JPWO2009116479A1 - Water treatment equipment water supply pipe cleaning method - Google Patents

Water treatment equipment water supply pipe cleaning method Download PDF

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JPWO2009116479A1
JPWO2009116479A1 JP2009512341A JP2009512341A JPWO2009116479A1 JP WO2009116479 A1 JPWO2009116479 A1 JP WO2009116479A1 JP 2009512341 A JP2009512341 A JP 2009512341A JP 2009512341 A JP2009512341 A JP 2009512341A JP WO2009116479 A1 JPWO2009116479 A1 JP WO2009116479A1
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water
pipe
air
backwash
cleaning
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JP5321450B2 (en
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織田 信博
信博 織田
三輪 昌之
昌之 三輪
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Kurita Water Industries Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00Cleaning hollow articles by methods or apparatus specially adapted thereto 
    • B08B9/02Cleaning pipes or tubes or systems of pipes or tubes
    • B08B9/027Cleaning the internal surfaces; Removal of blockages
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • C02F1/004Processes for the treatment of water whereby the filtration technique is of importance using large scale industrial sized filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/006Water distributors either inside a treatment tank or directing the water to several treatment tanks; Water treatment plants incorporating these distributors, with or without chemical or biological tanks
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/74Treatment of water, waste water, or sewage by oxidation with air
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • C02F2001/425Treatment of water, waste water, or sewage by ion-exchange using cation exchangers
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/38Gas flow rate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters

Abstract

濾過器の給水配管を十分に洗浄し、微生物が増殖しやすい有機物含有水の濾過に用いる濾過器であっても、長期にわたり安定に濾過を継続することを可能とする水処理装置給水配管の洗浄方法。空気注入配管(16)より、給水配管(12)に圧縮空気を注入し、原水と空気との気液混合水を給水配管(12)に流して空気洗浄し、洗浄排水を配管(17)より排出する。その後、常法に従って逆洗を行う。空気洗浄時に洗浄できない配管(13)部分を、空気洗浄後の逆洗で洗浄する。Washing the water supply piping of the water treatment device that allows the water supply piping of the filter to be washed sufficiently and enables filtration to continue for a long period of time, even if it is a filter used to filter organic-containing water that is prone to microbial growth Method. Compressed air is injected into the water supply pipe (12) from the air injection pipe (16), and a gas-liquid mixed water of raw water and air is supplied to the water supply pipe (12) for air cleaning, and cleaning wastewater is supplied from the pipe (17). Discharge. Then, backwashing is performed according to a conventional method. The portion of the pipe (13) that cannot be cleaned during air cleaning is cleaned by backwashing after air cleaning.

Description

発明の分野Field of Invention

本発明は、水処理装置給水配管の洗浄方法に係り、特に、有機物を多く含み、微生物が増殖し易い有機物含有水を濾過処理する濾過装置等の水処理装置給水配管を効率的に洗浄する方法に関する。  The present invention relates to a method for cleaning a water treatment apparatus water supply pipe, and in particular, a method for efficiently washing a water treatment apparatus water supply pipe such as a filtration apparatus for filtering organic substance-containing water that contains a large amount of organic matter and easily proliferates with microorganisms. About.

発明の技術Invention of the invention

濾過装置は、濾過器内に砂、アンスラサイト等の濾材を充填して形成した濾床に、SS等の不純物を捕捉して除去するものであり、濾過装置の運転は、通常、濾過原水を通水して処理水を得る濾過運転と、濾過器に逆洗水を導入して濾床に捕捉されたSS等を排出させる逆洗とが交互に行われる(例えば、特許文献1)。  The filtration device captures and removes impurities such as SS from the filter bed formed by filling the filter with sand, anthracite, and other filter media. A filtration operation in which treated water is obtained by passing water and backwashing in which backwashing water is introduced into the filter and SS or the like captured by the filter bed is discharged are alternately performed (for example, Patent Document 1).

このような濾過装置で、有機物を多く含み、微生物が増殖し易い原水を濾過処理する場合、原水中に含まれて濾床で捕捉された微生物や、濾床で増殖した微生物は、逆洗により洗浄除去される。  When filtering raw water that contains a lot of organic matter and easily proliferates with such a filtration device, microorganisms contained in the raw water and captured in the filter bed, or microorganisms grown in the filter bed, should be washed back. Washed away.

しかし、原水槽から濾過器までの原水の給水配管に付着、増殖した微生物は、逆洗により洗浄除去されることなく、経時により微生物が増殖する結果、給水配管が閉塞したり、配管に付着した微生物が塊となって濾過器に流入したりする。配管の閉塞自体も重大な問題であるが、配管から剥離した微生物の塊が濾過器に流入した場合、その比重が濾材と近いため、通常の逆洗によって排出することは困難である。そして、濾過器に蓄積した微生物が生産する粘性物質と濾材とでマッドボールを形成する結果、濾床の閉塞や濾材のショートパスにより濾過性能の低下を引き起こす。  However, the microorganisms that have grown and adhered to the raw water supply pipe from the raw water tank to the filter are not washed away by backwashing, but as a result of the microorganisms growing over time, the water supply pipe is blocked or attached to the pipe. Microorganisms clump into the filter. The clogging of the pipe itself is also a serious problem, but when a microbial mass separated from the pipe flows into the filter, it is difficult to discharge by normal backwashing because its specific gravity is close to that of the filter medium. Then, as a result of forming a mud ball with the viscous material produced by the microorganisms accumulated in the filter and the filter medium, the filter performance is reduced due to the clogging of the filter bed and the short path of the filter medium.

これらの問題を解決するため、従来、殺菌効果を持つ薬剤を原水に注入して微生物の増殖を防ぐことが広く行われていた。さらに、定期的な保守作業として、配管洗浄、濾過器の濾材交換が行れている。
特許第3460324号公報
In order to solve these problems, conventionally, it has been widely practiced to prevent the growth of microorganisms by injecting a drug having a bactericidal effect into raw water. Furthermore, pipe maintenance and filter media replacement are performed as regular maintenance work.
Japanese Patent No. 3460324

従来の薬剤による殺菌では、薬品の注入量調整、補充等、煩雑な日常作業が必要である;有害な薬品を取り扱うため、作業環境面で好ましくない;薬品コストがかかり、特に処理する水量が多くなると薬剤費も高騰する;濾過処理水に薬剤が混入するおそれがあるため、濾過処理水を利用する場合は薬剤を除去する手段を設けるか、或いは薬剤洗浄後に大量の水でリンス洗浄する必要がある;といった問題があり、実用上好ましくない。  Conventional sterilization with chemicals requires complicated daily work, such as adjusting and replenishing the amount of chemicals to be injected; handling harmful chemicals is undesirable in terms of the work environment; requires chemical costs, especially the amount of water to be treated is large Then, the cost of chemicals also rises; there is a possibility that chemicals may be mixed into the filtered water, so when using the filtered water, it is necessary to provide a means for removing the chemicals or to rinse with a large amount of water after chemical cleaning. There is a problem that there is;

また、定期的な保守作業としての配管洗浄や濾過器の濾材交換では、濾過装置の運転を停止する必要があるため、運転効率の面で好ましくない。また、そのための作業量や濾材コストが問題となる。  In addition, pipe cleaning and replacement of filter media as periodic maintenance operations are not preferable in terms of operating efficiency because it is necessary to stop the operation of the filtration device. In addition, the amount of work and the cost of the filter medium are problematic.

従って、このような薬品による殺菌や、濾過装置の運転を停止しての保守作業によることなく、濾過器の給水配管を洗浄する方法が望まれる。  Therefore, there is a demand for a method of cleaning the water supply piping of the filter without sterilization with such chemicals or maintenance work with the operation of the filtration device stopped.

なお、特許文献1に記載される方法は、空気逆洗と、アルカリ及び/又は酸による逆洗とを組み合わせて行うものであり、アルカリ及び/又は酸が必要となる上に、逆洗水は濾過器内を逆流方向に流れて濾過器から排出されるため、やはり給水配管を洗浄することはできない。  In addition, the method described in Patent Document 1 is a combination of backwashing with air and backwashing with an alkali and / or acid. In addition to the need for alkali and / or acid, backwashing water is Since the water flows in the reverse direction in the filter and is discharged from the filter, the water supply pipe cannot be washed.

