JP2679531B2 - Filtration device - Google Patents

Filtration device

Info

Publication number
JP2679531B2
JP2679531B2 JP13678392A JP13678392A JP2679531B2 JP 2679531 B2 JP2679531 B2 JP 2679531B2 JP 13678392 A JP13678392 A JP 13678392A JP 13678392 A JP13678392 A JP 13678392A JP 2679531 B2 JP2679531 B2 JP 2679531B2
Authority
JP
Japan
Prior art keywords
water
ejector
pipe
advection
backwash
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.)
Expired - Lifetime
Application number
JP13678392A
Other languages
Japanese (ja)
Other versions
JPH05329490A (en
Inventor
求 末方
Original Assignee
株式会社イナックス
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 株式会社イナックス filed Critical 株式会社イナックス
Priority to JP13678392A priority Critical patent/JP2679531B2/en
Publication of JPH05329490A publication Critical patent/JPH05329490A/en
Application granted granted Critical
Publication of JP2679531B2 publication Critical patent/JP2679531B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は生物膜濾過装置等の濾過
装置に係り、特に逆洗水の供給機構とを改良した濾過装
置に関する。
The present invention relates relates to a filtration device such as a biological membrane filtration apparatus, a filtration device having an improved supply mechanism backwash water especially.

【0002】[0002]

【従来の技術】生物膜濾過装置は、周知(例えば特公平
3−77000号)の通り、水槽と、該水槽内に設置さ
れた生物膜濾床と、該生物膜濾床の下側に設けられた散
気装置とを有するものである。従来の生物膜濾過装置の
概略的な構成とその作動について第3図を参照して説明
する。
2. Description of the Related Art As is well known (for example, Japanese Patent Publication No. 3-77000), a biofilm filtration device is provided with a water tank, a biofilm filter installed in the water tank, and a lower side of the biofilm filter bed. And an air diffuser that is installed. A schematic configuration of a conventional biofilm filtration device and its operation will be described with reference to FIG.

【0003】第3図において、水槽10内に生物膜濾床
12が設置され、該生物膜濾床12の下側に散気管14
が設置されている。生物膜濾床12の逆洗を行なうため
に、逆洗配管(逆洗水供給用配管)16を介して逆洗ポ
ンプ18から逆洗水が水槽10の底部に導入可能とされ
ている。この逆洗配管16は移流管20の途中に接続さ
れている。
In FIG. 3, a biofilm filter bed 12 is installed in a water tank 10, and an air diffuser 14 is provided below the biofilm filter bed 12.
Is installed. In order to carry out backwashing of the biofilm filter bed 12, backwash water can be introduced from the backwash pump 18 to the bottom of the water tank 10 through the backwash pipe (pipe for supplying backwash water) 16. The backwash pipe 16 is connected in the middle of the advection pipe 20.

【0004】水槽10へは原水供給管22から原水が供
給され、生物膜濾床12と接触し、生物処理されると共
に、濾床12によって濾過処理される。濾床12を通過
した処理水は移流管20を経て排出される。なお、好気
性生物処理の場合、この生物処理の間中、散気管14か
ら空気を供給する。
Raw water is supplied to the water tank 10 from a raw water supply pipe 22, comes into contact with the biological membrane filter bed 12, is biologically processed, and is filtered by the filter bed 12. The treated water that has passed through the filter bed 12 is discharged through the advection pipe 20. In the case of aerobic biological treatment, air is supplied from the air diffuser 14 throughout the biological treatment.

【0005】生物処理の進行に伴って、生物膜濾床12
の通水抵抗が増大してくる。そうすると、第3図(1)
に示す如く、生物膜濾床12の上側の水位が上昇してく
る。水位センサ24で検知される水位が所定水位以上に
なると、逆洗を行なう。即ち、まず、生物膜濾床12の
上方部位において水槽10に接続されている排水管26
の排水弁28を開き、生物膜濾床12の上側の水位を下
げる。
As the biological treatment progresses, the biofilm filter bed 12
The water resistance of the river will increase. Then, Fig. 3 (1)
As shown in, the water level above the biofilm filter bed 12 rises. When the water level detected by the water level sensor 24 reaches or exceeds a predetermined water level, backwashing is performed. That is, first, the drain pipe 26 connected to the water tank 10 at the upper portion of the biofilm filter bed 12.
The drainage valve 28 of the above is opened to lower the water level above the biofilm filter bed 12.

