の分離装置と、分離された濾材を前記下向流路に返送す
るための濾材返送手段とを有する生物膜濾過装置。A treatment tank having a downward flow path and an upward flow path communicating at the bottom of the tank, and a treated water discharge section provided in the upper flow path, and a raw water supply means for supplying raw water to the downward flow path. Then, the filter material with a specific gravity of less than 1 was charged into the tank to form a fluidized bed in the downward flow path, and the filter material that had settled at the bottom of the tank due to the adhesion of SS components and formed a fixed bed was removed from the tank. a filter medium extracting means for extracting the filter medium;
A biofilm filtration device comprising: a separation device for separating extracted filter media from wastewater containing SS components; and a filter media return means for returning the separated filter media to the downward flow path.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62330981A JPH01171693A (en) | 1987-12-26 | 1987-12-26 | Biomembrane filtration apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62330981A JPH01171693A (en) | 1987-12-26 | 1987-12-26 | Biomembrane filtration apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01171693A true JPH01171693A (en) | 1989-07-06 |
Family
ID=18238502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62330981A Pending JPH01171693A (en) | 1987-12-26 | 1987-12-26 | Biomembrane filtration apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01171693A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002136984A (en) * | 2000-11-06 | 2002-05-14 | Fuji Clean Kogyo Kk | Apparatus and method for treating sewage |
CN102465310A (en) * | 2010-10-28 | 2012-05-23 | 本田技研工业株式会社 | Water electrolysis system |
US10449052B2 (en) | 2009-03-27 | 2019-10-22 | Depuy Synthes Products, Inc | Methods and devices for preparing and implanting tissue scaffolds |
-
1987
- 1987-12-26 JP JP62330981A patent/JPH01171693A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002136984A (en) * | 2000-11-06 | 2002-05-14 | Fuji Clean Kogyo Kk | Apparatus and method for treating sewage |
US10449052B2 (en) | 2009-03-27 | 2019-10-22 | Depuy Synthes Products, Inc | Methods and devices for preparing and implanting tissue scaffolds |
CN102465310A (en) * | 2010-10-28 | 2012-05-23 | 本田技研工业株式会社 | Water electrolysis system |
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