上述した給水配管の洗浄に関する問題は、濾過装置に限らず、イオン交換器や軟水器、更には活性炭塔のように、実用上、内部のイオン交換樹脂や活性炭などの水処理材により濾過機能が奏され、定期的に又は必要に応じて逆洗が行われる装置すべてに共通する問題である。  The above-mentioned problems related to cleaning of water supply pipes are not limited to filtration devices, and practically, the filtration function is provided by water treatment materials such as ion exchange resins and activated carbon, such as ion exchangers, water softeners, and activated carbon towers. It is a problem common to all devices that are played and backwashed regularly or as needed.

本発明は上記従来の問題点を解決し、濾過装置等の水処理装置の給水配管を十分に洗浄することができ、微生物が増殖しやすい有機物含有水の処理に用いた場合であっても、長期にわたり安定に処理を継続することを可能とする水処理装置給水配管の洗浄方法を提供することを目的とする。  The present invention solves the above-mentioned conventional problems, can sufficiently wash the water supply piping of a water treatment device such as a filtration device, and even when used for treatment of organic matter-containing water in which microorganisms are likely to grow, It is an object of the present invention to provide a water treatment apparatus water supply pipe cleaning method capable of stably continuing treatment over a long period of time.

本発明(請求項1)の水処理装置給水配管の洗浄方法は、内部に水処理材が充填され、定期的又は必要に応じて逆洗が行われる水処理装置本体と、該水処理装置本体に原水を供給する給水配管と、該水処理装置本体から処理水を取り出す処理水配管と、該水処理装置本体に逆洗水を供給する逆洗水配管と、逆洗排水を系外へ排出する該給水配管に接続された逆洗排水配管とを有する水処理装置の該給水配管を洗浄する方法において、該逆洗排水配管と該給水配管との該接続部よりも上流側に空気混合水を供給し、この空気混合水を、前記接続部を経て前記逆洗排水配管から排出する空気洗浄工程と、その後、該水処理装置本体に逆洗水を供給し、該水処理装置本体からの逆洗排水を、前記接続部を経て前記逆洗排水配管から排出する逆洗工程とによって該給水配管を洗浄することを特徴とする  The water treatment apparatus water supply pipe cleaning method of the present invention (Claim 1) includes a water treatment apparatus main body filled with a water treatment material and backwashed periodically or as necessary, and the water treatment apparatus main body. Water supply pipe for supplying raw water to the main body, treated water pipe for extracting treated water from the main body of the water treatment apparatus, backwash water pipe for supplying backwash water to the main body of the water treatment apparatus, and discharge of backwash wastewater to the outside of the system In the method of cleaning the water supply pipe of the water treatment apparatus having the backwash drainage pipe connected to the water supply pipe, the air mixed water is located upstream of the connection portion between the backwash drainage pipe and the water supply pipe. An air washing step of discharging the mixed water from the backwash drainage pipe through the connecting portion, and then supplying backwash water to the water treatment device main body. Backwashing process for discharging backwashing drainage from the backwashing drainage pipe through the connecting portion. Characterized by washing the water supply pipe by

本発明においては、前記空気洗浄工程における前記給水配管への空気注入量を、該給水配管の断面積1cm当たり4〜10L/minであり、該空気洗浄工程の洗浄時間を、下記式(I)で算出される基準時間T(分)の3倍以上とすることができる(請求項2)。
T={S×L×0.001/W} …(I)
(ただし、Sは給水配管の断面積(cm)、Lは空気混合水が流れる給水配管の長さ(cm)、Wは洗浄時の通水量(L/min)である。)
In the present invention, the amount of air injected into the water supply pipe in the air cleaning step is 4 to 10 L / min per 1 cm 2 of the cross-sectional area of the water supply pipe, and the cleaning time of the air cleaning process is expressed by the following formula (I 3) or more than the reference time T (minutes) calculated in (2).
T = {S × L × 0.001 / W} (I)
(However, S is the cross-sectional area (cm 2 ) of the water supply pipe, L is the length (cm) of the water supply pipe through which the air-mixed water flows, and W is the water flow rate (L / min) during cleaning.)

また、前記逆洗工程後に、前記給水配管を介して前記水処理装置本体に原水を供給し、該水処理装置本体からの流出水を系外に排出する仕上げ洗浄工程を行ってもよい(請求項3)。  Further, after the backwashing step, a final cleaning step of supplying raw water to the water treatment device main body through the water supply pipe and discharging outflow water from the water treatment device main body out of the system may be performed. Item 3).

また、更に、処理水配管に空気混合水を供給して系外へ排出する処理水配管空気洗浄工程を行ってもよい(請求項4)。  Furthermore, you may perform the process water piping air washing | cleaning process which supplies mixed water to a treated water piping, and discharges | emits out of the system (Claim 4).

また、処理水配管からの処理水を貯留する処理水槽と、この処理水槽内の処理水を逆洗水として水処理装置本体に供給する逆洗水配管とを有する場合において、逆洗工程に先立ち、逆洗水配管に空気混合水を供給して系外へ排出する逆洗水配管空気洗浄工程を行ってもよく(請求項5)、この場合において、逆洗水配管が水処理装置本体の処理水排出口近傍で処理水配管に接続された構造とされている装置であれば、空気混合水を逆洗水配管から、逆洗水配管と処理水配管との接続部を経て処理水配管に処理水流通方向に通水させた後系外へ排出する逆洗水配管及び処理水配管空気洗浄工程を行ってもよい(請求項6)。  Further, in the case of having a treated water tank for storing treated water from the treated water pipe and a backwash water pipe for supplying treated water in the treated water tank as backwash water to the water treatment device main body, prior to the backwash process. Further, a backwash water pipe air washing step of supplying air mixed water to the backwash water pipe and discharging it outside the system may be performed (Claim 5). In this case, the backwash water pipe is connected to the water treatment device main body. If the device is structured to be connected to the treated water pipe in the vicinity of the treated water discharge port, the mixed water is supplied from the backwash water pipe to the treated water pipe through the connection between the backwash water pipe and the treated water pipe. In addition, a backwash water pipe and a treated water pipe air washing step for discharging water to the outside of the system after passing the water in the treated water flow direction may be performed.

本発明において、水処理装置本体としては、次のようなものが挙げられる(請求項7〜10)。
(1) 内部に水処理材として濾材が充填された濾過器
(2) 内部に水処理材としてイオン交換樹脂が充填されたイオン交換塔
(3) 内部に水処理材としてイオン交換樹脂が充填された軟水器
(4) 内部に水処理材として活性炭が充填された活性炭塔
In the present invention, the water treatment apparatus main body includes the following (claims 7 to 10).
(1) Filter with a filter medium filled as a water treatment material
(2) Ion exchange tower filled with ion exchange resin as water treatment material
(3) Water softener filled with ion exchange resin as water treatment material
(4) Activated carbon tower filled with activated carbon as water treatment material

このような本発明の水処理装置給水配管の洗浄方法は、例えば、有機物含有水を原水とする水処理装置の給水配管の洗浄に適用することができる(請求項11)。  Such a water treatment apparatus water supply pipe cleaning method of the present invention can be applied to, for example, cleaning of a water supply pipe of a water treatment apparatus using organic substance-containing water as raw water (claim 11).

本発明の水処理装置給水配管の洗浄方法では、空気洗浄工程において、給水配管の逆洗排水配管の接続部よりも上流側を空気混合水で洗浄して、配管内壁等に付着している微生物等の汚染物質を効率的に剥離洗浄して、逆洗排水配管から系外へ排出することができる。この空気洗浄工程においては、空気混合水は、給水配管の逆洗排水配管の接続部までしか流れず、この接続部から水処理装置本体までの給水配管は洗浄されない。この接続部から水処理装置本体までの配管長さは短く、この部分の洗浄の必要性は低いが、空気洗浄時に剥離された微生物等の不純物が、この部分に流入し、更には水処理装置本体に流入する恐れがある。  In the water treatment apparatus water supply pipe cleaning method according to the present invention, in the air cleaning process, the upstream side of the connection part of the backwash drainage pipe of the water supply pipe is washed with air mixed water and adhered to the inner wall of the pipe It is possible to efficiently remove and wash contaminants such as the like and discharge them from the backwash drainage pipe outside the system. In this air cleaning process, the air-mixed water flows only to the connection part of the backwash drainage pipe of the water supply pipe, and the water supply pipe from this connection part to the water treatment apparatus main body is not cleaned. The length of the pipe from this connection part to the main body of the water treatment device is short, and the necessity for washing of this part is low, but impurities such as microorganisms peeled off during air washing flow into this part, and further the water treatment apparatus There is a risk of flowing into the body.

