JPS5831964B2 - How to clean the filter tank - Google Patents

How to clean the filter tank

Info

Publication number
JPS5831964B2
JPS5831964B2 JP51114300A JP11430076A JPS5831964B2 JP S5831964 B2 JPS5831964 B2 JP S5831964B2 JP 51114300 A JP51114300 A JP 51114300A JP 11430076 A JP11430076 A JP 11430076A JP S5831964 B2 JPS5831964 B2 JP S5831964B2
Authority
JP
Japan
Prior art keywords
cleaning
backwashing
material layer
air
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.)
Expired
Application number
JP51114300A
Other languages
Japanese (ja)
Other versions
JPS5339566A (en
Inventor
一男 小島
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.)
Ebara Corp
Original Assignee
Ebara Infilco 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 Ebara Infilco Co Ltd filed Critical Ebara Infilco Co Ltd
Priority to JP51114300A priority Critical patent/JPS5831964B2/en
Publication of JPS5339566A publication Critical patent/JPS5339566A/en
Publication of JPS5831964B2 publication Critical patent/JPS5831964B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、砂、アンスラサイトその他の粒状物をP材層
としたf過槽の洗浄方法特にP層を流動化して洗浄する
流動化逆洗に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for cleaning an F filter tank in which the P material layer is made of sand, anthracite, or other granular materials, particularly fluidized backwashing in which the P layer is fluidized and cleaned.

一般に、r過槽内に原水を導入し、粒状f材層を通過さ
せて清澄水を得る場合、時間の経過とともに原水中に含
まれる濁質がe材層に捕捉され、沢材抵抗が増加し1、
遂には沢過不能に至る。
Generally, when raw water is introduced into an r-filtration tank and passed through a granular f-material layer to obtain clear water, the turbidity contained in the raw water is captured in the e-material layer over time, increasing the swamp resistance. 1,
Eventually, it becomes impossible to overcome.

したがって、成る時間運転後はf材層の洗浄を行なわな
ければならなL・。
Therefore, the f-material layer must be cleaned after operation for a certain period of time.

上水道等の処理に使用されて℃・る砂e過槽を例にとれ
ば、戸材層の洗浄はp過時と反対に洗浄水を流す逆流洗
浄(逆流)とr材層表面の洗浄(表洗)によっており、
通常、逆洗水量は0.61’r?/lrt’” min
前後で、表洗水量は0.05〜0.2d/n?−min
である。
Taking as an example a sand filter tank used for water treatment, etc., the cleaning of the door material layer involves backflow cleaning (backflow), in which the washing water is run in the opposite direction to that used during the P period, and cleaning of the surface of the R material layer (surface cleaning). Washing)
Normally, the amount of backwash water is 0.61'r? /lrt'”min
Before and after, surface washing water amount is 0.05 to 0.2 d/n? -min
It is.

この逆洗は、砂層を流動化せしめて砂層内に捕捉されて
℃・る濁質を追(・出すためであるが、砂層を流動化す
るにはもつと少なち・逆洗水量で十分である。
The purpose of this backwashing is to fluidize the sand layer and remove the turbidity trapped within the sand layer, but the amount of backwash water is sufficient to fluidize the sand layer. be.

しかし、流動化した砂の上部に追(・出された濁質をさ
らに排水樋まで上昇させるためには、大きな上昇流速を
必要とするために逆洗水量は0.6m3/rr12・m
inと砂が流動化するよりも大きな値をとって℃・る。
However, in order to further raise the discharged turbidity to the upper part of the fluidized sand, a large upward flow velocity is required, so the amount of backwash water is 0.6 m3/rr12 m
℃・ru, which is larger than the temperature at which the sand becomes fluidized.

また、表洗は、圧力水を砂層表面に噴射し、砂粒同志の
衝突、摩擦をはかり、マットボールの発生を防止すると
ともに洗浄効果の助長をはるために行われるものである
Surface washing is performed by spraying pressurized water onto the surface of the sand layer to measure the collision and friction between sand grains, to prevent matte balls from occurring, and to enhance the cleaning effect.

さらに、従来、逆洗時に逆洗水と同時に沢材層下部から
空気を吹込み洗浄効果をあげることも行なわれて(・た
が、使用する空気圧は4mAq程度を必要とし、またそ
のためにf材が流出することも多かった。
Furthermore, conventionally, during backwashing, air was blown from the bottom of the swamp layer at the same time as backwash water to increase the cleaning effect. was often leaked.

