JP2002320827A - Solid-liquid separation equipment - Google Patents

Solid-liquid separation equipment

Info

Publication number
JP2002320827A
JP2002320827A JP2001127393A JP2001127393A JP2002320827A JP 2002320827 A JP2002320827 A JP 2002320827A JP 2001127393 A JP2001127393 A JP 2001127393A JP 2001127393 A JP2001127393 A JP 2001127393A JP 2002320827 A JP2002320827 A JP 2002320827A
Authority
JP
Japan
Prior art keywords
membrane
tank
water
membrane separation
solid
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
JP2001127393A
Other languages
Japanese (ja)
Inventor
Masaaki Yoshino
正章 吉野
Toshiki Nagasaka
俊樹 長坂
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.)
Maezawa Industries Inc
Original Assignee
Maezawa Industries Inc
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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP2001127393A priority Critical patent/JP2002320827A/en
Publication of JP2002320827A publication Critical patent/JP2002320827A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a solid-liquid separation equipment capable of continuously carrying out efficient solid-liquid separation operation while making good use of the advantages of a membrane separator having a washing nozzle. SOLUTION: A plurality of membrane separation vessels 12 each housing an immersion membrane module 13 and having a washing nozzle 18 which blows washing water on the filtration surface of the membrane module in the upper part of the vessel 12 are arranged in parallel behind a sedimentation tank 11 and each of the membrane separation vessels 12 and the sedimentation tank 11 are connected by a channel 23 with a water shutoff means 22.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、固液分離装置に関
し、詳しくは、浸漬型膜モジュールを収納した膜分離槽
の上方にろ過面洗浄用の洗浄ノズルを備えた膜分離槽の
前段に沈殿槽を有する固液分離装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid-liquid separation apparatus, and more particularly to a solid-liquid separation apparatus in which a sedimentation is provided at a stage preceding a membrane separation tank provided with a washing nozzle for washing a filtration surface above a membrane separation tank containing a submerged membrane module. The present invention relates to a solid-liquid separation device having a tank.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】近年の
ディスポーザの普及によって流入下水中の夾雑物質が増
加することが予想され、下水処理場においては、最終沈
殿池での浮上汚泥による二次処理水質の悪化が問題とな
っている。このため、最終沈殿池から流出した二次処理
水を更にろ過処理してから放流することが行われつつあ
る。
2. Description of the Related Art It is expected that contaminants in influent sewage will increase due to the recent spread of disposers. In a sewage treatment plant, secondary treatment by floating sludge in a final sedimentation basin is considered. Deterioration of water quality is a problem. For this reason, the secondary treatment water flowing out of the final sedimentation basin is being discharged after being further filtered.

【0003】二次処理水を処理する方式として、急速ろ
過法やマイクロストレーナーが一般に用いられている
が、これらは設置面積等の点に問題があり、この問題を
解決するためのろ過処理装置として、特開2000−6
2833号公報に記載された固液分離装置(膜分離装
置)が提案されている。
[0003] As a method for treating the secondary treated water, a rapid filtration method and a micro-strainer are generally used. However, these methods have problems in terms of an installation area and the like, and are used as filtration treatment devices for solving this problem. JP-A-2000-6
A solid-liquid separation device (membrane separation device) described in Japanese Patent No. 2833 has been proposed.

【0004】この膜分離装置は、浸漬型膜モジュールを
収納した固液分離槽(膜分離槽)の上方にろ過面洗浄用
の洗浄ノズルを設けたものであって、ろ過面の洗浄を効
率よく行うことができるので、膜モジュールの間隔を狭
めることが可能となって狭い設置面積でも十分なろ過面
積を得ることができ、ろ過速度にも優れるとともに、メ
ンテナンスも容易に行うことができるという利点を有し
ている。
In this membrane separation apparatus, a washing nozzle for washing a filtration surface is provided above a solid-liquid separation tank (membrane separation tank) accommodating an immersion type membrane module, so that the filtration surface can be efficiently washed. Since it is possible to reduce the distance between the membrane modules, it is possible to obtain a sufficient filtration area even with a small installation area, and it has an advantage that the filtration speed is excellent and the maintenance can be easily performed. Have.

【0005】しかし、洗浄ノズルで膜モジュールろ過面
の洗浄を行う際には、膜分離槽内の水を排出する必要が
あり、装置の規模によっては、この排水操作から洗浄操
作を経て再び膜分離槽内に注水してろ過操作を再開する
までに長時間を要することがあり、水処理効率を低下さ
せてしまうことがある。
However, when washing the filtration surface of the membrane module with the washing nozzle, it is necessary to discharge the water in the membrane separation tank, and depending on the scale of the apparatus, the membrane is separated from the drainage operation through the washing operation again. It may take a long time before water is injected into the tank and the filtration operation is restarted, and the water treatment efficiency may be reduced.