本発明では、この空気洗浄工程後に、該水処理装置本体に逆洗水を供給し、該水処理装置本体からの逆洗排水を、前記接続部を経て前記逆洗排水配管から排出する逆洗工程を行うことにより、この濾過器本体と前記接続部との間の給水配管や水処理装置本体内を洗浄することができ、空気洗浄時に当該部分に剥離された微生物等の汚染物質が流入しても、これを効果的に逆洗排水配管を経て系外へ排出することができる。  In the present invention, after this air cleaning step, backwash water is supplied to the water treatment device main body, and the backwash drainage from the water treatment device main body is discharged from the backwash drainage pipe through the connecting portion. By performing the process, the water supply pipe between the filter body and the connection part and the inside of the water treatment apparatus body can be washed, and contaminants such as microorganisms separated into the part flow into the part during air washing. However, this can be effectively discharged out of the system through the backwash drainage pipe.

本発明において、空気洗浄工程における前記給水配管への空気注入量は、給水配管の断面積1cm当たり4〜10L/minで、空気洗浄工程の洗浄時間は、下記式(I)で算出される基準時間T(分)の3倍以上とすると、より一層効率的な洗浄を行って、高い洗浄効果を得ることができる(請求項2)。
T={S×L×0.001/W} …(I)
(ただし、Sは給水配管の断面積(cm)、Lは空気混合水が流れる給水配管の長さ(cm)、Wは洗浄時の通水量(L/min)である。)
In the present invention, the amount of air injected into the water supply pipe in the air cleaning step is 4 to 10 L / min per 1 cm 2 of the cross-sectional area of the water supply pipe, and the cleaning time in the air cleaning process is calculated by the following formula (I). When the reference time T (min) is 3 times or more, more efficient cleaning can be performed and a high cleaning effect can be obtained (claim 2).
T = {S × L × 0.001 / W} (I)
(However, S is the cross-sectional area (cm 2 ) of the water supply pipe, L is the length (cm) of the water supply pipe through which the air-mixed water flows, and W is the water flow rate (L / min) during cleaning.)

また、逆洗工程後に、水処理装置本体に給水配管を介して原水を供給して水処理装置本体からの流出水を系外へ排出する仕上げ洗浄工程を行うことにより、洗浄後の運転再開時に高水質の処理水を得ることができる(請求項3)。  In addition, after the backwash process, by performing a final cleaning process in which raw water is supplied to the main body of the water treatment apparatus via the water supply pipe and the effluent water from the main body of the water treatment apparatus is discharged out of the system, High-quality treated water can be obtained (claim 3).

また、定期的に又は必要に応じて更に、処理水配管に空気混合水を供給して系外へ排出する処理水配管空気洗浄工程を行うことにより、処理水配管における微生物等の汚染物質の剥離洗浄を行える(請求項4)。  In addition, the treatment water pipe air washing process that supplies air mixture water to the treatment water pipe and discharges it outside the system periodically or as needed further removes contaminants such as microorganisms in the treatment water pipe. Cleaning can be performed (Claim 4).

また、処理水配管からの処理水を貯留する処理水槽と、この処理水槽内の処理水を逆洗水として水処理装置本体に供給する逆洗水配管とを有する場合において、逆洗工程に先立ち、逆洗水配管に空気混合水を供給して系外へ排出する逆洗水配管空気洗浄工程を行うことにより、逆洗水配管における微生物等の汚染物質の剥離洗浄を行って、逆洗水配管内の汚染物質が、逆洗工程において水処理装置本体内に逆洗水と共に流入することを防止することができる(請求項5)。  Further, in the case of having a treated water tank for storing treated water from the treated water pipe and a backwash water pipe for supplying treated water in the treated water tank as backwash water to the water treatment device main body, prior to the backwash process. The backwash water pipe supplies air mixed water to the backwash water pipe and discharges it outside the system. Contaminants in the pipe can be prevented from flowing into the water treatment apparatus main body together with the backwash water in the backwash process (Claim 5).

この逆洗水配管の洗浄工程において、空気混合水を逆洗水配管から処理水配管と逆洗水配管との接続部を経て処理水配管に通水させた後系外へ排出することにより、逆洗水配管と共に、処理水配管をも洗浄することができる(請求項6)。  In the washing process of the backwash water pipe, the air mixed water is passed from the backwash water pipe to the treated water pipe through the connecting portion of the treated water pipe and the backwash water pipe, and then discharged out of the system. The treated water pipe can be washed together with the backwash water pipe (Claim 6).

本発明の水処理装置給水配管の洗浄方法の実施の形態を示す濾過装置の系統図である。It is a systematic diagram of the filtration apparatus which shows embodiment of the washing | cleaning method of the water treatment apparatus water supply piping of this invention. 図1の濾過装置の空気洗浄工程1(給水配管空気洗浄工程)を説明する図である。It is a figure explaining the air washing process 1 (water supply piping air washing process) of the filtration apparatus of FIG. 図1の濾過装置の空気洗浄工程2(逆洗水配管及び処理水配管空気洗浄工程)を説明する図である。It is a figure explaining the air washing | cleaning process 2 (backwash water piping and treated water piping air washing process) of the filtration apparatus of FIG. 図1の濾過装置の逆洗工程を説明する図である。It is a figure explaining the backwashing process of the filtration apparatus of FIG. 図1の濾過装置の仕上げ洗浄工程を説明する図である。It is a figure explaining the finish washing process of the filtration apparatus of FIG. 本発明の水処理装置給水配管の洗浄方法の他の実施の形態を示す濾過装置の系統図である。It is a systematic diagram of the filtration apparatus which shows other embodiment of the washing | cleaning method of the water treatment apparatus water supply piping of this invention. 図6の濾過装置の空気洗浄工程1(給水配管空気洗浄工程)を説明する図である。It is a figure explaining the air washing | cleaning process 1 (water supply piping air washing | cleaning process) of the filtration apparatus of FIG. 図6の濾過装置の空気洗浄工程2(処理水配管空気洗浄工程)を説明する図である。It is a figure explaining the air washing process 2 (process water piping air washing process) of the filtration apparatus of FIG. 図6の濾過装置の逆洗工程を説明する図である。It is a figure explaining the backwashing process of the filtration apparatus of FIG. 図6の濾過装置の仕上げ洗浄工程を説明する図である。It is a figure explaining the finish washing process of the filtration apparatus of FIG. 本発明の水処理装置給水配管の洗浄方法の別の実施の形態を示す水処理装置の系統図である。It is a systematic diagram of the water treatment apparatus which shows another embodiment of the washing | cleaning method of the water treatment apparatus water supply piping of this invention. 図11の水処理装置の空気洗浄工程1(給水配管空気洗浄工程)を説明する図である。It is a figure explaining the air cleaning process 1 (water supply piping air cleaning process) of the water treatment apparatus of FIG. 図11の水処理装置の空気洗浄工程2(濾過処理水配管空気洗浄工程)を説明する図である。It is a figure explaining the air washing process 2 (filtered water piping air washing process) of the water treatment apparatus of FIG. 図11の水処理装置の逆洗工程を説明する図である。It is a figure explaining the backwashing process of the water treatment apparatus of FIG. 図11の水処理装置の仕上げ洗浄工程1を説明する図である。It is a figure explaining the finishing cleaning process 1 of the water treatment apparatus of FIG. 図11の水処理装置の仕上げ洗浄工程2を説明する図である。It is a figure explaining the finishing cleaning process 2 of the water treatment apparatus of FIG. 図11の水処理装置の空気洗浄工程3(カチオン交換処理水配管空気洗浄工程)を説明する図である。It is a figure explaining the air washing process 3 (cation exchange process water piping air washing process) of the water treatment apparatus of FIG.

詳細な説明Detailed description

以下に図面を参照して本発明の実施の形態を詳細に説明する。  Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

なお、本発明において、水処理装置の給水配管の空気洗浄を行う工程を「空気洗浄工程1」と称し、水処理装置の処理水配管や逆洗水配管の空気洗浄を行う工程を「空気洗浄工程2」又は「空気洗浄工程3」と称す。  In the present invention, the process of performing air cleaning of the water supply piping of the water treatment apparatus is referred to as “air cleaning process 1”, and the process of performing air cleaning of the treated water piping and backwash water piping of the water treatment apparatus is referred to as “air cleaning. This is referred to as “Step 2” or “Air Cleaning Step 3”.