本発明は、f材層の洗浄水量を極小にし、しかも洗浄効
果をあげる有用な洗浄方法を提供することを目的とする
ものである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a useful cleaning method that minimizes the amount of water used to clean the f-material layer and improves the cleaning effect.

本発明は粒状物をf材層とした沢過槽にお℃゛て、沢材
層を洗浄水により逆流洗浄するに際し、前記r材層の逆
流洗浄におけるr材膨張面より上に空気吹込管を配置さ
せ、前記逆流洗浄時にP材膨張面上に剥離された濁質を
前記空気吹込管から吹込まれた空気ならびに洗浄水によ
り移送し上部に設けた排水樋から排出することを特徴と
するf過槽の洗浄方法である。
The present invention provides an air blowing pipe which is installed above the expansion surface of the R material during backwashing of the R material layer in the backwashing of the slough material layer with washing water in a swell tank with granular materials as an F material layer. is arranged, and the suspended matter exfoliated on the expanded surface of the P material during the backwashing is transferred by the air and washing water blown from the air blowing pipe, and is discharged from the drain gutter provided at the upper part. This is a method of cleaning the tank.

この場合、逆洗水量としては0.3〜0.4n’?/7
?Z2・minで十分であり、さらにP材が流動化し膨
張した上部に空気を0.3〜0.577Z’/rr?
・m in吹き込む仁と□より、P°材の流動化した上
部では見掛は上、逆洗流速は0.7〜0.9m3/rr
?・minとなり、短時間に洗浄を完了させることがで
き、またマッドボールの発生を防止することもでき、さ
らに従来逆洗用に使用してL・た空気圧4mAq にく
らべて、本発明方法では逆洗時の膨張面上に吹き込むの
で0.5〜0.7mAqの圧力ですみ濾材の流出をなく
し安全な洗浄作業が可能となる。
In this case, the amount of backwash water is 0.3 to 0.4 n'? /7
? Z2・min is sufficient, and air is added to the upper part where the P material is fluidized and expanded at a rate of 0.3 to 0.577 Z'/rr?
・From the injection hole and □, the upper part of the fluidized P° material looks upward, and the backwash flow rate is 0.7 to 0.9 m3/rr.
?・Min, cleaning can be completed in a short time, and the generation of mud balls can be prevented.Furthermore, compared to the conventional backwashing method, which required an air pressure of 4 mAq, the method of the present invention can complete cleaning in a short time. Since it is blown onto the expanded surface during washing, a pressure of 0.5 to 0.7 mAq is sufficient, eliminating the outflow of the filter medium and allowing safe washing work.

なお前記空気の吹き込みは、沢材膨張面上に多孔管、ノ
ズル等により分散させ吹き込むようにする。
Note that the air is dispersedly blown onto the expanding surface of the swamp material using a porous pipe, a nozzle, or the like.

本発明の一実施例を図面を参照しつつ説明すれば、1は
濾過槽、2は洗浄水流入管、3は逆流洗浄におけるf材
膨張面より上に設けた空気吹込管、4は沢材層、5は排
水樋である。
An embodiment of the present invention will be described with reference to the drawings. 1 is a filtration tank, 2 is a washing water inflow pipe, 3 is an air blowing pipe provided above the expansion surface of the f-material in backwashing, and 4 is a spring material layer. , 5 is a drainage gutter.

このようなf過槽1にお(・て、P材層4が目詰りし、
た場合には、r過操作を停止し、P材層4の洗浄を行う
が、まず洗浄水流人管2から洗浄水を流入し、P材層4
を流動化させ、p材層4内に捕捉されて(・る濁質をは
くりさせ沢材膨張面上へ追(゛出す。
In such a f overtank 1, the P material layer 4 becomes clogged,
In this case, the overflow operation is stopped and the P material layer 4 is cleaned.
The suspended matter trapped in the p-material layer 4 is peeled off and expelled onto the expanding surface of the sludge.

この際、空気吹込管3がら空気を吹込み、空気と洗浄水
とによってP材膨張面上へ追ち・出された濁質を押し上
げ移送し、排水樋5から濁質は排出される。
At this time, air is blown through the air blowing pipe 3, and the air and washing water push up and transport the turbidity that has been pushed onto the expanding surface of the P material, and the turbidity is discharged from the drainage gutter 5.

