JPH0533808U - Sewage treatment equipment using floating media - Google Patents
Sewage treatment equipment using floating mediaInfo
- Publication number
- JPH0533808U JPH0533808U JP089060U JP8906091U JPH0533808U JP H0533808 U JPH0533808 U JP H0533808U JP 089060 U JP089060 U JP 089060U JP 8906091 U JP8906091 U JP 8906091U JP H0533808 U JPH0533808 U JP H0533808U
- Authority
- JP
- Japan
- Prior art keywords
- filter medium
- floating filter
- layer
- closed tank
- floating
- 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)
Abstract
(57)【要約】
【目的】 浮上ろ材層に下方から汚水と曝気用の空気を
供給し、夾雑物および生物膜等の分離再生が容易な汚水
の処理装置を得る。
【構成】 密閉槽内に浮上ろ材を充填するとともに、こ
の浮上ろ材層中に、下方から汚水と曝気用空気を送入
し、そのろ液を密閉槽の上部から取り出し、さらに、密
閉層の底部に浮上ろ材の撹拌翼を設けたものである。浮
上ろ材に付着した微細固形物および生物膜を除去するに
当って、撹拌翼を回転することによって、最も目詰りの
激しい浮上ろ材の下層を先ずほぐして順次上層をほぐす
ことができ、ろ材を完全に撹拌して目詰り物を分離して
除去することができる。
(57) [Abstract] [Purpose] To obtain a sewage treatment device in which sewage and aeration air are supplied to the floating filter medium layer from below to easily separate and regenerate contaminants and biofilms. [Structure] The floating filter medium is filled in the closed tank, and sewage and aeration air are fed into the floating filter layer from below, and the filtrate is taken out from the upper part of the closed tank, and further, the bottom part of the closed layer. It is equipped with a stirring blade for the floating filter medium. When removing fine solids and biofilm adhering to the floating filter medium, by rotating the stirring blade, the lower layer of the floating filter medium with the most clogging can be unraveled first, and then the upper layer can be unraveled in order to complete the filter medium. The clogging can be separated and removed by stirring.
Description
【0001】[0001]
この考案は、浮上ろ材を用いた汚水の処理装置の改良に関する。 The present invention relates to improvement of a wastewater treatment device using a floating filter medium.
【0002】[0002]
従来、この種浮上ろ材を用いた汚水の処理装置としては、特公平2−2268 2号、特公昭63−85号等がある。特公平2−22682号は、密閉タンク内 に浮上ろ材を充填し、この浮上ろ材層に汚水を下部から送入してそのろ液を頂部 から取出すようにしたろ過機である。また、特公昭63−85号は、密閉タンク に原液よりも若干軽い比重のろ材物質を装入し、このろ材物質を密閉タンク内に おいて、これらを通過させない帯域内におき、そのろ材物質中を汚水を流すとと もに曝気を行い、原液の浄化を図ったものである。 Conventionally, as a sewage treatment apparatus using this type of floating filter material, there are Japanese Examined Patent Publication No. 2-226882 and Japanese Examined Patent Publication No. 63-85. Japanese Examined Patent Publication No. 2-22682 is a filter in which a closed tank is filled with a floating filter medium, and sewage is sent to the floating filter medium layer from the lower part and the filtrate is taken out from the top part. In Japanese Examined Patent Publication No. 63-85, a filter material having a specific gravity slightly lighter than that of the stock solution is charged into a closed tank, and the filter material is placed in a sealed tank in a zone that does not pass through the filter material. This is to purify the undiluted solution by flushing sewage and aeration.
【0003】[0003]
然しながら、上述の特公平2−22682号発明は、原液によって押上げられ て圧密状の浮上ろ材によるろ過器であり、生物的処理はできず、また、特公昭6 3−85号発明では、ろ材は、その粒子の通過し得ない帯域にあり、ここで発生 した異物のうち、大きく成長したものは分離できない。また、この発明では、原 液は上向流でありながら、異物を上下に取出すものであり、分離しにくいはもと よりろ過機としての主要な機能を欠く物である。 However, the invention of Japanese Patent Publication No. 2-22682 mentioned above is a filter using a flotation filter material that is pushed up by the undiluted solution and is in a compacted state, and cannot be biologically treated. Are in the zone where the particles cannot pass, and among the foreign substances generated here, those that have grown large cannot be separated. Further, in the present invention, the stock solution is an upward flow, but it takes out foreign matter up and down, which makes it difficult to separate and lacks a major function as a filter.