[実施形態1]
まず、図1〜5を参照して本発明の実施形態の一例を説明する。
図1〜5は、本発明の水処理装置給水配管の洗浄方法の実施の形態を示す濾過装置の系統図であり、このうち、図2は、本発明に係る空気洗浄工程1(給水配管空気洗浄工程)を示す図であり、図3は、本発明に係る空気洗浄工程2(逆洗水配管及び処理水配管空気洗浄工程)を示す図であり、図4は、本発明に係る逆洗工程を示す図であり、図5は、本発明に係る仕上げ洗浄工程を示す図である。図2〜5において、流体が流通している配管は、流体が流通していない配管よりも太い実線で示してある。また、流体の流れている弁は黒塗りされている。
[Embodiment 1]
First, an example of an embodiment of the present invention will be described with reference to FIGS.
1 to 5 are system diagrams of a filtration device showing an embodiment of a water treatment device water supply pipe cleaning method of the present invention. Among these, FIG. 2 shows an air cleaning step 1 (water supply pipe air according to the present invention). FIG. 3 is a diagram showing an air cleaning step 2 (backwash water piping and treated water piping air cleaning step) according to the present invention, and FIG. 4 is a backwashing according to the present invention. FIG. 5 is a diagram illustrating a finishing cleaning process according to the present invention. 2-5, the pipe | tube with which the fluid distribute | circulates is shown with the thick continuous line rather than the pipe | tube with which the fluid does not distribute | circulate. The valve through which the fluid flows is painted black.

図1〜5中、1は原水槽、2は濾過器、3は処理水槽、Pは原水ポンプ、Pは逆洗ポンプ、V,Vは空気入口弁、Vは濾過入口弁、Vは濾過出口弁、Vは逆洗出口弁、Vは逆洗入口弁、V,Vは洗浄出口弁、Vは処理水槽入口弁である。11〜23は配管を示す。X〜Xは配管接続部を示す。1 to 5, 1 is a raw water tank, 2 is a filter, 3 is a treated water tank, P 1 is a raw water pump, P 2 is a backwash pump, V 1 and V 7 are air inlet valves, and V 2 is a filtration inlet valve. , V 3 is filtered outlet valve, V 4 is the backwash outlet valve, V 5 is backwashing inlet valve, V 6, V 8 is washed outlet valve, V 9 is a process water tank inlet valve. 11-23 show piping. X 1 to X 5 represents a pipe connection part.

なお、空気注入配管16は、原水ポンプPの吐出部近傍に設けられており、通常、空気注入配管16と給水配管12との接続部Xと原水ポンプPの吐出部との配管距離は50cm以下である。また、逆洗排水を排出する配管(逆洗排水配管)17と給水配管12との接続部Xと濾過器2の原水導入口2Aとの配管距離、即ち、配管13の長さは通常20〜200cm程度である。The air injection pipe 16 is provided in the discharge portion near the raw water pump P 1, usually, the pipe distance between the connecting portion X 1 and raw water discharge portion of the pump P 1 of a water supply pipe 12 and the air injection pipe 16 Is 50 cm or less. Further, the pipe distance piping (backwash drain pipe) 17 and the connecting portions X 2 and the water supply pipe 12 and the raw water inlet 2A of the filter 2 for discharging the backwash effluent, i.e., the length of the pipe 13 is usually 20 About 200 cm.

また、空気注入配管21は、逆洗ポンプPの吐出部近傍に設けられており、通常、空気注入配管21と逆洗水配管19との接続部Xと逆洗ポンプPの吐出部との配管距離は50cm以下である。また、逆洗水配管19と処理水配管15との接続部Xと濾過器2の処理水排出口2Bとの配管距離、即ち、配管14の長さは通常20〜200cm程度となるように、逆洗水配管19は、処理水配管のうちの濾過器2の処理水排出口2Bの近傍に設けられている。更に、逆洗水配管19及び処理水配管15の洗浄排水を排出する配管(洗浄排水配管)22と処理水配管15との接続部Xと処理水槽3の処理水入口3Aとの配管距離、即ち、配管23の長さは、通常50〜500cm程度である。The air injection pipe 21 is provided in the discharge portion near the backwash pump P 2, usually connecting portion X 4 and backwash discharge portion of the pump P 2 of the air injection pipe 21 and the backwash water pipe 19 And the piping distance is 50 cm or less. Further, the pipe distance between the backwash water pipe 19 and the connecting portion X 3 of the treated water pipe 15 and the treated water outlet 2B of filter 2, i.e., so that the length of the piping 14 becomes usually about 20~200cm The backwash water pipe 19 is provided in the vicinity of the treated water discharge port 2B of the filter 2 in the treated water pipe. Furthermore, the pipe distance between the pipe (detergent drain pipe) 22 and the treated water inlet 3A of the connecting portions X 5 and the processing water tank 3 with the treated water pipe 15 for discharging the wash effluent backwash water pipe 19 and the treated water pipe 15, That is, the length of the pipe 23 is usually about 50 to 500 cm.

なお、図1〜5の濾過装置に限らず、いずれの水処理装置においても、空気注入配管は、空気がポンプに入らないように、ポンプの吐出側に接続される。  In addition, not only the filtration apparatus of FIGS. 1-5, but in any water treatment apparatus, air injection piping is connected to the discharge side of a pump so that air may not enter a pump.

原水の濾過運転時には、濾過入口弁Vと濾過出口弁V及び処理水槽入口弁Vを開、その他の弁を閉とし、また、原水ポンプPを作動、逆洗ポンプPを停止し、原水槽1内の原水を配管11、配管12、及び配管13を経て濾過器2に導入して濾過処理し、濾過処理水を配管14、配管15及び配管23を経て処理水槽3に導入する。During filtration operation of the raw water is filtered inlet valve V 2 and filtration outlet valve V 3 and the process water tank inlet valve V 9 is opened, the other valves are closed, also operates the raw water pump P 1, stop backwash pump P 2 Then, the raw water in the raw water tank 1 is introduced into the filter 2 through the pipe 11, the pipe 12 and the pipe 13 and filtered, and the filtered water is introduced into the treated water tank 3 through the pipe 14, the pipe 15 and the pipe 23. To do.

このような濾過運転を継続することにより系内の汚れにより圧力損失の増大、その他の不具合が生じた場合、或いは、所定の濾過運転を継続した後、定期的に以下の(1)〜(7)の手順で洗浄を行う。  By continuing such filtration operation, when the pressure loss increases due to dirt in the system or other problems occur, or after the predetermined filtration operation is continued, the following (1) to (7) ) Follow the procedure for cleaning.

(1) 空気洗浄工程1(給水配管空気洗浄工程)(図2)
原水ポンプPを運転したまま、空気入口弁V及び逆洗出口弁Vを開、濾過出口弁V及び処理水槽入口弁Vを閉とし(即ち、空気入口弁V、及び濾過入口弁Vと逆洗出口弁Vのみ開、その他の弁は閉)、空気注入配管16より、給水配管12に圧縮空気を注入し、原水と空気との気液混合流体を給水配管12に流して空気洗浄し、洗浄排水を配管17より排出する。
(1) Air cleaning process 1 (water supply pipe air cleaning process) (Fig. 2)
While operating the raw water pump P 1, an air inlet valve V 1 and the backwash outlet valve V 4 opened, the filtration outlet valve V 3 and the process water tank inlet valve V 9 is closed (i.e., the air inlet valve V 1, and filtered an inlet valve V 2 only backwash outlet valve V 4 opened, the other valves closed), from the air injection pipe 16, by injecting compressed air into the water supply pipe 12, water supply pipe to the gas-liquid mixed fluid of the raw water and the air 12 The air is washed with air and the washing waste water is discharged from the pipe 17.

この空気洗浄工程1では、原水は通常の濾過運転時と同等の流量で給水配管12内を流れるが、原水ポンプPの直近に設けられた空気注入配管16から吹き込まれた空気と原水とが混合流体となって、給水配管12内を流れることにより、配管12内で乱流が発生し、配管12の内壁に付着した微生物等の汚染物を剥離除去する。この剥離された微生物塊等の不純物を含む気液混合流は、濾過入口弁Vを通って、更に一部配管13にまで流入するが、逆洗出口弁Vが開とされ、他の弁V,V,Vが閉とされていることにより、濾過器2内まで殆ど入り込むことはなく、配管17より系外へ排出される。In the air cleaning process 1, the raw water is flowing through the normal filtration water supply pipe 12 in operation at the same flow rate, and air blown from the air injection pipe 16 provided in the immediate vicinity of the raw water pump P 1 raw water Metropolitan By flowing through the water supply pipe 12 as a mixed fluid, turbulent flow is generated in the pipe 12, and contaminants such as microorganisms attached to the inner wall of the pipe 12 are peeled and removed. The gas-liquid mixed flow containing impurities such as the separated microbial mass flows through the filtration inlet valve V 2 and further flows into the pipe 13, but the backwash outlet valve V 4 is opened, and the other Since the valves V 3 , V 5 , and V 6 are closed, they hardly enter the filter 2 and are discharged out of the system through the pipe 17.