【0006】そこで本発明は、前記洗浄ノズルを有する
膜分離装置の利点を生かしながら、効率のよい固液分離
操作を連続して行うことができる固液分離装置を提供す
ることを目的としている。
Accordingly, an object of the present invention is to provide a solid-liquid separation device capable of continuously performing an efficient solid-liquid separation operation while taking advantage of the membrane separation device having the washing nozzle.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するた
め、本発明の固液分離装置は、浸漬型膜モジュールを収
納した膜分離槽の上方に前記膜モジュールのろ過面に向
けて洗浄水を噴出する洗浄ノズルを配置した膜分離槽
を、沈殿槽の後段に並列に複数配置するとともに、各膜
分離槽と沈殿槽とを、止水手段を備えた経路を介してそ
れぞれ接続したことを特徴としている。
In order to achieve the above-mentioned object, a solid-liquid separation device of the present invention is provided with washing water directed toward a filtration surface of a membrane module above a membrane separation tank containing a submerged membrane module. A plurality of membrane separation tanks each having a washing nozzle to be ejected are arranged in parallel at the subsequent stage of the settling tank, and each of the membrane separation tanks and the settling tank are connected to each other via a path provided with a water stopping means. And

【0008】[0008]

【発明の実施の形態】図1及び図2は、本発明の固液分
離装置の一形態例を示すもので、図1は水の流れを示す
系統図、図2は膜分離槽と沈殿槽との配置状態を示す概
略平面図である。この固液分離装置は、沈殿槽11の後
段に複数の膜分離槽12を並列に配置し、沈殿槽11で
沈殿処理した処理水を更に膜分離槽12で膜分離するよ
うに形成されている。
1 and 2 show an embodiment of a solid-liquid separation apparatus according to the present invention. FIG. 1 is a system diagram showing a flow of water, and FIG. 2 is a membrane separation tank and a sedimentation tank. FIG. 4 is a schematic plan view showing an arrangement state of FIG. This solid-liquid separation device is formed such that a plurality of membrane separation tanks 12 are arranged in parallel at the subsequent stage of the precipitation tank 11, and the treated water precipitated in the precipitation tank 11 is further subjected to membrane separation in the membrane separation tank 12. .

【0009】膜分離槽12は、微細目スクリーンやろ布
等の面状ろ過材を2枚向い合わせにしてその外周部を枠
材で密閉した複数の膜モジュール13をスペーサーによ
り所定間隔で保持して鉛直方向に配置したものであっ
て、膜モジュール13の側方の枠材の一部には通水口1
4が形成されており、膜モジュール13で固液分離処理
された膜処理水は、この通水口14から溢流室15の堰
をオーバーフローして経路16から処理水槽17に流下
するように形成されている。
The membrane separation tank 12 holds a plurality of membrane modules 13 having two planar filter materials, such as a fine mesh screen and a filter cloth, facing each other and sealing the outer periphery thereof with a frame material at predetermined intervals by spacers. It is arranged vertically, and a part of the frame material on the side of the membrane module 13
4 is formed, and the membrane treatment water subjected to the solid-liquid separation treatment in the membrane module 13 is formed so as to overflow the weir of the overflow chamber 15 from the water inlet 14 and flow down to the treatment water tank 17 from the path 16. ing.

【0010】また、膜分離槽12の上方には、膜モジュ
ール13の両面のろ過面に向けて洗浄水を噴出し、該洗
浄水によってろ過面の洗浄を行うための洗浄ノズル18
が設けられている。さらに、膜分離槽12の天板19に
は、排水時や注水時に開くエア抜きバルブ20が設けら
れ、底部には洗浄排水を排出するためのドレンバルブ2
1が設けられている。
[0010] Further, washing water is jetted toward the filtration surfaces on both sides of the membrane module 13 above the membrane separation tank 12, and a washing nozzle 18 for washing the filtration surface with the washing water.
Is provided. Further, the top plate 19 of the membrane separation tank 12 is provided with an air release valve 20 which opens when draining or pouring water, and a drain valve 2 for discharging washing drainage is provided at the bottom.
1 is provided.

【0011】上述のように形成された膜分離槽12は、
図2に示すように、前記沈殿槽11の後段に並列に複数
配置されており、各膜分離槽12と沈殿槽11とは、弁
等の止水手段22を備えた送水経路23を介してそれぞ
れ接続している。
The membrane separation tank 12 formed as described above is
As shown in FIG. 2, a plurality of the membrane separation tanks 12 and the sedimentation tanks 11 are arranged in parallel at the subsequent stage of the settling tanks 11. Each is connected.

