JPH01155993A - Multimodule biomembrane filter device - Google Patents

Multimodule biomembrane filter device

Info

Publication number
JPH01155993A
JPH01155993A JP62312186A JP31218687A JPH01155993A JP H01155993 A JPH01155993 A JP H01155993A JP 62312186 A JP62312186 A JP 62312186A JP 31218687 A JP31218687 A JP 31218687A JP H01155993 A JPH01155993 A JP H01155993A
Authority
JP
Japan
Prior art keywords
multimodule
carriers
washing
module
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
Application number
JP62312186A
Other languages
Japanese (ja)
Inventor
Eiichi Sugiura
鋭一 杉浦
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP62312186A priority Critical patent/JPH01155993A/en
Publication of JPH01155993A publication Critical patent/JPH01155993A/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)

Abstract

PURPOSE:To enable the direct and easy installation of a membrane filter device to water channels of various shapes by forming a multimodule constituted by arranging cylindrical modules packed with carriers such as active carbon to a zigzag shape. CONSTITUTION:The cylindrical modules 12 packed with the carriers 3 such as active carbon, sand, glass or plastic balls are arranged and fixed zigzag to an inside wall 8 of a box body on the water bottom and the upper part thereof is fixed to a stay 10. The respective modules 2 are joined together to form the multimodule which can be freely installed to the existing water channels of various shapes. The surfaces of the multimodule are covered by filter cloths 4 to prevent outflow of the carriers 3 in the modules 2. Furthermore, annular washing units 5 for washing the surfaces of the filter cloths 4 are provided freely vertically movably. Washing water is sprayed from the washing nozzles 6 of the washing device units toward the respective modules 2 to wash the carriers 3 therein and is then discharged from the drain trough of the upper stage 10. The entire part of the multimodule is thus continuously backwashed.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、水道原水の生物膜濾過装置に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a biofilm filtration device for raw water.

[従来の技術] 水道の高普及時代を迎え、量の確保から水道水質の安全
性と良質で美味しい水の供給が求められている。特に汚
染の進んだ湖沼水を水道水源とする場合には、異臭味の
発生やトリハロメタンの生成等の問題が起こり、安全と
良質な水を確保することが困難な状況になっている。
[Prior Art] As we enter an era in which water supply is becoming more widespread, there is a need to ensure the quantity of tap water, ensure safe quality of tap water, and supply high-quality, delicious water. In particular, when highly polluted lake water is used as a tap water source, problems such as the generation of off-flavors and trihalomethanes occur, making it difficult to secure safe and high-quality water.

この対策としては、浄水システムの中に、前処理として
生物浄化法を用いること、或いは高度処理としてオゾン
、活性炭処理を行うこと等の方法が開発されている。中
でも生物浄化法はランニングコストが安価である点注目
されており、その方法には、現在ハエコームチューブ法
や、回転円板法、流動床法等とキャピラリー膜(中空糸
)を用いる担体による生物処理法等がある。
As a countermeasure against this problem, methods have been developed such as using a biological purification method as a pretreatment in a water purification system, or using ozone or activated carbon treatment as an advanced treatment. Among them, biological purification methods are attracting attention because of their low running costs, and current methods include the fly comb tube method, rotating disk method, fluidized bed method, and biological purification methods using carriers using capillary membranes (hollow fibers). There are processing methods etc.

これら現在行われている方法のうち、固定床式生物処理
設備の従来例を示す。
Among these currently used methods, a conventional example of a fixed bed biological treatment facility is shown below.

第4図は固定床法による下向流式生物処理設備の説明図
である。
FIG. 4 is an explanatory diagram of a downward flow type biological treatment facility using a fixed bed method.

図において、21は充填塔でその中に充填炉材22を充
填した充填床23が設けられている。また24は原水ポ
ンプ、25は逆洗用ポンプ、26は着水井、27は逆洗
用ブローワ27.28は流出管である。
In the figure, 21 denotes a packed column, in which a packed bed 23 filled with a packed furnace material 22 is provided. Further, 24 is a raw water pump, 25 is a backwash pump, 26 is a landing well, 27 is a backwash blower, and 27 is an outflow pipe.

これら第4図の固定床法による生物処理設備は、充填塔
21、原水ポンプ24、逆洗用ポンプ25、逆洗用ブロ
ーワ27から構成されており、充填塔21の塔内では藻
類の増殖を防止するための処置として遮光等の対策が取
られている。
The fixed bed biological treatment equipment shown in FIG. 4 is composed of a packed tower 21, a raw water pump 24, a backwashing pump 25, and a backwashing blower 27. Measures such as light shielding are being taken to prevent this.