【0006】第3図(2)の如く十分に排水が行なわれ
た後、排水弁28を閉弁し、次いで散気管14から空気
又はその他の気体を送り込み、生物膜濾床12に付着し
ている生物膜及び汚泥を気泡によって剥ぎ取る如くして
減少させる。
After the water has been sufficiently drained as shown in FIG. 3 (2), the drain valve 28 is closed, and then air or other gas is sent from the diffuser pipe 14 to adhere to the biofilm filter bed 12. Reduces biofilms and sludge present by removing air bubbles.

【0007】次いで、第3図(4)の如く、逆洗ポンプ
18を作動させ、逆洗水を水槽10の底部に導入し、剥
ぎ取られた生物膜及び汚泥を逆洗水と共に生物膜濾床1
2の上方に流出させる。これにより、第5図に示すよう
に、生物膜濾床12の上側に、剥離した生物膜、汚泥を
多量に含んだ水がたまるので、排水弁28を開き、この
水を排出する。
Then, as shown in FIG. 3 (4), the backwash pump 18 is operated to introduce the backwash water into the bottom of the water tank 10 and remove the stripped biofilm and sludge together with the backwash water. Floor 1
Drain above 2. As a result, as shown in FIG. 5, water containing a large amount of the separated biofilm and sludge collects on the upper side of the biofilm filter bed 12, so the drain valve 28 is opened and the water is discharged.

【0008】これにより、第3図(6)の如く、初期状
態に復帰するので、再び原水供給管22から原水を供給
して生物処理を行なう。なお、この生物処理を行なって
いる間、移流管20に設けられた移流弁30は開放され
ている。また、逆洗ポンプ18を作動させて逆洗水を水
槽10内に導入するときには、移流弁30を閉弁状態と
しておき、逆洗水が移流管20の下流方向に向って流れ
ることを防止する。
As a result, as shown in FIG. 3 (6), the initial state is restored, and raw water is again supplied from the raw water supply pipe 22 to perform biological treatment. Note that the advection valve 30 provided in the advection pipe 20 is opened during the biological treatment. When the backwash water is introduced into the water tank 10 by operating the backwash pump 18, the advection valve 30 is kept closed to prevent the backwash water from flowing in the downstream direction of the advection pipe 20. .

【0009】[0009]

【発明が解決しようとする課題】上記従来の濾過装置に
おいては、排水弁28と移流弁30が必要であった。こ
の弁28、30が設置されている環境は、硫化水素など
の腐食性ガス濃度が高かったり、湿気の多いきわめて腐
食性の強い環境であると共に、弁の点検、修理を行ない
にくい箇所であるのが通常である。このため、排水弁2
8や移流弁30の耐久性が損なわれ、かつそれらの点
検、修理が行ないにくいという問題があった。
DISCLOSURE OF THE INVENTION In the above conventional filtering device, the drain valve 28 and the advection valve 30 are required. The environment in which the valves 28 and 30 are installed is a highly corrosive environment where the concentration of corrosive gas such as hydrogen sulfide is high, and it is a place where it is difficult to inspect and repair the valves. Is normal. Therefore, the drain valve 2
8 and the advection valve 30 are impaired in durability, and it is difficult to inspect and repair them.

【0010】[0010]

【課題を解決するための手段】本発明の濾過装置は、水
槽と、該水槽内に設置された濾床と、該濾床の下側に設
けられた散気装置と、該水槽の下部から水を抜き出すた
めの移流管と、該移流管に接続された逆洗水供給用配管
と、を有する濾過装置において、該移流管の途中にエジ
ェクタを設け、前記逆洗水供給用配管を該エジェクタの
作動水導入口に接続し、該エジェクタの作動水流出口に
前記移流管のうちエジェクタよりも上流側の部分を接続
し、該エジェクタの負圧吸引口に前記移流管のうちエジ
ェクタよりも下流側の部分を接続したことを特徴とする
ものである。
The filtration device of the present invention comprises a water tank, a filter bed installed in the water tank, an air diffuser provided below the filter bed, and a lower portion of the water tank. In a filtering device having an advection pipe for extracting water and a backwash water supply pipe connected to the advection pipe, an ejector is provided in the middle of the advection pipe, and the backwash water supply pipe is connected to the ejector. Connected to the working water inlet of the ejector, a part of the advection pipe upstream of the ejector is connected to the actuating water outlet of the ejector, and the negative pressure suction port of the ejector is downstream of the ejector of the advection pipe. It is characterized by connecting the part of.