【0012】固液分離処理を行う原水は、流入管31か
ら沈殿槽11内に流入して沈殿処理が行われる。槽底部
に沈殿した汚泥は排泥弁32から抜取られ、堰33を越
えた上澄水が前記送水経路23を通って各膜分離槽12
に流入する。膜分離槽12では、膜モジュール13によ
る膜分離処理が行われ、処理水が経路16から処理槽1
7に流出する。
The raw water to be subjected to the solid-liquid separation treatment flows from the inflow pipe 31 into the sedimentation tank 11, where the sedimentation treatment is performed. The sludge settled at the bottom of the tank is withdrawn from the drain valve 32, and the supernatant water that has passed through the weir 33 passes through the water supply path 23 to each of the membrane separation tanks 12.
Flows into. In the membrane separation tank 12, a membrane separation process is performed by the membrane module 13, and treated water flows from the path 16 through the treatment tank 1
Outflow to 7.

【0013】膜モジュール13の洗浄を行う際には、複
数の膜分離槽12の中の一つを選択して行う。まず、膜
洗浄を行う膜分離槽12に至る送水経路23の止水手段
22を作動させ、沈殿槽11からの流入水を遮断すると
ともに、該膜分離槽12のエア抜きバルブ20及びドレ
ンバルブ21を開いて槽内の水を排出する。続いて、洗
浄水ポンプ34を作動させるとともに、該膜分離槽12
に対応した洗浄弁35を開き、処理水槽17から該膜分
離槽12の洗浄ノズル18に洗浄水を供給する。
When cleaning the membrane module 13, one of the plurality of membrane separation tanks 12 is selected. First, the water stopping means 22 of the water supply path 23 leading to the membrane separation tank 12 for performing membrane cleaning is operated to shut off the inflow water from the sedimentation tank 11, and the air release valve 20 and the drain valve 21 of the membrane separation tank 12. To drain the water in the tank. Subsequently, the washing water pump 34 is operated and the membrane separation tank 12 is operated.
Is opened, and the cleaning water is supplied from the treatment water tank 17 to the cleaning nozzle 18 of the membrane separation tank 12.

【0014】これにより、該膜分離槽12に設置された
膜モジュール13のろ過面が、洗浄ノズル18から濾過
面に向かって噴出する洗浄水により洗浄され、洗浄排水
がドレンバルブ21を経て抜出される。また、必要に応
じて、図示しない薬液槽から薬液を洗浄ノズル18に供
給し、膜モジュール13を薬液で洗浄することもでき
る。
As a result, the filtration surface of the membrane module 13 installed in the membrane separation tank 12 is washed by the washing water spouting from the washing nozzle 18 toward the filtration surface, and the washing wastewater is drawn out through the drain valve 21. It is. Further, if necessary, a chemical solution can be supplied from a chemical solution tank (not shown) to the cleaning nozzle 18 to clean the membrane module 13 with the chemical solution.

【0015】膜モジュール13の洗浄が終了したら、洗
浄水ポンプ34を停止して洗浄弁35を閉じ、ドレンバ
ルブ21を閉じるとともに止水手段22を開放して沈殿
槽11から膜分離槽12内に水を流入させる。そして、
槽内の水位が所定高さになったときにエア抜きバルブ2
0を閉じると、沈殿槽11とのヘッド差によって膜モジ
ュール13での膜分離が再開する。
When the washing of the membrane module 13 is completed, the washing water pump 34 is stopped, the washing valve 35 is closed, the drain valve 21 is closed, and the water stopping means 22 is opened to move the washing water from the sedimentation tank 11 into the membrane separation tank 12. Allow water to flow in. And
When the water level in the tank reaches a predetermined height, the air release valve 2
When 0 is closed, membrane separation in the membrane module 13 resumes due to the head difference from the sedimentation tank 11.

【0016】このようにして一つの膜分離槽12に設置
した膜モジュール13の洗浄を終了したら、次の膜分離
槽12の膜洗浄を行うようにする。したがって、本形態
例に示すように、膜分離槽12を並列に5槽設けた場合
は、膜モジュール13を洗浄している以外の4槽で継続
して膜分離処理を行っている状態になるので、4槽の膜
分離槽12を基準にして水量等を設計することにより、
常に所定量の膜処理を行うことができる。
After the cleaning of the membrane module 13 installed in one membrane separation tank 12 is completed, the next membrane cleaning of the membrane separation tank 12 is performed. Therefore, as shown in this embodiment, when five membrane separation tanks 12 are provided in parallel, the membrane separation process is continuously performed in four tanks other than the membrane module 13 being washed. Therefore, by designing the amount of water and the like based on the four membrane separation tanks 12,
A predetermined amount of film processing can always be performed.