原水の通水は、粒状充填P材22を充填した塔の上部か
ら下向流方式で行い、処理水は充填炉材22上面とほぼ
同じレベルに設定した流出管28から流出させる。充填
炉材22に捕捉された汚濁物質や余剰汚泥により、充填
塔21の濾過抵抗が増加し一定の水頭値に達するとバッ
チ式により逆洗を行う。
The raw water is passed in a downward flow manner from the upper part of the tower filled with the granular packed P material 22, and the treated water is discharged from the outflow pipe 28 set at approximately the same level as the top surface of the packed furnace material 22. The filtration resistance of the packed tower 21 increases due to the pollutants and excess sludge captured in the packed furnace material 22, and when a certain water head value is reached, backwashing is performed in a batch manner.

この方式では、バッチ式のために連続操業が出来ないか
若しくは処理量を増加する必要がある場合には充填塔を
多く設置する必要がある等の欠点がある。
This method has drawbacks such as the fact that continuous operation is not possible because it is a batch method, or it is necessary to install many packed towers when it is necessary to increase the throughput.

[発明の解決すべき問題点] ′  水道原水中には、主に有機物、藻の屑が含まれて
おり、且つ酸素濃度が高いので生物処理が行われるが、
この水道用浄水システムの主体は濾過である。
[Problems to be solved by the invention] ' Raw water from tap water mainly contains organic matter and algae debris, and has a high oxygen concentration, so biological treatment is performed.
The main body of this tap water purification system is filtration.

本発明は、以上の如き水道原水を処理するに当たって、
従来の生物処理方法における問題点を解決したマルチモ
ジュール生物膜濾過装置を提供することを目的とするも
のである。
In treating raw water from tap water as described above, the present invention provides the following features:
The object of the present invention is to provide a multi-module biofilm filtration device that solves the problems in conventional biological treatment methods.

[問題点を解決するための手段] 本発明は、活性炭、砂、硝子、プラスチック製玉等の担
体を充填した円筒状のモジュールを千鳥状に配列してな
るマルチモジュールを形成し、前記各モジュール表面を
濾布にて覆い、該各モジュールの濾布表面を洗浄するた
めのリング状の洗浄装置ユニットを上下可動に設けたこ
とを特徴とするマルチモジュール生物膜濾過装置である
[Means for Solving the Problems] The present invention forms a multi-module in which cylindrical modules filled with carriers such as activated carbon, sand, glass, plastic balls, etc. are arranged in a staggered manner, and each of the modules is arranged in a staggered manner. This is a multi-module biofilm filtration device characterized in that the surface is covered with a filter cloth and a ring-shaped cleaning device unit for cleaning the filter cloth surface of each module is vertically movable.

[作用] 本発明装置は、後述する実施例の第1図並びに第2図に
示す如く、活性炭、砂、硝子、プラスチック製玉等の担
体を充填した円筒状のモジュールを千鳥状に配列してマ
ルチモジュールを形成したので、種々の形の水流等に設
置し易く、またその7 /I/ fモジュール表面を濾
布にて覆いモジュール内の担体が流出することを防止し
、更に第2図に示すように、そのマルチモジュールの濾
布表面を洗浄するための上下可動の洗浄装置ユニットを
設けたので逆洗がし易く且つ連続的に逆洗排水を可能と
するものである。
[Function] As shown in FIGS. 1 and 2 of the embodiment described later, the device of the present invention has cylindrical modules filled with carriers such as activated carbon, sand, glass, and plastic beads arranged in a staggered manner. Since it is formed into a multi-module, it can be easily installed in various types of water streams, and the surface of the 7/I/f module is covered with a filter cloth to prevent the carrier inside the module from flowing out. As shown, a vertically movable cleaning device unit for cleaning the surface of the filter cloth of the multi-module is provided, making backwashing easy and allowing continuous backwashing and drainage.

更に、水道原水中には藻の含有が多いので、第3図に示
すような繊維を曲げ加工して小さな弾性体を作り、この
繊維を不織に成形した濾布を用いると空隙率が大きく通
水抵抗が小さく処理能力を大きくすることが出来るもの
である。
Furthermore, since raw water from tap water contains a lot of algae, it is possible to create a small elastic body by bending fibers as shown in Figure 3, and use a filter cloth made of non-woven fibers to increase the porosity. It has low water flow resistance and can increase processing capacity.

次に本発明の実施例について述べる。Next, examples of the present invention will be described.

[実施例コ 第1図及び第2図は本発明のマルチモジュール生物膜濾
過装置の説明図、第3図は濾布の説明図である。
[Example 1] Figures 1 and 2 are explanatory diagrams of a multi-module biofilm filtration device of the present invention, and Figure 3 is an explanatory diagram of a filter cloth.

