JPS6154214A - Method of washing filter - Google Patents

Method of washing filter

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Publication number
JPS6154214A
JPS6154214A JP59174264A JP17426484A JPS6154214A JP S6154214 A JPS6154214 A JP S6154214A JP 59174264 A JP59174264 A JP 59174264A JP 17426484 A JP17426484 A JP 17426484A JP S6154214 A JPS6154214 A JP S6154214A
Authority
JP
Japan
Prior art keywords
filter
water
washing
pipe
tank
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
JP59174264A
Other languages
Japanese (ja)
Inventor
Hiroshi Matsumoto
博 松本
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.)
Sasakura Engineering Co Ltd
Original Assignee
Sasakura Engineering Co 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 Sasakura Engineering Co Ltd filed Critical Sasakura Engineering Co Ltd
Priority to JP59174264A priority Critical patent/JPS6154214A/en
Publication of JPS6154214A publication Critical patent/JPS6154214A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To economically wash a filter without causing any trouble in blocking meshes of a strainer by reutilizing as washing water, the waste water obtd. by usual washing in the following step of back washing of the filter. CONSTITUTION:A washing step is commenced when resistance passing through the filter 1 increases due to blocking of the meshes. After stopping the operation, the waste water stored in a tank 3' in the preceding usual washing step is led to the filter 1 to back wash the filter 2 via a pump 14 and an inlet pipe 15 for the waste water using to back wash the filter member 2 whereby a solid deposited in the filter member 2 is discharged with water via a discharging pipe 7 followed by changing to the usual washing by passing raw water. The raw water is fed to the filter via the inlet pipe 13 to wash the filter member 2, and the waste water is stored in the tank 3' via the outlet pipe 10. After the filter member is stabilized or conditioned, a fluid flow is changed to the outlet pipe 11 followed by returning to the usual washing.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は逆浸透圧装置の前処理、その他一般の水処理に
通ずる濾過器の経済的洗浄方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an economical method for cleaning filters used in pretreatment of reverse osmosis devices and other general water treatments.

(従来の技術) 逆浸透圧装置はエネルギ消費量が少なく取扱いもwIR
であるなどの理由から、最近は海水地下水の淡水化、工
業用水の再生、ジュースの濃縮等に、大規模の装置から
小容量の装置に至るまで広く利用されてきているが、逆
浸透膜は原水中に存在する懸濁性固体、コロイド、その
他機生物、スライム発生等の各種の汚れによって分離性
能は低下する。特に懸濁性固体のうち、0.3〜5μm
位の懸濁粒子およびコロイドが最もトラブルを起こし易
いと云われているので、凝集剤を加えて大きな粒子とし
補足しやすくしたのち、砂濾過、珪藻土濾過、あるいは
精密フィルター等の濾過器によって濾過し、逆浸透圧装
置に供給している。このような処理は一般の濾過にも採
用されている。
(Conventional technology) Reverse osmosis devices consume less energy and are easy to handle.
For these reasons, reverse osmosis membranes have recently been widely used in both large-scale and small-capacity devices for desalination of seawater and groundwater, reclamation of industrial water, concentration of juice, etc. Separation performance deteriorates due to various types of contamination such as suspended solids, colloids, other organic organisms, and slime that are present in the raw water. Especially among suspended solids, 0.3 to 5 μm
It is said that small suspended particles and colloids are the most likely to cause trouble, so after adding a coagulant to make them larger particles and making them easier to capture, filter them using a filter such as sand filtration, diatomaceous earth filtration, or precision filter. , feeding the reverse osmosis device. Such processing is also used in general filtration.

濾過器は運転の経過に伴い次第に汚濁粒子が蓄積し、圧
力損失が大となるため、適宜洗浄を行って分離性能を回
復させている。
The filter gradually accumulates contaminant particles as it is operated, resulting in a large pressure loss, so it is washed as appropriate to restore separation performance.