この空気洗浄工程により、給水配管のうち、前述の接続部Xの上流側の配管12が空気洗浄される。
なお、この空気洗浄工程1における空気混合水用の洗浄水は、原水に限らず、濾過処理水や、他系統の水であっても良い。
By this air cleaning step, of the water supply pipe, upstream of the pipe 12 of the aforementioned connecting portion X 2 is an air purifier.
Note that the cleaning water for the air-mixed water in the air cleaning step 1 is not limited to raw water, but may be filtered water or water of another system.

(2) 休止工程1
上記空気洗浄工程1後は、直ちに次の洗浄工程を実施しても良く、休止工程を介在させても良い。休止工程の有無は、洗浄効果に特に影響しない。
休止工程を行なう場合は、すべての弁を閉とすると共に、原水ポンプP、逆洗ポンプPを停止する。
(2) Pause process 1
After the air cleaning step 1, the next cleaning step may be performed immediately or a pause step may be interposed. The presence or absence of the pause process does not particularly affect the cleaning effect.
When performing the suspension process, all the valves are closed and the raw water pump P 1 and the backwash pump P 2 are stopped.

(3) 空気洗浄工程2(逆洗水配管及び処理水配管空気洗浄工程)(図3)
本実施形態の濾過装置においては、処理水が流通する処理水配管や逆洗水配管も給水配管ほどではないものの微生物が増殖し、汚染物質が付着するおそれがあり、特に、逆洗水配管に付着した汚染物質が逆洗時に剥離して濾過器2に流入すると二次汚染の原因となる。
(3) Air washing process 2 (back washing water pipe and treated water pipe air washing process) (Fig. 3)
In the filtration device of the present embodiment, the treated water pipe and the backwash water pipe through which the treated water circulates are not as large as the feed water pipe, but there is a risk that microorganisms will grow and contaminate may adhere, especially in the backwash water pipe. If the adhering contaminants peel off at the time of backwashing and flow into the filter 2, it causes secondary contamination.

このため、処理水配管、及び逆洗水として処理水を用いる場合の逆洗水配管についても、空気混合水で空気洗浄して汚染物質を剥離除去し、系外へ排出することが好ましい。  For this reason, also about the backwash water piping in the case of using the treated water as the backwater and the backwash water, it is preferable to remove the pollutants by air cleaning with the air mixed water, and to discharge out of the system.

そこで、この空気洗浄工程2では、逆洗水配管19と処理水配管15を空気混合水で洗浄するために、空気入口弁V及び逆洗入口弁V、濾過出口弁V、洗浄出口弁Vを開とし、その他の弁は閉として、逆洗ポンプPを作動させ(原水ポンプPは停止)、空気注入配管21より、逆洗水配管19に圧縮空気を注入し、配管18を経て送給される処理水槽3からの処理水と空気との気液混合流体を、逆洗水配管19から接続部Xを経て処理水配管15に流して空気洗浄し、洗浄排水を配管22より系外へ排出する。Therefore, in the air cleaning step 2, the backwash water pipe 19 and the treated water pipe 15 for cleaning air mixed water, air inlet valves V 7 and backwash inlet valve V 5, filtered outlet valve V 3, washed outlet the valve V 8 is opened, the other valves closed, actuating the backwash pump P 2 (raw water pump P 1 is stopped), from the air injection pipe 21, by injecting compressed air into the backwash water pipe 19, the pipe the treated water and gas-liquid mixed fluid of air 18 from the process water tank 3 is fed through, and air cleaning by passing the backwash water pipe 19 to the connection part X 3 a through the process water pipe 15, the detergent drain It is discharged out of the system through the pipe 22.

この空気洗浄工程2では、処理水槽3からの処理水は、後述の逆洗工程における流量と同等の流量で逆洗水配管19及び処理水配管15内を流れるが、逆洗ポンプPの直近に設けられた空気注入配管21から吹き込まれた空気と処理水とが混合流体となって、逆洗水配管19及び処理水配管15内を流れることにより、配管19,15内で乱流が発生し、配管19,15の内壁に付着した微生物等の汚染物を剥離除去する。この剥離された微生物塊等の不純物を含む気液混合流は、更に一部配管23にまで流入するが、処理水槽入口の近傍に設けた処理水槽入口弁Vを閉じることにより、処理水槽3内まで殆ど入り込むことはなく、配管22より系外へ排出される。In the air cleaning step 2, processing the treated water from the water tank 3 is flowing within flow equivalent backwash water pipe 19 and treated water pipe at a rate of 15 in the backwash process will be described later, the most recent backwash pump P 2 Turbulent flow is generated in the pipes 19 and 15 when the air blown from the air injection pipe 21 provided in the water and the treated water become a mixed fluid and flow in the backwash water pipe 19 and the treated water pipe 15. Then, contaminants such as microorganisms attached to the inner walls of the pipes 19 and 15 are peeled and removed. The gas-liquid mixed flow containing impurities such as the separated microbial mass flows further into a part of the pipe 23, but the treated water tank 3 is closed by closing the treated water tank inlet valve V 9 provided in the vicinity of the treated water tank inlet. It hardly enters the inside and is discharged out of the system through the pipe 22.

この空気洗浄工程2により、逆洗水配管のうち、接続部Xと接続部Xとの間の部分の逆洗水配管19と、処理水配管のうち、接続部Xと接続部Xとの間の部分の処理水配管15が空気洗浄される。The air washing step 2, of the backwash water pipe, the connection section and the backwash water pipe 19 portion between X 4 and the connecting portion X 3, among the treated water pipe, the connection portions X 3 and the connecting portion X portion of the treated water pipe 15 between the 5 is air cleaned.

なお、上記空気洗浄工程2では、逆洗水配管のうち逆洗ポンプPの上流側の配管18を洗浄することはできないが、逆洗ポンプPを処理水槽3の処理水出口3Bに極力近づけて設けることにより、配管の非洗浄部を殆どなくすことができる。ただし、配管15の長さが数m(1〜5m)程度となる場合には、配管15の処理水槽3近傍に洗浄液体導入手段と、該洗浄液体導入手段よりも処理水槽側にバルブを設け、数日から数週間に1回程度洗浄するようにすることもできる。
また、接続部Xと濾過器2の処理水排出口2Bとの間の配管14についても、配管14の長さはせいぜい20〜200cm程度であり、この間が非洗浄部となっても問題はない。
同様に、接続部Xと処理水槽3の処理水入口3Aとの間の配管23についても、接続部Xを処理水入口3A近傍に設け、配管23の長さを500cm以下、好ましくは100〜200cmとすることにより、非洗浄部を殆どなくすことができる。
In the air cleaning step 2, it is not possible to clean the upstream side of the pipe 18 of the backwash pump P 2 of the backwash water piping, as much as possible backwash pump P 2 in the treated water outlet 3B of the treatment water tank 3 By providing them close to each other, the non-cleaning portion of the pipe can be almost eliminated. However, when the length of the pipe 15 is about several meters (1 to 5 m), a cleaning liquid introducing means is provided near the treated water tank 3 of the pipe 15 and a valve is provided on the treated water tank side of the cleaning liquid introducing means. In addition, it may be cleaned once every few days to several weeks.
Further, the pipe 14 between the connecting portions X 3 and the treated water outlet 2B of filter 2 also, the length of the pipe 14 is at most about 20~200Cm, even the problem during this time the non-cleaning section Absent.
Similarly, the pipe 23 between the treated water inlet 3A of the connecting portions X 5 and the processing water tank 3 is also provided in the treated water inlet 3A near the connection portions X 5, a length of tubing 23 500 cm or less, preferably 100 By setting it to ~ 200 cm, the non-cleaning part can be almost eliminated.

また、逆洗水配管19からの空気混合水は、接続部Xから一部配管14に流入するおそれがあるが、濾過入口弁Vと逆洗出口弁Vが閉とされていることにより、濾過器2内には殆ど流入することはない。Further, the air mixed water from the backwash water pipe 19, there is a risk that flows into the part pipe 14 from the connecting portion X 3, that the filtration inlet valve V 2 backwashing outlet valve V 4 is closed Therefore, it hardly flows into the filter 2.