図において、1はマルチモジュール、2はモジュール、
3は担体、4は濾布、5は洗浄装置ユニット、6は洗浄
ノズル、7は洗浄用伸縮管、8は躯体内壁、9は濾布繊
維、10はステージである。
In the figure, 1 is a multi-module, 2 is a module,
3 is a carrier, 4 is a filter cloth, 5 is a cleaning device unit, 6 is a cleaning nozzle, 7 is a cleaning telescopic tube, 8 is an inner wall of the body, 9 is a filter cloth fiber, and 10 is a stage.

まず本発明を第1図及び第2図にて説明する。First, the present invention will be explained with reference to FIGS. 1 and 2.

図示する如く、水流の中に活性炭、砂、硝子、プラスチ
ック製玉等(本実施例ではプラスチック製玉を用いた。
As shown in the figure, activated carbon, sand, glass, plastic balls, etc. (plastic balls were used in this example) were placed in the water stream.

)の担体3を充填した円筒状のモジュール2を水底の躯
体内壁8に千鳥状に配列して固定し、上部をステージ1
0に固定し、各モジュール2をあわせてマルチモジュー
ル1を形成する。
) Cylindrical modules 2 filled with carriers 3 are arranged and fixed in a staggered manner on the wall 8 of the frame at the bottom of the water, and the upper part is fixed to the stage 1.
0, and each module 2 is combined to form a multi-module 1.

またモジュール2の表面を濾布4にて覆いモジュール2
内の担体3が流出することを防止する。
In addition, the surface of the module 2 is covered with a filter cloth 4, and the module 2
This prevents the carrier 3 inside from flowing out.

この場合に用いるP布4は、通常用いられるものを用い
ても良いが、第3図に示す如き、曲げ加工された多数の
耐水性繊維であるポリ塩化ビニリデン繊維9を結合剤で
被覆結合し、三次元の網目模様の構造にして不織布に加
工した物を用いると空隙率が大きく通水抵抗が小さく処
理能力が大きくすることが出来る。
The P cloth 4 used in this case may be a commonly used one, but as shown in FIG. If a non-woven fabric with a three-dimensional mesh pattern structure is used, the porosity is large, the resistance to water flow is small, and the processing capacity can be increased.

濾布4を構成する前記繊維9の径は100デニールから
1000デニールのものが望ましく、この実施例では5
00デニールのものを使用した。
The diameter of the fibers 9 constituting the filter cloth 4 is preferably from 100 deniers to 1000 deniers, and in this embodiment, the diameter is 5 deniers.
00 denier was used.

モして濾布4の空隙率は93%になるように加工されて
いる。
The filter cloth 4 is processed to have a porosity of 93%.

更にそのマルチモジュール1の表面を洗浄するための洗
浄装置ユニット5を上部ステージ10に固設する。
Further, a cleaning device unit 5 for cleaning the surface of the multi-module 1 is fixedly installed on the upper stage 10.

ステージ10には洗浄装置ユニット5及び洗浄排水トラ
フ(図示なし)等を設ける。
The stage 10 is provided with a cleaning device unit 5, a cleaning drainage trough (not shown), and the like.

第2図に示す如く、洗浄装置ユニット5は、上下に伸縮
自在な洗浄用伸縮管7の先端にリング状の洗浄ノズル6
を取り付けたものである。
As shown in FIG. 2, the cleaning device unit 5 includes a ring-shaped cleaning nozzle 6 at the tip of a cleaning telescopic tube 7 that is vertically expandable.
is attached.

洗浄に当たっては、洗浄装置ユニット5を各モジュール
重錘に洗浄用伸縮管7を上下して移動し洗浄ノズル6よ
り洗浄水を洗浄用ポンプ(図示なし)を介して吹付は洗
浄する。洗浄ノズル6よりモジュール2内に吹込まれた
洗浄水は、担体3を洗浄し図示する如くモジュール2内
の上部に行き、上部ステージ10に設けた排水トラフよ
り排出される。
During cleaning, the cleaning device unit 5 is moved up and down the cleaning telescopic tube 7 using the weight of each module, and cleaning water is sprayed from the cleaning nozzle 6 via a cleaning pump (not shown) for cleaning. The cleaning water blown into the module 2 from the cleaning nozzle 6 cleans the carrier 3, goes to the upper part of the module 2 as shown in the figure, and is discharged from a drainage trough provided on the upper stage 10.

このように各モジュール2面毎に逆洗を行うことにより
、マルチモジュール1全体としては逆洗を連続的に行う
ものである。
By performing backwashing on two sides of each module in this way, the multi-module 1 as a whole is backwashed continuously.