【0017】また、全体を一つの膜分離槽とした場合に
比べて、膜モジュール13を洗浄する際に排出する水量
及び膜分離処理再開のために流入させる水量が少なくて
すむので、膜モジュール13を洗浄する膜分離槽12の
休止時間を短くすることができる。
Further, compared with the case where the entire membrane is formed as one membrane separation tank, the amount of water discharged when cleaning the membrane module 13 and the amount of water introduced for restarting the membrane separation process can be reduced. The downtime of the membrane separation tank 12 that cleans the water can be shortened.

【0018】[0018]

【発明の効果】以上説明したように、本発明の固液分離
装置によれば、膜モジュールを洗浄する際にも膜分離に
よる固液分離処理を継続して行うことができ、効率のよ
い固液分離を行うことができる。
As described above, according to the solid-liquid separation apparatus of the present invention, the solid-liquid separation process by the membrane separation can be continuously performed even when the membrane module is washed, so that an efficient solid-liquid separation can be performed. Liquid separation can be performed.

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

【図1】 本発明の固液分離装置の一形態例を示す系統
図である。
FIG. 1 is a system diagram showing one embodiment of a solid-liquid separation device of the present invention.

【図2】 膜分離槽と沈殿槽との配置状態を示す概略平
面図である。
FIG. 2 is a schematic plan view showing an arrangement state of a membrane separation tank and a precipitation tank.

【符号の説明】[Explanation of symbols]

11…沈殿槽、12…膜分離槽、13…膜モジュール、
14…通水口、15…溢流室、16…経路、17…処理
水槽、18…洗浄ノズル、19…天板、20…エア抜き
バルブ、21…ドレンバルブ、22…止水手段、23…
送水経路、31…流入管、32…排泥弁、33…堰、3
4…洗浄水ポンプ、35…洗浄弁
11: sedimentation tank, 12: membrane separation tank, 13: membrane module,
14 ... water inlet, 15 ... overflow chamber, 16 ... route, 17 ... treated water tank, 18 ... washing nozzle, 19 ... top plate, 20 ... air release valve, 21 ... drain valve, 22 ... water stopping means, 23 ...
Water supply path, 31: Inflow pipe, 32: Drain valve, 33: Weir, 3
4: Cleaning water pump, 35: Cleaning valve

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 29/04 530A 29/38 510A ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) B01D 29/04 530A 29/38 510A

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 浸漬型膜モジュールを収納した膜分離槽
の上方に前記膜モジュールのろ過面に向けて洗浄水を噴
出する洗浄ノズルを配置した膜分離槽を、沈殿槽の後段
に並列に複数配置するとともに、各膜分離槽と沈殿槽と
を、止水手段を備えた経路を介してそれぞれ接続したこ
とを特徴とする固液分離装置。
1. A plurality of membrane separation tanks, each having a washing nozzle for jetting washing water toward a filtration surface of the membrane module disposed above a membrane separation tank containing an immersion type membrane module, are arranged in parallel at the subsequent stage of the settling tank. A solid-liquid separation device, wherein each of the membrane separation tanks and the sedimentation tank is arranged via a path provided with a water stopping means.
JP2001127393A 2001-04-25 2001-04-25 Solid-liquid separation equipment Pending JP2002320827A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001127393A JP2002320827A (en) 2001-04-25 2001-04-25 Solid-liquid separation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001127393A JP2002320827A (en) 2001-04-25 2001-04-25 Solid-liquid separation equipment

Publications (1)

Publication Number Publication Date
JP2002320827A true JP2002320827A (en) 2002-11-05

Family

ID=18976263

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001127393A Pending JP2002320827A (en) 2001-04-25 2001-04-25 Solid-liquid separation equipment

Country Status (1)

Country Link
JP (1) JP2002320827A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108355382A (en) * 2018-05-16 2018-08-03 贵州开磷集团矿肥有限责任公司 A kind of solid-liquid is from separator

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1157739A (en) * 1997-08-25 1999-03-02 Hitachi Ltd Water purifying method
JPH1170325A (en) * 1997-06-20 1999-03-16 Ngk Insulators Ltd Operating method for membrane filter
JP2000062833A (en) * 1998-08-20 2000-02-29 Maezawa Ind Inc Solid and liquid separating device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1170325A (en) * 1997-06-20 1999-03-16 Ngk Insulators Ltd Operating method for membrane filter
JPH1157739A (en) * 1997-08-25 1999-03-02 Hitachi Ltd Water purifying method
JP2000062833A (en) * 1998-08-20 2000-02-29 Maezawa Ind Inc Solid and liquid separating device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108355382A (en) * 2018-05-16 2018-08-03 贵州开磷集团矿肥有限责任公司 A kind of solid-liquid is from separator

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