【0011】[0011]

【作用】本発明の濾過装置においては、逆洗水をエジェ
クタを介して水槽下部に導入すると、エジェクタで発生
した負圧がエジェクタよりも下流側の移流管の水を吸引
する作用をなす。この結果、従来用いられていた移流弁
を省略しても、逆洗水が移流管の下流側へ流出すること
がない。即ち、本発明の濾過装置によると、移流弁を省
略できる。
In the filtering apparatus of the present invention, when the backwash water is introduced into the lower part of the water tank through the ejector, the negative pressure generated in the ejector serves to suck the water in the advection pipe on the downstream side of the ejector. As a result, even if the conventionally used advection valve is omitted, the backwash water will not flow out to the downstream side of the advection pipe. That is, according to the filtration device of the present invention , the advection valve can be omitted.

【0012】[0012]

【実施例】以下図面を参照して実施例について説明す
る。第1図は本発明の実施例に係る生物膜濾過装置の構
成を示す縦断面図、第2図は実施例装置におけるエジェ
クタ部分の断面図である。
Embodiments will be described below with reference to the drawings. FIG. 1 is a vertical cross-sectional view showing the configuration of a biofilm filtration device according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view of an ejector portion of the embodiment device.

【0013】本実施例においても、水槽10内に生物膜
濾床12が設置され、その下側に散気管14が設置され
ている。水槽10内には原水供給管22から原水が供給
され、処理水は移流管20を経て取り出される。本実施
例では、生物処理水は逆洗水槽32に一旦導入されてお
り、この逆洗水槽32内に水中ポンプよりなる逆洗ポン
プ18が設置されている。
Also in this embodiment, the biofilm filter bed 12 is installed in the water tank 10 and the air diffuser 14 is installed below it. Raw water is supplied from the raw water supply pipe 22 into the water tank 10, and the treated water is taken out through the advection pipe 20. In the present embodiment, the biologically treated water is once introduced into the backwash water tank 32, and the backwash pump 18 which is an underwater pump is installed in the backwash water tank 32.

【0014】本実施例では、第3図に示した従来装置の
排水管26、排水弁28及び移流弁30がいずれも省略
されている。その代わりに、移流管20の途中にエジェ
クタ34が設置されており、このエジェクタ34の作動
水導入口36に逆洗配管16が接続されている。エジェ
クタ34の負圧吸引口38に移流管20のうちエジェク
タ34よりも下流側の部分が接続されており、エジェク
タ34の作動水流出口40に移流管20のうちエジェク
タ34よりも上流側の部分が接続されている。
In this embodiment, all of the drain pipe 26, drain valve 28 and advection valve 30 of the conventional device shown in FIG. 3 are omitted. Instead, the ejector 34 is installed in the middle of the advection pipe 20, and the backwash pipe 16 is connected to the working water introduction port 36 of the ejector 34. A portion of the advection pipe 20 downstream of the ejector 34 is connected to the negative pressure suction port 38 of the ejector 34, and a portion of the advection pipe 20 upstream of the ejector 34 is connected to the working water outlet 40 of the ejector 34. It is connected.

【0015】前記水槽10内にはエアリフトポンプ42
が設置されている。このエアリフトポンプ42にあって
は、生物膜濾床12の上側において吸込口44が開口し
ており、この吸込口44から短い立上り部46が立ち上
がり、次いで立下り部48及び長い立上り部50を介し
て排出部52に至っている。この立上り部50の下部に
空気導入用の配管54が接続されている。
An air lift pump 42 is installed in the water tank 10.
Is installed. In the air lift pump 42, the suction port 44 is opened on the upper side of the biofilm filter bed 12, a short rising part 46 rises from the suction port 44, and then a falling part 48 and a long rising part 50 are passed. To the discharge section 52. A pipe 54 for introducing air is connected to the lower portion of the rising portion 50.

【0016】このように構成された生物膜濾過装置にお
いて、原水供給管22から供給された原水が生物膜濾床
12と接触し、生物処理及び濾過処理される。処理水は
移流管20を経て逆洗水槽32に取り出される。
In the biofilm filtration device constructed as described above, the raw water supplied from the raw water supply pipe 22 comes into contact with the biofilm filter bed 12, and is subjected to biological treatment and filtration treatment. The treated water is taken out to the backwash water tank 32 through the advection pipe 20.