濾過器洗浄方法の先行技術としては第2図及び第3図に
示すように特開昭59−42011号公報記載の方式が
あり、これでは逆浸透膜モジュール用前処理として使用
する濾過器の洗浄は、濾過器1の下端側から逆洗ブロア
Bによって空気を濾過器1内に送り込み、炉材2と内部
の水を攪拌混合し、炉材2から汚濁粒子を分離させ、次
いで第2図では高圧ポンプP2の入口側に設けられた中
間タンク3に貯留した濾過水を、第3図では逆浸透膜モ
ジュールRからの管4の濃縮水と中間タンク3から管5
を経て導入した濾過水との混合水をボーンプまたはエゼ
クタにより管6を通して洗浄用水として濾過器1に送り
、汚濁粒子と注入流体を濾過器上部の排出管7から排出
させている。このように濾過水を逆洗用水に使用すると
きは、逆浸透圧装置への原水の供給量を2〜3%増とす
る必要があり、濾過器の容量をその分だけ大形化しなけ
ればならず、給水用動力費も増大してコスト高となる欠
点がある。
As a prior art method for cleaning a filter, there is a method described in Japanese Patent Application Laid-open No. 59-42011, as shown in Figures 2 and 3. In Fig. 2, air is sent into the filter 1 from the lower end side of the filter 1 by a backwash blower B, the furnace material 2 and the water inside are stirred and mixed, and the pollutant particles are separated from the furnace material 2. In FIG. 3, the filtered water stored in the intermediate tank 3 provided on the inlet side of the high-pressure pump P2 is combined with the concentrated water in the pipe 4 from the reverse osmosis membrane module R and the pipe 5 from the intermediate tank 3.
The water mixed with the filtered water introduced through the filter is sent to the filter 1 as cleaning water through a pipe 6 by a bone pump or an ejector, and the pollutant particles and the injected fluid are discharged from a discharge pipe 7 at the top of the filter. When using filtered water for backwashing in this way, it is necessary to increase the amount of raw water supplied to the reverse osmosis device by 2 to 3%, and the capacity of the filter must be increased by that amount. However, there is a drawback that the power cost for water supply increases, resulting in high costs.

また第4図に示す別の先行技術では、濾過水ラインに中
間タンクを設けず、濾過器lの下方の逆洗洗浄用入口管
8と上方の通水洗浄管9とを設けて、逆洗は原水にて下
方の逆洗洗浄用入口管8より1日1回約10分間行い、
排水は上部排水管7より放出し、切替えて上方の通水洗
浄管9から原水を供給して下部の排出管10から外部へ
放出するが1、この通水洗浄を約1〜2時間行ったのち
切替えて濾過水取出管11より取出し正常運転に移行す
る。この洗浄方法は単に配管のみを設置すれば足りるの
で装置はwU単となる利点があるが、原水の汚れが甚だ
しい場合は濾過器下部のストレーナ12が目詰りする欠
点がある。
In another prior art shown in FIG. 4, an intermediate tank is not provided in the filtered water line, and an inlet pipe 8 for backwashing at the bottom of the filter l and a water passage washing pipe 9 at the top are provided for backwashing. This is done once a day for about 10 minutes using raw water from the lower backwashing inlet pipe 8.
Drainage water is discharged from the upper drain pipe 7, then raw water is supplied from the upper water washing pipe 9 and discharged to the outside from the lower discharge pipe 10.1 This water washing was carried out for about 1 to 2 hours. Afterwards, the filter is switched over and taken out from the filtered water take-out pipe 11, and normal operation begins. This cleaning method has the advantage of requiring only the piping to be installed, making the device simple, but has the disadvantage that the strainer 12 at the bottom of the filter can become clogged if the raw water is extremely contaminated.

なお前記のように通水洗浄水を放出することは、特にア
フリカ、中近東地域のように井戸水を原水として使用す
る内陸部においては原水自体置型であるので洗浄に使用
する水と云えども無駄にできないことより経済的な洗浄
方法でない欠点がある。
Furthermore, discharging the flushing water as mentioned above is especially important in inland areas where well water is used as raw water, such as in Africa and the Middle East, because the raw water itself is stationary, so even though the water is used for cleaning, it cannot be wasted. The drawback is that it is not a more economical cleaning method.

(発明が解決しようとする問題点) そこで本発明は、従来の濾過器洗浄方法において、系外
に捨てられていた通水洗浄排水は濾過器の炉材を通過し
ており、比較的清浄である点に着目し、この通水洗浄排
水を逆洗洗浄用水に再利用することにより前記先行技術
の各種欠点を解消することを目的とする。
(Problems to be Solved by the Invention) Therefore, in the conventional filter cleaning method, the water-washing wastewater that was discarded outside the system passes through the furnace material of the filter, making it relatively clean. Focusing on a certain point, the present invention aims to solve the various drawbacks of the prior art by reusing this water washing wastewater as water for backwashing.