この空気洗浄工程2は、逆洗工程時に逆洗水配管内の汚染物質が濾過器2内に流入することを防止するために、逆洗工程に先立って実施されるが、逆洗工程の前であれば、前記空気洗浄工程1の前であっても後であっても良い。
この空気洗浄工程2を空気洗浄工程1と同時に行うこともできるが、通常は別々に行われる。
This air washing step 2 is performed prior to the back washing step in order to prevent contaminants in the back washing water pipe from flowing into the filter 2 during the back washing step. If so, it may be before or after the air cleaning step 1.
The air cleaning step 2 can be performed simultaneously with the air cleaning step 1, but is usually performed separately.

また、上記空気洗浄工程2では、逆洗水配管と処理水配管とを同時に空気洗浄するが、逆洗水配管と処理水配管とは別々に洗浄してもよい。
例えば、空気入口弁V及び逆洗入口弁V、洗浄出口弁Vを開とし、その他の弁は閉として逆洗ポンプPを作動させ(原水ポンプPは停止)、空気注入配管21からの圧縮空気と処理水槽3からの処理水との気液混合流体を逆洗水配管19に流して空気洗浄し、洗浄排水を接続部Xを経て配管20より系外へ排出することにより、逆洗水配管19のみを洗浄することができる。
In the air washing step 2, the backwash water pipe and the treated water pipe are simultaneously air washed, but the backwash water pipe and the treated water pipe may be washed separately.
For example, the air inlet valve V 7 and backwash inlet valve V 5, a cleaning outlet valve V 6 is opened, other valves activates the backwash pump P 2 is closed (the raw water pump P 1 is stopped), an air injection pipe the gas-liquid mixed fluid of treated water from the compressed air and the treatment water tank 3 from 21 and air washing by passing the backwash water pipe 19, to discharge the washing water discharge to the outside of the system from the pipe 20 via connection X 3 Thus, only the backwash water pipe 19 can be washed.

また、処理水配管については、後述の実施形態2における空気洗浄工程2のように、処理水配管15に空気を注入する空気注入配管を設けておき、この空気注入配管の空気入口弁と、濾過入口弁V、濾過出口弁V、及び洗浄出口弁Vを開、その他の弁を閉として、原水ポンプP作動、逆洗ポンプP停止で、原水を配管12及び配管13を経て濾過器2に導入し、濾過器2からの処理水と空気との気液混合流体を配管15に流し、配管22から系外へ排出することにより、処理水配管15の空気洗浄を行うことができる。Moreover, about the treated water piping, the air injection piping which inject | pours air into the treated water piping 15 is provided like the air washing process 2 in below-mentioned Embodiment 2, the air inlet valve of this air injection piping, and filtration The inlet valve V 2 , the filtration outlet valve V 3 , and the washing outlet valve V 8 are opened, the other valves are closed, the raw water pump P 1 is activated, the backwash pump P 2 is stopped, and the raw water is passed through the pipe 12 and the pipe 13. By introducing the gas-liquid mixed fluid of treated water and air from the filter 2 to the pipe 15 and discharging the pipe 22 out of the system, the treated water pipe 15 is cleaned with air. it can.

ただし、この場合、前記逆洗水配管のみの洗浄は、逆洗工程の前に行うことが好ましいが、上記処理水配管のみの洗浄は、給水配管13の洗浄を行う逆洗工程を行った後に行うことが好ましく、また、更に、後述の仕上げ洗浄工程後に行ってもよい。  However, in this case, it is preferable to perform the cleaning of only the backwashing water pipe before the backwashing process. However, the cleaning of only the treated water pipe is performed after the backwashing process of cleaning the water supply pipe 13. It is preferable to carry out, and further, it may be carried out after the finishing cleaning step described later.

なお、この空気洗浄工程2における空気混合水用の洗浄水は、処理水に限らず、原水や他系統の水であっても良い。  Note that the cleaning water for the air mixed water in the air cleaning step 2 is not limited to the treated water but may be raw water or water of another system.

また、この空気洗浄工程2は必須ではなく適宜省略することができる。即ち、原水の給水配管は、原水槽1内で増殖した微生物の塊(マッドボール)が流入してくるために、比較的頻繁に洗浄を行う必要があるが、原水の濾過処理水が流通する処理水配管や逆洗水配管は、原水の給水配管ほど微生物の増殖の問題はない。このため、逆洗水配管や処理水配管の洗浄を行う空気洗浄工程2は、原水の給水配管の洗浄を行う前述の空気洗浄工程1及び後述の逆洗工程よりも洗浄頻度を低くして行ってもよく、処理水の水質によっては省略することも可能である。  Further, the air cleaning step 2 is not essential and can be omitted as appropriate. That is, the raw water supply pipe needs to be cleaned relatively frequently because the microbial mass (mud ball) grown in the raw water tank 1 flows in, but the filtered water of the raw water circulates. Treated water piping and backwash water piping are less prone to microbial growth than raw water supply piping. For this reason, the air washing process 2 for washing the backwash water pipe and the treated water pipe is performed at a lower washing frequency than the air washing process 1 for washing the raw water supply pipe and the backwashing process described later. It may be omitted depending on the quality of the treated water.

(4) 休止工程2
上記空気洗浄工程2後は、直ちに逆洗工程を実施しても良く、休止工程を介在させても良い。休止工程の有無は、洗浄効果に特に影響しない。
休止工程を行なう場合は、すべての弁を閉とすると共に、原水ポンプP、逆洗ポンプPを停止する。
(4) Pause process 2
After the air washing step 2, a back washing step may be performed immediately or a pause step may be interposed. The presence or absence of the pause process does not particularly affect the cleaning effect.
When performing the suspension process, all the valves are closed and the raw water pump P 1 and the backwash pump P 2 are stopped.

(5) 逆洗工程(図4)
前述の如く、空気洗浄工程1において、給水配管12部分の剥離洗浄は行えるが、給水配管のうち、逆洗排水配管17の接続部Xの下流側の配管13部分の洗浄は行うことはできない上に、この配管13部分や濾過器2内の入口部分に、空気洗浄時の洗浄水が剥離された微生物等と共に一部流入する恐れがある。
従って、本発明においては、上述の空気洗浄工程1,2、或いは空気洗浄工程1を行った後、逆洗工程を行って、濾過器2内及び配管13部分を洗浄する。
(5) Backwash process (Figure 4)
As described above, in the air cleaning step 1, the water supply pipe 12 can be peeled and cleaned, but the water supply pipe cannot clean the pipe 13 part downstream of the connection portion X 2 of the backwash drain pipe 17. Furthermore, there is a risk that the washing water at the time of air washing partially flows into the pipe 13 and the inlet portion in the filter 2 together with microorganisms and the like from which the washing water has been peeled off.
Therefore, in this invention, after performing the above-mentioned air washing process 1, 2, or the air washing process 1, the back washing process is performed and the inside of the filter 2 and the piping 13 part are wash | cleaned.

逆洗工程では、逆洗入口弁V、及び逆洗出口弁Vを開、その他の弁を閉として、逆洗ポンプP作動、原水ポンプP停止で、処理水槽3内の処理水を配管18、配管19及び配管14を経て濾過器2に逆流させ、逆洗排水を配管13及び配管17を経て系外へ排出する。
これにより、濾過器2内及び空気洗浄工程1で洗浄できなかった配管13部分を洗浄し、汚染物を系外へ排出することができる。
In the backwashing process, the backwashing inlet valve V 5 and the backwashing outlet valve V 4 are opened, the other valves are closed, the backwash pump P 2 is activated, the raw water pump P 1 is stopped, and the treated water in the treated water tank 3 is Is returned to the filter 2 through the pipe 18, the pipe 19 and the pipe 14, and the backwash waste water is discharged out of the system through the pipe 13 and the pipe 17.
Thereby, the piping 13 part which could not be cleaned in the filter 2 and the air cleaning step 1 can be cleaned, and the contaminants can be discharged out of the system.