【0017】生物膜濾床12の生物膜が成長し、水槽1
0内の水位が規定水位以上になった場合には、水位セン
サ24からの信号に基いて原水供給が一旦停止されると
共に、配管54に空気又はその他のガスを供給してエア
リフトポンプ42を作動させる。これにより、水槽10
内の水位はエアリフトポンプ42の吸込口44のレベル
にまで下がる。そこで、散気管14から空気又はその他
のガスを噴出させ、生物膜濾床12の余分な生物膜を、
気泡で擦る如くして剥離させる。次いで、逆洗ポンプ1
8を作動させ、逆洗水を水槽10内に導入し、生物膜濾
床12から剥ぎ取られた生物膜を逆洗水によって濾床1
2の上方に運び出す。
Biofilm The biofilm of the filter bed 12 grows and the aquarium 1
When the water level in 0 becomes equal to or higher than the specified water level, the raw water supply is temporarily stopped based on the signal from the water level sensor 24, and air or other gas is supplied to the pipe 54 to operate the air lift pump 42. Let As a result, the aquarium 10
The water level inside drops to the level of the suction port 44 of the air lift pump 42. Therefore, air or other gas is ejected from the air diffuser 14 to remove excess biofilm from the biofilm filter bed 12,
Peel off like rubbing with bubbles. Then backwash pump 1
8 is operated, backwash water is introduced into the water tank 10, and the biofilm stripped off from the biofilm filter bed 12 is washed with the backwash water to the filter bed 1
Carry above 2.

【0018】そこで、再びエアリフトポンプ42を作動
させ、濾床12の水を水槽10外に排出させる。
Then, the air lift pump 42 is operated again to discharge the water in the filter bed 12 out of the water tank 10.

【0019】必要に応じ、逆洗水の導入とエアリフトポ
ンプ42による排水を繰り返し行ない、剥離した生物膜
を十分に水槽10外に排出する。
If necessary, backwash water is introduced and drained by the air lift pump 42 repeatedly to sufficiently discharge the peeled biofilm out of the water tank 10.

【0020】このような生物膜濾床12の逆洗が終了し
た後、再び原水供給管22から原水を供給し、生物処理
及び濾過処理を行なう。
After the backwashing of the biological membrane filter bed 12 is completed, raw water is again supplied from the raw water supply pipe 22 to perform biological treatment and filtration treatment.

【0021】本実施例においては、前記した通り、排水
弁及び移流弁が不要である。従って、装置の耐久性がき
わめて高い。なお、エジェクタ34を設けているので、
逆洗ポンプ18を作動させて逆洗配管16から水槽10
内に逆洗水を導入する場合にも、逆洗水が移流管の下流
側に向って流出することがない。即ち、エジェクタ34
の負圧吸引口38に移流管20の下流側が接続されてい
るため、逆洗水をエジェクタ34に導入すると、下流側
の移流管20内の水はエジェクタ34に向って吸引され
るようになり、移流管下流側に向って逆洗水が流出する
ことがない。
In this embodiment, as described above, the drain valve and advection valve are unnecessary. Therefore, the durability of the device is extremely high. Since the ejector 34 is provided,
The backwash pump 18 is operated to move the backwash pipe 16 to the water tank 10.
Even when the backwash water is introduced into the inside, the backwash water does not flow out toward the downstream side of the advection pipe. That is, the ejector 34
Since the downstream side of the advection pipe 20 is connected to the negative pressure suction port 38, the water in the advection pipe 20 on the downstream side is sucked toward the ejector 34 when the backwash water is introduced into the ejector 34. The backwash water does not flow out toward the downstream side of the advection pipe.

【0022】上記実施例では、水位センサ24の検知水
位が所定水位になると逆洗を行なうようにしているが、
定期的又は随時に逆洗を行なっても良い。
In the above embodiment, backwashing is performed when the water level detected by the water level sensor 24 reaches a predetermined water level.
You may perform backwash regularly or at any time.

【0023】上記実施例では、エアリフトポンプ42が
生物膜濾床12内に延設しているが、このエアリフトポ
ンプ42は水槽10の外部に配置しても良い。
In the above embodiment, the air lift pump 42 extends inside the biofilm filter bed 12, but the air lift pump 42 may be arranged outside the water tank 10.