(問題を解決するための手段) 本発明は濾過器の逆洗洗浄の後に行う通水洗浄の際に生
ずる排水をタンクに溜め、次回の逆洗洗浄水として再利
用することを特徴とするろ過器洗浄方法を提供するもの
である。
(Means for Solving the Problem) The present invention is a filtration system characterized by storing wastewater generated during water washing performed after backwashing of a filter in a tank and reusing it as water for next backwashing. The present invention provides a method for cleaning equipment.

(作用) 前記のように逆洗洗浄作業に引続いて行われる通水洗浄
の排水を一旦タンク類に貯め、この通水洗浄′排水を次
回の逆洗洗浄に利用することによって原水の増量を考慮
する必要はなく、動力費も節減できる効果があり、しか
もこの逆洗洗浄に使う通水洗浄排水は濾過器の炉材を通
過した水であるから目詰りした濾過器の逆洗洗浄に使用
しても何等支障はない。
(Function) As mentioned above, the amount of raw water can be increased by temporarily storing the wastewater from water washing that is carried out following backwashing work in tanks, and using this water washing wastewater for the next backwashing. There is no need to take this into account, and it has the effect of reducing power costs.Moreover, the water used for backwashing is water that has passed through the furnace material of the filter, so it can be used for backwashing clogged filters. There is no problem in doing so.

(実施例) 本発明の一実施例を第1図によって説明する。(Example) An embodiment of the present invention will be described with reference to FIG.

内部に砂層、珪藻土あるいはカートリッジ等の炉材2を
充虜した濾過器1は原水供給管13に連絡し、濾過水取
出管11が下部に設けられており、分岐した排出管10
にタンク3′が接続し、該タンク3′はポンプ14およ
び逆洗洗浄水入口管15を経て濾過器1に連絡されてお
り、上部に逆洗洗浄水排出管7が設けられている。
A filter 1, which is filled with a furnace material 2 such as a sand layer, diatomaceous earth, or a cartridge, is connected to a raw water supply pipe 13, and has a filtered water outlet pipe 11 at the bottom, and a branched discharge pipe 10.
A tank 3' is connected to the filter 1, and the tank 3' is connected to the filter 1 via a pump 14 and a backwash water inlet pipe 15, and a backwash water discharge pipe 7 is provided at the upper part.

上記のように構成した濾過器洗浄装置において、通常運
転時は、原水供給管13から導入された原水は濾過器l
に入り、炉材2を通過して固形物は除去され、濾過水は
取出管11より取出され次工程へ送出されるが、長時間
の運転によって濾過器lが目詰りして通過抵抗が大きく
なれば洗浄作業に入る。即ち先ず運転を停止し、前の洗
浄工程でタンク3′に貯留した通水洗浄排水をポンプ1
4、逆洗洗浄水入口管15を経て濾過器lに導入し、炉
材2を逆洗洗浄して、炉材2の間隙に沈積した固形物を
排出管7から水と共に放出する。この逆洗洗浄は1日1
回程度の頻度で行い約10分間行ったのち切替え、原水
供給管13から原水を供給して炉材2を通水洗浄し、排
水は排出管1oを経てタンク3′に貯留する。この通水
洗浄は約1〜2時間行い、これによって炉材2は安定す
るので洗浄は終了し、管路を取出管11に切替え、再び
正常運転へ復帰する。このようにタンク3′には通水洗
浄排水をその都度貯め次回の逆洗洗浄水として利用する
In the filter cleaning device configured as described above, during normal operation, raw water introduced from the raw water supply pipe 13 flows through the filter l.
The solid matter is removed by passing through the furnace material 2, and the filtered water is taken out from the take-out pipe 11 and sent to the next process, but the filter 1 becomes clogged due to long-term operation and the passage resistance becomes large. If so, start cleaning. That is, first, the operation is stopped, and the water flowing cleaning wastewater stored in the tank 3' from the previous cleaning process is transferred to the pump 1.
4. Backwash water is introduced into the filter l through the inlet pipe 15, backwashes the furnace material 2, and discharges the solid matter deposited in the gaps of the furnace material 2 from the discharge pipe 7 together with water. This backwash cleaning is done once a day.
The process is repeated once or twice for about 10 minutes, then switched, raw water is supplied from the raw water supply pipe 13, the furnace material 2 is flushed, and the waste water is stored in the tank 3' via the discharge pipe 1o. This water flushing is carried out for about 1 to 2 hours, and as the furnace material 2 becomes stable, the cleaning is completed, the pipe is switched to the outlet pipe 11, and normal operation is resumed. In this way, the tank 3' stores the flow-through cleaning wastewater each time and uses it as backwashing water for the next time.