【0004】[0004]
この考案は、ろ過機の機能を備え乍ら、生物的処理も可能にしたものであって 、その要旨とするところは、密閉槽内に浮上ろ材を充填し、その密閉槽の底部に 、撹拌翼および原水の導入口を設けるとともに、上記浮上ろ材層の上層には、ろ 液の取出管を埋設し、浮上ろ材層の下方および下層部に散気管を設け、さらに、 密閉槽の頂部にエヤ抜孔を設けたものである。 The present invention, which has the function of a filter, enables biological treatment, and the gist of the invention is to fill a floating filter material in a closed tank and to stir the bottom of the closed tank. A wing and an inlet for raw water are provided, a filtrate extraction pipe is embedded in the upper layer of the floating filter material layer, air diffusers are provided below and in the lower portion of the floating filter material layer, and an air filter is provided on the top of the closed tank. A hole is provided.
【0005】[0005]
この考案に係る装置は、上述のように構成してあり、密閉槽の下部から供給さ れた原液は、浮上ろ材層中を上昇する間に、その夾雑物がろ材によって捕捉され 、そのろ液は取出管から取出することができる。これと同時に、浮上ろ材層の下 方および下層の散気管からの空気によって、原液が曝気され原液中に含まれる溶 解性の有機物質が酸化分解される。すなわれ、浮上ろ材によるろ過と好気性生物 処理を同時に行うことができる。以上のようにして、浮上ろ材が浮遊固形物や成 長した生物膜でろ材層が詰まったときには、撹拌翼を回転させることで、目詰り の最も激しい浮上ろ材層をほぐすことで、浮上ろ材層を撹拌することができ、浮 上ろ材から分離した生物膜等の異物を密閉槽の下部から取出すことができる。以 下、図面に基づいてこの考案を具体的に説明する。 The device according to the present invention is configured as described above, and while the stock solution supplied from the lower part of the closed tank rises in the floating filter medium layer, the impurities are captured by the filter medium and the filtrate is collected. Can be removed from the extraction tube. At the same time, the undiluted solution is aerated by the air from the lower and lower air diffusing tubes of the floating filter material layer, and the soluble organic substances contained in the undiluted solution are oxidatively decomposed. That is, it is possible to simultaneously perform filtration by a floating filter medium and aerobic biological treatment. As described above, when the filter material layer is clogged with suspended solids or grown biofilm, the stirring blade is rotated to loosen the filter material layer that causes the most clogging, and the floating filter material layer is removed. Can be stirred, and foreign matter such as biofilm separated from the floating filter can be taken out from the lower part of the closed tank. Hereinafter, the present invention will be specifically described with reference to the drawings.
【0006】[0006]
図1において、符号1は、密閉タンク、2は密閉タンクに充填した発泡スチロ ールよりなる浮上ろ材、3は密閉タンク1の底部に設けたろ材の撹拌翼、4は浮 上ろ材層の下層部に埋設した散気管、5は密閉タンク1の下部に設けた散気管で ある。 In FIG. 1, reference numeral 1 is a closed tank, 2 is a floating filter medium made of expanded polystyrene filled in the closed tank, 3 is a stirring blade of a filter medium provided at the bottom of the closed tank 1, and 4 is a lower layer of the floating filter layer. Air diffusers 5 embedded in the section are air diffusers provided in the lower part of the closed tank 1.
【0007】 次に符号6は、密閉タンク1の下底部に開口する原液の供給管で他端は、ポン プP1を介して原液槽7に接続してある。尚、原液の供給管6の回路中、符号P Sは圧力スイッチ、8は流量計を示すものである。次に、符号9は、浮上ろ材層 の上層部に埋設したろ液の集水管で処理水管10を接続してこれを処理水槽11 に開口させるとともに、岐管10aを分岐してこの岐管10aを逆洗ポンプP2 を介して処理水槽11に接続している。10bは、岐管10aに設けた逆止弁で ある。Next, reference numeral 6 is a stock solution supply pipe that opens to the lower bottom of the closed tank 1, and the other end is connected to a stock solution tank 7 via a pump P1. In the circuit of the supply pipe 6 for the undiluted solution, reference symbol P S is a pressure switch, and 8 is a flow meter. Next, reference numeral 9 is a filtrate collecting water pipe buried in the upper part of the floating filter medium layer, which connects the treated water pipe 10 to the treated water tank 11 and opens the manifold 10a to branch the manifold 10a. Is connected to the treated water tank 11 via a backwash pump P2. 10b is a check valve provided in the manifold 10a.