【0024】本発明装置は、好気性生物膜処理及び嫌気
性生物膜処理のいずれにも適用できる。本発明は、生物
膜濾床以外の濾床(例えば、砂や活性炭など)を有する
濾過装置にも適用できる。
The apparatus of the present invention can be applied to both aerobic biofilm treatment and anaerobic biofilm treatment. The present invention can also be applied to a filtration device having a filter bed (for example, sand or activated carbon) other than the biofilm filter bed.

【0025】[0025]

【発明の効果】本発明の濾過装置にあっては、従来必要
であった移流弁が不要である。
The filter device of the present invention does not require the advection valve, which has been conventionally required.

【0026】このように、比較的故障し易い移流弁が省
略されているため、本発明装置はきわめて耐久性が良
い。また、移流弁を点検、修理する手間が省けるため、
本発明装置は保守管理がきわめて容易である。
As described above, since the advection valve, which is relatively susceptible to failure, is omitted, the device of the present invention is extremely durable. Also, because you can save the trouble of checking and repairing the advection valve,
The device of the present invention is extremely easy to maintain.

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

【図1】本発明の実施例に係る生物膜濾過装置の縦断面
図である。
FIG. 1 is a vertical cross-sectional view of a biofilm filtration device according to an embodiment of the present invention.

【図2】エジェクタ部分の断面図である。FIG. 2 is a sectional view of an ejector portion.

【図3】従来の生物膜濾過装置の系統図である。FIG. 3 is a system diagram of a conventional biofilm filtration device.

【符号の説明】[Explanation of symbols]

10 水槽 12 生物膜濾床 14 散気管 16 逆洗配管 18 逆洗ポンプ 20 移流管 22 原水供給管 26 排水管 28 排水弁 30 移流管 34 エジェクタ 36 作動水導入口 38 負圧吸引口 40 作動水流出口 42 エアリフトポンプ 10 Water Tank 12 Biofilm Filter Bed 14 Diffuser Pipe 16 Backwash Pipe 18 Backwash Pump 20 Advection Pipe 22 Raw Water Supply Pipe 26 Drain Pipe 28 Drain Valve 30 Advection Pipe 34 Ejector 36 Working Water Inlet 38 Negative Pressure Suction Port 40 Working Water Outlet 42 Air lift pump

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水槽と、該水槽内に設置された濾床と、
該濾床の下側に設けられた散気装置と、該水槽の下部か
ら水を抜き出すための移流管と、該移流管に接続された
逆洗水供給用配管と、を有する濾過装置において、 該移流管の途中にエジェクタを設け、前記逆洗水供給用
配管を該エジェクタの作動水導入口に接続し、該エジェ
クタの作動水流出口に前記移流管のうちエジェクタより
も上流側の部分を接続し、該エジェクタの負圧吸引口に
前記移流管のうちエジェクタよりも下流側の部分を接続
したことを特徴とする濾過装置。
1. A water tank, and a filter bed installed in the water tank,
In a filter device having an air diffuser provided on the lower side of the filter bed, an advection pipe for extracting water from the lower portion of the water tank, and a backwash water supply pipe connected to the advection pipe, An ejector is provided in the middle of the advection pipe, the backwash water supply pipe is connected to a working water inlet of the ejector, and a portion of the advection pipe upstream of the ejector is connected to a working water outlet of the ejector. The negative pressure suction port of the ejector is connected to a part of the advection pipe on the downstream side of the ejector.
JP13678392A 1992-05-28 1992-05-28 Filtration device Expired - Lifetime JP2679531B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13678392A JP2679531B2 (en) 1992-05-28 1992-05-28 Filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13678392A JP2679531B2 (en) 1992-05-28 1992-05-28 Filtration device

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JPH05329490A JPH05329490A (en) 1993-12-14
JP2679531B2 true JP2679531B2 (en) 1997-11-19

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JP4865997B2 (en) * 2004-10-22 2012-02-01 株式会社クボタ Operation method of sewage treatment apparatus and sewage treatment apparatus

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JPH07237Y2 (en) * 1989-04-11 1995-01-11 株式会社クボタ Sewage treatment equipment

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JPH05329490A (en) 1993-12-14

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