(効果) 本発明は濾過器の逆洗洗浄の後に行う通水洗浄の際に生
ずる排水をタンク類に溜め、次回の逆洗洗浄水に使用す
る濾過器洗浄方法であるから、従来は無為に捨てられて
いた通水洗浄排水が逆洗洗浄に利用され、しかもこの逆
洗洗浄水は前回の逆洗洗浄工程の後に行われた通水洗浄
からの排水であるので、固形物は濾過されて比較的清浄
であり、再度逆洗洗浄に利用しても同等支障はなく、さ
らに先行技術に見られるような原水の汚れが激しい場合
における濾過器内のストレーナ−の目詰まりによるトラ
ブルはなく、また第2図第3図で説明したような原水を
増量し、これに伴って濾過器本体を大型にしなければな
らないと云った欠点もないので、頗る経済的な洗浄方法
が可能となり、この方法は逆/:j:’M圧方法の前処
理のみならず、一般の濾過器の洗浄にも広く利用でき、
特に内陸地方で不足勝ぢな井戸水を原水として使用する
場合に、貴重な水資源の無駄がなくなるなど、その効果
は大である。
(Effects) The present invention is a filter cleaning method in which the wastewater generated during water washing performed after backwashing the filter is stored in a tank and used as water for the next backwashing, so conventional methods are useless. Wastewater from flush washing that had been discarded is used for backwashing, and since this backwashing water is wastewater from flushing that was carried out after the previous backwashing process, solids are not filtered out. It is relatively clean and there is no problem even if it is used again for backwashing.Furthermore, there is no trouble caused by clogging of the strainer in the filter when the raw water is heavily contaminated as seen in the prior art. Since there is no disadvantage of increasing the amount of raw water and increasing the size of the filter body as explained in Fig. 2 and Fig. 3, a very economical cleaning method is possible, and this method is Reverse/:j:'M It can be widely used not only for pretreatment of the pressure method, but also for cleaning general filters.
This is particularly effective when using well water, which is in short supply in inland areas, as raw water, as it eliminates the waste of valuable water resources.

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

第1図は本発明の一実施例を示すフローシートであり、
第2図、第3図及び第4図は従来例におけるフローシー
トである。 ■・・・濾過器、     2・・・f材、3・・・中
間タンク、   3′・・・タンク、7・・・排水管、
    8・・・逆洗洗浄水入口管、9・・・通水洗浄
管、  10・・・排水管、11・・・濾過氷取出管、
12・・・下部ストレーナ−113・・・原水供給管、
 14・・・ポンプ、15・・・逆洗洗浄水入口管、 B・・・逆洗プロア、  R・・・逆浸透膜モジュール
。 特許出願人 株式会社 笹倉機械製作所第1 ―: −タ−
FIG. 1 is a flow sheet showing one embodiment of the present invention,
FIG. 2, FIG. 3, and FIG. 4 are flow sheets in the conventional example. ■...Filter, 2...F material, 3...Intermediate tank, 3'...Tank, 7...Drain pipe,
8... Backwash cleaning water inlet pipe, 9... Water flow cleaning pipe, 10... Drain pipe, 11... Filtered ice removal pipe,
12...Lower strainer-113...Raw water supply pipe,
14... Pump, 15... Backwash cleaning water inlet pipe, B... Backwash proa, R... Reverse osmosis membrane module. Patent applicant Sasakura Machinery Co., Ltd. No. 1 -: -tar-

Claims (1)

【特許請求の範囲】[Claims] ろ過器の逆洗洗浄の後に行う通水洗浄の際に生ずる排水
をタンク類に溜め、次回の逆洗洗浄水として再利用する
ことを特徴とするろ過器洗浄方法。
A filter cleaning method characterized by storing wastewater generated during water flow cleaning performed after backwashing the filter in a tank or the like and reusing it as water for the next backwash.
JP59174264A 1984-08-22 1984-08-22 Method of washing filter Pending JPS6154214A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59174264A JPS6154214A (en) 1984-08-22 1984-08-22 Method of washing filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59174264A JPS6154214A (en) 1984-08-22 1984-08-22 Method of washing filter

Publications (1)

Publication Number Publication Date
JPS6154214A true JPS6154214A (en) 1986-03-18

Family

ID=15975597

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59174264A Pending JPS6154214A (en) 1984-08-22 1984-08-22 Method of washing filter

Country Status (1)

Country Link
JP (1) JPS6154214A (en)

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