(6) 休止工程3
上記逆洗工程後は、直ちに濾過運転を再開しても良く、後述の仕上げ洗浄工程を行った後、濾過運転を再開しても良く、濾過運転又は仕上げ洗浄工程との間に休止工程を介在させても良い。
休止工程の有無は、洗浄効果に特に影響しない。休止工程を行なう場合は、すべての弁を閉とすると共に、原水ポンプP、逆洗ポンプPを停止する。
(6) Pause process 3
After the backwashing process, the filtration operation may be resumed immediately, or after the finishing washing process described later, the filtering operation may be resumed, and a pause process is interposed between the filtering operation or the finishing washing process. You may let them.
The presence or absence of the pause process does not particularly affect the cleaning effect. When performing the suspension process, all the valves are closed and the raw water pump P 1 and the backwash pump P 2 are stopped.

(7) 仕上げ洗浄工程(図5)
仕上げ洗浄を行う場合は、濾過入口弁V及び洗浄出口弁Vを開、その他の弁を閉とし、原水ポンプP作動、逆洗ポンプP停止として、原水槽1内の原水を配管11、配管12及び配管13を経て濾過器2に導入し、配管14、配管20及び配管17を経て系外へ排出する。
(7) Finish cleaning process (Figure 5)
When performing finish washing, filtration inlet valve V 2 and washed outlet valve V 6 opens, other valves were closed, the raw water pump P 1 operates as backwash pump P 2 is stopped, the raw water raw water tank 1 pipe 11, the pipe 12 and the pipe 13 are introduced into the filter 2, and the pipe 14, the pipe 20 and the pipe 17 are discharged to the outside of the system.

なお、図1〜5において、洗浄排水を排出する配管20は、逆洗排水配管17に接続しているが、この配管20は、逆洗排水配管17と接続されることなく、直接洗浄排水を排出するものであっても良い。  1 to 5, the pipe 20 for discharging the washing wastewater is connected to the backwash drainage pipe 17, but this pipe 20 is not connected to the backwash drainage pipe 17, It may be discharged.

この仕上げ洗浄は必須ではないが、このような仕上げ洗浄を行うことにより、濾過器2の出口側に残留する汚染物(逆洗工程で濾材から剥離した汚染物)を排出することができる。なお、この仕上げ洗浄の洗浄水には、原水の他、濾過処理水や他系統の処理水を用いることもできる。  Although this final cleaning is not essential, by performing such final cleaning, contaminants remaining on the outlet side of the filter 2 (contaminants separated from the filter medium in the backwashing step) can be discharged. In addition, as the cleaning water for the final cleaning, filtered water or other system water can be used in addition to the raw water.

上記一連の洗浄工程を経た後は、再び濾過入口弁Vと濾過出口弁Vを開、その他の弁を閉、原水ポンプP作動、逆洗ポンプP停止として、原水の濾過運転を再開する。After passing through the above series of washing steps, the filtration inlet valve V 2 and the filtration outlet valve V 3 are opened again, the other valves are closed, the raw water pump P 1 is activated, and the backwash pump P 2 is stopped, and the raw water is filtered. Resume.

[実施形態2]
次に、図6〜10を参照して本発明の実施形態の他の例を説明する。
図6〜10は、本発明の水処理装置給水配管の洗浄方法の実施の形態を示す濾過装置の系統図であり、このうち、図7は、本発明に係る空気洗浄工程1(給水配管空気洗浄工程)を示す図であり、図8は、本発明に係る空気洗浄工程2(処理水配管空気洗浄工程)を示す図であり、図9は、本発明に係る逆洗工程を示す図であり、図10は、本発明に係る仕上げ洗浄工程を示す図である。図7〜10において、流体が流通している配管は、流体が流通していない配管よりも太い実線で示してある。また、流体の流れている弁は黒塗りされている。
[Embodiment 2]
Next, another example of the embodiment of the present invention will be described with reference to FIGS.
6 to 10 are system diagrams of a filtration apparatus showing an embodiment of a method for cleaning a water treatment apparatus water supply pipe of the present invention. Among these, FIG. 7 shows an air cleaning step 1 (water supply pipe air according to the present invention). FIG. 8 is a diagram showing an air cleaning step 2 (process water piping air cleaning step) according to the present invention, and FIG. 9 is a diagram showing a back washing step according to the present invention. FIG. 10 is a diagram showing a finish cleaning process according to the present invention. 7 to 10, the pipe through which the fluid flows is shown by a solid line that is thicker than the pipe through which no fluid flows. The valve through which the fluid flows is painted black.

図6〜10に示す濾過装置は、処理水ではなく、系外からの市水、工水等の比較的清浄度の高い水で逆洗を行うように逆洗水配管19、逆洗入口弁V及び逆洗ポンプPが設けられている点が、図1〜5に示される濾過装置と異なり、その他は同様の構成とされている。
図6〜10において、図1〜5に示される部材と同一機能を奏する部材には同一符号を付してある。
The filtration device shown in FIGS. 6 to 10 has a backwash water pipe 19 and a backwash inlet valve so that backwashing is performed not with treated water but with water with relatively high cleanliness, such as city water and industrial water from outside the system. point V 5 and backwash pump P 2 is provided with, different from the filtering device shown in FIGS. 1-5, others have the same construction.
6 to 10, members having the same functions as those shown in FIGS. 1 to 5 are denoted by the same reference numerals.

この濾過装置において、原水の濾過運転、空気洗浄工程1(図7)、逆洗工程(図9)及び仕上げ洗浄工程(図10)は、図1〜5に示す濾過装置の空気洗浄工程1(図2)、逆洗工程(図4)及び仕上げ洗浄工程(図5)と同様に実施される。
従って、空気洗浄工程1、逆洗工程及び仕上げ洗浄工程については説明を省略し、以下に、図8を参照して、処理水配管の空気洗浄を行う空気洗浄工程2について説明する。
In this filtration apparatus, the raw water filtration operation, the air washing process 1 (FIG. 7), the back washing process (FIG. 9) and the final washing process (FIG. 10) are performed in the air washing process 1 ( 2), backwashing process (FIG. 4) and finish cleaning process (FIG. 5).
Therefore, description of the air cleaning process 1, the back cleaning process, and the finish cleaning process is omitted, and the air cleaning process 2 for performing air cleaning of the treated water pipe will be described below with reference to FIG.

本実施形態の濾過装置では、逆洗水配管には、工水、市水等の微生物の増殖の問題のない水が流れるため、逆洗水配管19についての空気洗浄を行う必要はない。
従って、空気洗浄工程2においては、濾過入口弁V、濾過出口弁V、空気入口弁V 及び洗浄出口弁Vを開、その他の弁を閉として、原水ポンプPを作動させ(逆洗ポンプPは停止)、空気注入配管21より、処理水配管15に圧縮空気を注入すると共に、原水槽1内の原水を配管11、配管12及び配管13を経て濾過器2に導入し、配管14からの処理水と空気との気液混合流体を処理水配管15に流して空気洗浄し、洗浄排水を配管22より系外へ排出することにより、処理水配管15内の汚染物質を剥離除去して系外へ排出する。
  In the filtration device of the present embodiment, water having no problem of microbial growth such as industrial water and city water flows through the backwash water pipe, and therefore it is not necessary to perform air washing on the backwash water pipe 19.
  Therefore, in the air washing step 2, the filtration inlet valve V2, Filtration outlet valve V3, Air inlet valve V 7And washing outlet valve V8Open the other valve and close the raw water pump P1(Backwash pump P2The compressed water is injected into the treated water pipe 15 from the air injection pipe 21, and the raw water in the raw water tank 1 is introduced into the filter 2 through the pipe 11, the pipe 12 and the pipe 13. A gas-liquid mixed fluid of treated water and air is flowed to the treated water pipe 15 for air cleaning, and the washing waste water is discharged out of the system through the pipe 22 to remove and remove contaminants in the treated water pipe 15. Drain out.

本実施形態において、空気洗浄工程2は、必ずしも逆洗工程の前に行う必要はなく、逆洗工程後であってもよい。また、空気洗浄工程1の前に行ってもよく、仕上げ洗浄工程後に行ってもよい。また、実施形態1と同様、この空気洗浄工程2は適宜省略することができ、また、空気洗浄に用いる水も、原水に限らず、工水等の系外からの水であってもよい。  In this embodiment, the air washing process 2 does not necessarily need to be performed before the back washing process, and may be after the back washing process. Moreover, you may perform before the air washing | cleaning process 1 and you may carry out after a finishing washing | cleaning process. Further, as in the first embodiment, the air cleaning step 2 can be omitted as appropriate, and the water used for the air cleaning is not limited to raw water but may be water from outside the system such as industrial water.