【0008】 次に、符号12は、前述の原液の供給管6に接続した排水管であり、排水弁V 1によって供給管6と開閉自在にするとともに、その他端部には、処理水管10 から分岐した捨水管10cが接続してある。符号V2は、捨水管10cに設けた 捨水弁であり、捨水管10cは、ろ過初期の夾雑物の混入したろ液を排棄するた めのものである。また、図1において、符号V4はエヤー抜弁、M1は、撹拌翼 3の駆動モーター、B1はブロワーである。図2は、この考案に係る装置の運転 タイムチャートであり、各機器の符号は、図1に一致させてある。Next, reference numeral 12 is a drain pipe connected to the above-mentioned undiluted solution supply pipe 6, which can be opened and closed with the supply pipe 6 by a drain valve V 1, and at the other end thereof from the treated water pipe 10 A branched drain pipe 10c is connected. Reference numeral V2 is a drain valve provided in the drain pipe 10c, and the drain pipe 10c is for discarding the filtrate mixed with impurities at the initial stage of filtration. Further, in FIG. 1, reference numeral V4 is an air vent valve, M1 is a drive motor for the stirring blade 3, and B1 is a blower. FIG. 2 is an operation time chart of the device according to the present invention, and the reference numerals of the devices are the same as those in FIG.
【0009】 この考案に係る装置は、上述のように構成してあり、供給管6で密閉タンク1 内に供給された原水は、散気管4、5によって曝気されるとともに、浮上ろ材層 中を上昇して夾雑物が捕捉されて浄化され、処理水管10を経て処理水槽11に 取出される。すなわち、原水に対して散気管4、5による曝気と浮上ろ材2によ るろ過とが同時に行われるもので、そのろ液は夾雑物が分離されるのみならず、 曝気によって生物的処理がなされ、質的にも清浄なろ液を得ることができる。The apparatus according to the present invention is configured as described above, and the raw water supplied into the closed tank 1 by the supply pipe 6 is aerated by the diffuser pipes 4 and 5 and flows through the floating filter material layer. Ascends, impurities are captured and purified, and are taken out to the treated water tank 11 through the treated water pipe 10. That is, the raw water is simultaneously aerated by the air diffusers 4 and 5 and filtered by the floating filter medium 2. The filtrate is not only separated from impurities, but also biologically treated by the aeration. Therefore, a qualitatively clean filtrate can be obtained.
【0010】 以上のように処理運転を継続して、ろ材層が目詰りすると密閉タンク1内の圧 力が上昇する。この圧力の上昇は、圧力スイッチPSによって検知され、その検 知信号によって、各機器が作動して処理運転からろ材の洗浄工程に移行する。こ れを図2に基づいて詳述すると、圧力スイッチPSからの信号によって駆動モー ターM1が回転し、目詰りしたろ材層の下部層を解きほぐす。このとき、エヤー 抜き弁V4以外の機器、バルブ等は停止している。(図2参照)そして、夾雑物 を分離してろ材層の静止を待ったのち、逆洗ポンプP2によって処理水を集水管 9から浮上ろ材層に送り、ろ材を逆洗する。このとき、排水弁V1は開かれてお り、夾雑物および生物膜等を含んだ洗浄汚泥水は、排水管12を経て系外に排出 される。以上のろ材の洗浄操作において、この考案では、上向流で最も目詰りし 易いろ材層の下面を撹拌翼3によって解きほぐすのでろ材を完全に撹拌して夾雑 物をろ材から分離することができる。As described above, when the treatment operation is continued and the filter layer is clogged, the pressure in the closed tank 1 increases. This increase in pressure is detected by the pressure switch PS, and each device operates according to the detection signal to shift from the processing operation to the filter medium cleaning step. Explaining this in detail with reference to FIG. 2, the drive motor M1 is rotated by a signal from the pressure switch PS, and the lower layer of the clogged filter medium layer is unraveled. At this time, the devices and valves other than the air release valve V4 are stopped. (See FIG. 2) Then, after separating the impurities and waiting for the filter medium layer to stand still, the treated water is sent from the water collecting pipe 9 to the floating filter medium layer by the backwash pump P2 to backwash the filter medium. At this time, the drain valve V1 is opened, and the cleaning sludge water containing contaminants and biofilms is discharged to the outside of the system through the drain pipe 12. In the above cleaning operation of the filter medium, according to the present invention, the lower surface of the filter medium layer which is most likely to be clogged in the upward flow is unraveled by the stirring blade 3, so that the filter medium can be completely stirred to separate the contaminants from the filter medium.