更に、洗浄ノズル5にはシール性をよくするためにゴム
シールをまた走向性をよくするためにローラを取付ける
ことが好ましい。
Furthermore, it is preferable to attach a rubber seal to the cleaning nozzle 5 to improve sealing performance, and a roller to improve running properties.

本発明のマルチモジュール生物膜濾過装置は、このよう
に構成したことにより、逆洗がし易く、且つ逆洗排水ト
ラフ を別に設は逆洗排水を集約したので、逆洗排水と
処理水との混合も無く綺麗に処理することが出来る。
With the multi-module biofilm filtration device of the present invention configured in this way, backwashing is easy, and since the backwash wastewater is consolidated instead of having a separate backwash wastewater trough, the backwash wastewater and treated water can be easily combined. It can be processed cleanly without any mixing.

[発明の効果] 本発明のマルチモジュール生物膜濾過装置によれば、 (1)既設水路に随意に直接設置出来るので便利である
[Effects of the Invention] According to the multi-module biofilm filtration device of the present invention, (1) It is convenient because it can be directly installed in an existing waterway at will.

(2)連続逆洗が出来、処理水が綺麗である。(2) Continuous backwashing is possible and the treated water is clean.

(3)担体の流出が無くなる。(3) No outflow of carrier.

等の効果を奏するものである。It has the following effects.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図及び第2図は本発明のマルチモジュール生物膜が
過装置の説明図、第3図は沢布の説明図、第4図は固定
床法による下向流式生物処理設備の説明図である。 図において、1:マルチモジュール、2:モジニール、
3;担体、4:P布、5:洗浄装置ユニット、6:洗浄
ノズル、7:洗浄用伸縮管、8:躯体内壁、9:P布繊
維、10:ステージ、21:充填塔、22:充填P材、
23:充填床、24:原水ポンプ、25:逆洗用ポンプ
、26:着水井。 27:逆洗用ブローワ、28:流出管である。 尚各図中間−符号は同−又は相当部分を示す。
Figures 1 and 2 are explanatory diagrams of the multi-module biofilm filtering device of the present invention, Figure 3 is an explanatory diagram of Sawafu, and Figure 4 is an explanatory diagram of the downward flow biological treatment equipment using the fixed bed method. It is. In the figure, 1: Multi-module, 2: Modineal,
3: Carrier, 4: P cloth, 5: Cleaning equipment unit, 6: Cleaning nozzle, 7: Telescopic tube for cleaning, 8: Internal wall of frame, 9: P cloth fiber, 10: Stage, 21: Packed tower, 22: Filling P material,
23: Filled bed, 24: Raw water pump, 25: Backwash pump, 26: Water landing well. 27: Backwash blower, 28: Outflow pipe. Note that the reference numerals in the middle of each figure indicate the same or equivalent parts.

Claims (1)

【特許請求の範囲】[Claims] 担体を充填した円筒状のモジュールを千鳥状に配列して
なるマルチモジュールを形成し、前記各モジュール表面
を濾布にて覆い、該各モジュールの濾布表面を洗浄する
ためのリング状の洗浄装置ユニットを上下可動に設けた
ことを特徴とするマルチモジュール生物膜濾過装置。
A ring-shaped cleaning device for forming a multi-module formed by arranging cylindrical modules filled with carriers in a staggered manner, covering the surface of each module with a filter cloth, and cleaning the surface of the filter cloth of each module. A multi-module biofilm filtration device characterized by a unit that is movable up and down.
JP62312186A 1987-12-11 1987-12-11 Multimodule biomembrane filter device Pending JPH01155993A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62312186A JPH01155993A (en) 1987-12-11 1987-12-11 Multimodule biomembrane filter device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62312186A JPH01155993A (en) 1987-12-11 1987-12-11 Multimodule biomembrane filter device

Publications (1)

Publication Number Publication Date
JPH01155993A true JPH01155993A (en) 1989-06-19

Family

ID=18026253

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62312186A Pending JPH01155993A (en) 1987-12-11 1987-12-11 Multimodule biomembrane filter device

Country Status (1)

Country Link
JP (1) JPH01155993A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6086769A (en) * 1996-09-16 2000-07-11 Commodore Separation Technologies, Inc. Supported liquid membrane separation
CN107344761A (en) * 2017-08-25 2017-11-14 扬州大学 A kind of non-point source water quality decontamination of biological reactor designed based on function and volume modular and preparation method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6086769A (en) * 1996-09-16 2000-07-11 Commodore Separation Technologies, Inc. Supported liquid membrane separation
US6096217A (en) * 1996-09-16 2000-08-01 Lockheed Martin Energy Research Corporation Supported liquid membrane separation
CN107344761A (en) * 2017-08-25 2017-11-14 扬州大学 A kind of non-point source water quality decontamination of biological reactor designed based on function and volume modular and preparation method thereof

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