本発明は粒状物をF材層とした濾過層にお(・て、沢材
層を洗浄水により逆流洗浄するに際し、この逆流洗浄に
よるP材膨張時に該膨張面上に空気を吹込むことにより
従来逆洗に必要とされてL・た逆洗水量以下の少L・量
で戸材同志の接触や衝突が多くなり濁質の分離を容易に
て洗浄効果をあげ、しかも逆洗水量を極小たらしめ、か
つ使用する空気圧も低くてすむ等工業上極めて有用なる
利点を有するものであり、逆流洗浄に関する諸元を著し
く合理的にでき経済的な濾過槽の設計をも可能にし、し
かも表面洗浄が併用される方式となるし、効果的な流動
化逆洗方式とすることが保証され運転経費も大巾に節減
できる有益な特長がある。
In the present invention, when the filtration layer is made of granular material as the F material layer, when the swamp material layer is backwashed with washing water, air is blown onto the expanded surface of the P material when the P material expands due to this backwashing. With a small amount of backwash water that is less than the amount of backwash water conventionally required for backwashing, contact and collision between door materials increases, turbidity can be easily separated, and the cleaning effect is increased, while the amount of backwash water is minimized. It has extremely useful advantages industrially, such as the fact that the air pressure used is low, and the specifications related to backwashing can be made extremely rational, making it possible to design an economical filtration tank. This method is used in combination with this method, and has the advantageous feature that it is guaranteed to be an effective fluidized backwash method and that operating costs can be greatly reduced.

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

図面は本発明の一実施例を示す縦断面図である。 1・・・濾過槽、2・・・洗浄水流入管、3・・・空気
吹込管、4・・・P材層、5・・・排水樋。
The drawing is a longitudinal sectional view showing an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Filter tank, 2... Washing water inflow pipe, 3... Air blowing pipe, 4... P material layer, 5... Drain gutter.

Claims (1)

【特許請求の範囲】 1 粒状物をP材層とした沢過槽におち・て、P材層を
洗浄水により逆流洗浄するに際し、前記P材層の逆流洗
浄における沢材膨張面より上に空気吹込管を配置させ、
前記逆流洗浄時に沢材膨張面上に剥離された濁質を前記
空気吹込管から吹込まれた空気ならびに洗浄水により移
送し上部に設けた排水樋から排出することを特徴とする
t過槽の洗浄方法。 2 前記沢材層の逆流洗浄のための逆洗水量を0.3〜
0.4rri’/rr?・minとして処理する特許請
求の範囲第1項記載のf過槽の洗浄方法。 3 前記p材膨張面上に吹き込む空気吹込量を0.3〜
0.577fl/?722・minとして処理する特許
請求の範囲第1項又は第2項記載の沢過槽の洗浄方法。 4 前記逆洗時に吹き込まれる空気が0.5〜0.7m
Aqの圧力で処理される特許請求の範囲第1項、第2項
又は第3項記載の沢過槽の洗浄方法。
[Scope of Claims] 1. When placing particulate matter in a slough tank with a P material layer and backwashing the P material layer with washing water, above the expansion surface of the swamp material during backwashing of the P material layer. Place the air blowing pipe,
Cleaning of a t-filter tank characterized in that during the backwashing, the suspended solids separated on the expanded surface of the swamp material are transferred by the air and cleaning water blown from the air blowing pipe and discharged from the drainage gutter provided at the upper part. Method. 2 The amount of backwash water for backwashing the swamp material layer is 0.3~
0.4rr'/rr?・The method for cleaning an f overtank according to claim 1, wherein the cleaning method is performed as min. 3 The amount of air blown onto the expanded surface of the p-material is 0.3~
0.577fl/? The cleaning method for a wastewater tank according to claim 1 or 2, wherein the cleaning method is performed at a rate of 722 min. 4 The air blown during the backwashing is 0.5 to 0.7 m.
A method for cleaning a slough tank according to claim 1, 2 or 3, wherein the cleaning method is carried out at a pressure of Aq.
JP51114300A 1976-09-22 1976-09-22 How to clean the filter tank Expired JPS5831964B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51114300A JPS5831964B2 (en) 1976-09-22 1976-09-22 How to clean the filter tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51114300A JPS5831964B2 (en) 1976-09-22 1976-09-22 How to clean the filter tank

Publications (2)

Publication Number Publication Date
JPS5339566A JPS5339566A (en) 1978-04-11
JPS5831964B2 true JPS5831964B2 (en) 1983-07-09

Family

ID=14634406

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51114300A Expired JPS5831964B2 (en) 1976-09-22 1976-09-22 How to clean the filter tank

Country Status (1)

Country Link
JP (1) JPS5831964B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2572301B1 (en) * 1984-10-29 1989-06-23 Degremont METHOD AND APPARATUS FOR FILTERING A SUSPENSION ON A GRANULAR FILTER LAYER

Also Published As

Publication number Publication date
JPS5339566A (en) 1978-04-11

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