【0011】 以上のようにしてろ材の洗浄が終わると、逆洗ポンプP2を停止するとともに 、排水弁V1を閉止して原水ポンプP1を作動し処理運転に入る。同時に、ブロ ワーB1によって曝気空気を供給して元の運転に復帰するのであるが、ろ材洗浄 直後のろ材層中に残存する夾雑物等の処理水への混入を避けるため、初期の処理 水を捨水する。この捨水操作は、図2において、処理水弁V3を閉じて捨水弁V 2を開放して行われる。尚、以上のろ材の洗浄操作、汚水の処理操作における各 機器、弁等の操作は、所定のタイムチャートに基づいて自動的に行われるもので ある。When the cleaning of the filter medium is completed as described above, the backwash pump P2 is stopped, the drain valve V1 is closed and the raw water pump P1 is operated to start the processing operation. At the same time, aeration air is supplied by the blower B1 to return to the original operation. However, in order to avoid contamination of the treated water with impurities remaining in the filter layer immediately after washing the filter medium, the initial treated water is Dispose of water. This drainage operation is performed by closing the treated water valve V3 and opening the drainage valve V2 in FIG. The above-mentioned operations for cleaning the filter medium and for treating each device and valve in the wastewater treatment operation are automatically performed based on a predetermined time chart.
【0012】[0012]
このように、この考案に係る装置は、極めて軽量な浮上ろ材を用いて設置する にも、そのろ材を洗浄再生処理するにも手数を要しないものであり、特に、この 考案では、夾雑物の分離と曝気による汚水の生物的処理が同時にでき、汚水の質 的処理まで可能にしたものであって、汚水処理上得られる利益は著大なものであ る。 As described above, the device according to the present invention does not require any labor for installation using an extremely lightweight floating filter medium and for cleaning and reprocessing the filter medium. The biological treatment of sewage by separation and aeration can be performed at the same time, and even qualitative treatment of sewage is possible, and the profits obtained from sewage treatment are enormous.
【図1】この考案に係る汚水の処理装置のフローシート
である。FIG. 1 is a flow sheet of a wastewater treatment apparatus according to the present invention.
【図2】この考案に係る汚水の処理装置の作動タイムチ
ャートである。FIG. 2 is an operation time chart of the sewage treatment apparatus according to the present invention.
1 密閉タンク 2 浮上ろ材 3 撹拌翼 4、5 散気管 9 集水管 1 Closed tank 2 Floating filter medium 3 Stirring blades 4, 5 Diffuser pipe 9 Water collecting pipe
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C02F 3/08 B 6647−4D 3/10 A 6647−4D ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location C02F 3/08 B 6647-4D 3/10 A 6647-4D
Claims (1)
密閉槽1の底部に、撹拌翼3および原水の導入口を設け
るとともに、上記浮上ろ材層の上層にはろ液の集水管9
を埋設し、浮上ろ材層の下方および下層部に散気管4、
5を設け、さらに、密閉槽1の頂部にエヤ抜孔を設けて
なる浮上ろ材を用いた汚水の処理装置。1. A closed tank 1 is filled with a floating filter medium 2, a stirring blade 3 and an inlet for raw water are provided at the bottom of the closed tank 1, and a filtrate collecting pipe 9 is provided above the floating filter layer.
Embedded in the air diffusion tube 4, below the floating filter layer and in the lower layer.
5, a treatment apparatus for sewage using a floating filter medium, further comprising an air vent hole at the top of the closed tank 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP089060U JPH0533808U (en) | 1991-10-03 | 1991-10-03 | Sewage treatment equipment using floating media |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP089060U JPH0533808U (en) | 1991-10-03 | 1991-10-03 | Sewage treatment equipment using floating media |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0533808U true JPH0533808U (en) | 1993-05-07 |
Family
ID=13960312
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP089060U Pending JPH0533808U (en) | 1991-10-03 | 1991-10-03 | Sewage treatment equipment using floating media |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0533808U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20140017558A (en) * | 2011-04-25 | 2014-02-11 | 가부시키가이샤 이시가키 | Buoyant filter medium-stirring device and filter |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6258796A (en) * | 1985-09-06 | 1987-03-14 | Mitsubishi Electric Corp | Pal system application type luminance signal and chrominance signal separation filter |
JPH01262909A (en) * | 1988-04-13 | 1989-10-19 | Nippon Rensui Kk | Up-flow filter apparatus |
-
1991
- 1991-10-03 JP JP089060U patent/JPH0533808U/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6258796A (en) * | 1985-09-06 | 1987-03-14 | Mitsubishi Electric Corp | Pal system application type luminance signal and chrominance signal separation filter |
JPH01262909A (en) * | 1988-04-13 | 1989-10-19 | Nippon Rensui Kk | Up-flow filter apparatus |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20140017558A (en) * | 2011-04-25 | 2014-02-11 | 가부시키가이샤 이시가키 | Buoyant filter medium-stirring device and filter |
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