[実施形態3]
次に、図11〜17を参照して本発明の実施の形態の更に別の例を説明する。
図11〜17は、本発明の水処理装置給水配管の洗浄方法の実施の形態を示す、濾過器とカチオン交換塔とを備える水処理装置の系統図であり、このうち、図12は、本発明に係る空気洗浄工程1(給水配管空気洗浄工程)を示す図であり、図13は、本発明に係る空気洗浄工程2(濾過処理水配管空気洗浄工程)を示す図であり、図14は、本発明に係る逆洗工程を示す図であり、図15は、本発明に係る仕上げ洗浄工程1を示す図であり、図16は、本発明に係る仕上げ洗浄工程2を示す図であり、図17は、本発明に係る空気洗浄工程3(カチオン交換処理水配管空気洗浄工程)を示す図である。
図12〜17において、流体が流通している配管は、流体が流通していない配管よりも太い実線で示してある。また、流体の流れている弁は黒塗りされている。
[Embodiment 3]
Next, still another example of the embodiment of the present invention will be described with reference to FIGS.
FIGS. 11 to 17 are system diagrams of a water treatment apparatus including a filter and a cation exchange tower, showing an embodiment of a method for cleaning a water treatment apparatus water supply pipe of the present invention. Among these, FIG. FIG. 13 is a diagram showing an air cleaning step 1 (feed water piping air cleaning step) according to the invention, FIG. 13 is a diagram showing an air cleaning step 2 (filtered water piping air cleaning step) according to the present invention, and FIG. FIG. 15 is a diagram showing a backwashing process 1 according to the present invention, FIG. 16 is a diagram showing a finishwashing process 2 according to the present invention, FIG. 17 is a diagram showing an air cleaning step 3 (cation exchange treated water piping air cleaning step) according to the present invention.
12-17, the pipe | tube with which the fluid distribute | circulates is shown with the thick continuous line rather than the pipe | tube with which the fluid does not distribute | circulate. The valve through which the fluid flows is painted black.

図11〜17に示す水処理装置は、図6〜10に示す濾過装置の後段に更にカチオン交換塔4を設けたものであり、濾過装置については、図6〜11に示すものと同様の構成とされ、同一機能を奏する部材には同一符号を付してある。
は、カチオン交換塔4の逆洗ポンプ、V11,V12は洗浄出口弁、V10はカチオン交換入口弁、V13は逆洗入口弁、V14は空気入口弁、V15はカチオン交換出口弁である。
24〜31は配管を示し、X〜Xは配管接続部を示す。
The water treatment apparatus shown in FIGS. 11 to 17 is provided with a cation exchange tower 4 in the subsequent stage of the filtration apparatus shown in FIGS. 6 to 10, and the filtration apparatus has the same configuration as that shown in FIGS. The members having the same function are denoted by the same reference numerals.
P 3 is a backwash pump of the cation exchange tower 4, V 11 and V 12 are washing outlet valves, V 10 is a cation exchange inlet valve, V 13 is a backwash inlet valve, V 14 is an air inlet valve, and V 15 is a cation. Exchange outlet valve.
Reference numerals 24 to 31 denote pipes, and X 6 to X 8 denote pipe connection parts.

配管接続部Xとカチオン交換塔4の導入口4Aとの間の配管距離、即ち配管23の長さは通常20〜200cm程度であり、配管接続部Xと処理水槽3の処理水入口3Aとの間の配管距離、即ち、配管27の長さは通常50〜500cm程度である。
また、逆洗水配管30とカチオン交換処理水配管との接続部Xとカチオン交換塔4のカチオン交換処理水排出口4Bとの配管距離、即ち、配管24の長さは通常20〜200cm程度となるように、逆洗水配管30は、カチオン交換処理水配管のうちのカチオン交換塔4の処理水排出口4Bの近傍に設けられている。更に、カチオン交換処理水配管26の洗浄排水を排出する配管(洗浄排水配管)28と処理水配管26との接続部Xと処理水槽3の処理水入口3Aとの配管距離、即ち、配管27の長さは、通常50〜500cm程度である。
また、空気注入配管31とカチオン交換処理水配管との接続部Xを、逆洗水配管30と処理水配管24との接続部X近傍に設ける事で、配管25の長さに関係なく空気洗浄することができる。
Piping distance between the inlet 4A of the pipe connecting portion X 5 and the cation exchange column 4, i.e. the length of the pipe 23 is usually about 20~200Cm, the treatment water tank 3 and the pipe connecting portion X 8 treated water inlet 3A The distance between the pipes, that is, the length of the pipe 27 is usually about 50 to 500 cm.
Moreover, the backwash water pipe 30 and the pipe distance between the connecting part X 6 and the cation exchange treated water outlet 4B of the cation exchange column 4 of the cation exchange treatment water pipe, i.e., the length of the pipe 24 is usually about 20~200cm Thus, the backwash water pipe 30 is provided in the vicinity of the treated water discharge port 4B of the cation exchange tower 4 in the cation exchange treated water pipe. Furthermore, the pipe distance between the treated water inlet 3A of the connecting portions X 8 processed water tank 3 and the pipe (detergent drain pipe) 28 for discharging the washing water discharge of the cation exchange treatment water pipe 26 and the treated water pipe 26, i.e., the pipe 27 The length of is usually about 50 to 500 cm.
Further, by providing the connection portion X 7 between the air injection pipe 31 and the cation exchange treated water pipe in the vicinity of the connection portion X 6 between the backwash water pipe 30 and the treated water pipe 24, regardless of the length of the pipe 25. Can be air washed.

原水の水処理運転時には、濾過入口弁V及び濾過出口弁Vと、カチオン交換入口弁V10およびカチオン交換出口弁V15を開、その他の弁を閉とし、また、原水ポンプP を作動、逆洗ポンプP,Pを停止し、原水槽1内の原水を配管11、配管12、及び配管13を経て濾過器2に導入して濾過処理し、濾過処理水を更に配管14、配管15、及び配管23を経てカチオン交換塔4に導入してカチオン交換処理し、カチオン交換処理水を配管24、配管25、配管26及び配管27を経て処理水槽3に導入する。  During raw water treatment operation, the filtration inlet valve V2And filtration outlet valve V3And cation exchange inlet valve V10And cation exchange outlet valve V15Open the other valve, and close the raw water pump P 1, Backwash pump P2, P3The raw water in the raw water tank 1 is introduced into the filter 2 through the pipe 11, the pipe 12 and the pipe 13 and filtered, and the filtered water is further cationd through the pipe 14, the pipe 15 and the pipe 23. The cation exchange treatment water is introduced into the exchange tower 4 and cation exchange treatment water is introduced into the treated water tank 3 through the pipe 24, the pipe 25, the pipe 26 and the pipe 27.

このような水処理運転を継続することにより系内の汚れにより圧力損失の増大、その他の不具合が生じた場合、或いは、所定の濾過運転を継続した後、定期的に以下の(1)〜(7)の手順で洗浄を行う。  By continuing such a water treatment operation, when the pressure loss increases due to dirt in the system and other problems occur, or after a predetermined filtration operation is continued, the following (1) to ( Wash according to the procedure of 7).

(1) 空気洗浄工程1(給水配管空気洗浄工程)(図12)
図1〜10に示す濾過装置の空気洗浄工程1と同様に、原水ポンプPを運転したまま、空気入口弁V及び逆洗出口弁Vを開、濾過出口弁V、カチオン交換入口弁V10、カチオン交換出口弁V15及び処理水槽入口弁Vを閉とし(即ち、空気入口弁V、及び濾過入口弁Vと逆洗出口弁Vのみ開、その他の弁は閉)、空気注入配管16より、給水配管12に圧縮空気を注入し、原水と空気との気液混合流体を給水配管12に流して空気洗浄し、洗浄排水を配管17より排出する。
この空気洗浄工程では、原水は通常の濾過運転時と同等の流量で給水配管12内を流れるが、原水ポンプPの直近に設けられた空気注入配管16から吹き込まれた空気と原水とが混合流体となって、給水配管12内を流れることにより、配管12内で乱流が発生し、配管12の内壁に付着した微生物等の汚染物を剥離除去する。この剥離された微生物塊等の不純物を含む気液混合流は、濾過入口弁Vを通って、更に一部配管13にまで流入するが、逆洗出口弁Vが開とされ、他の弁V,V,Vが閉とされていることにより、濾過器2内まで殆ど入り込むことはなく、配管17より系外へ排出される。
(1) Air washing process 1 (water supply pipe air washing process) (FIG. 12)
As in the air washing step 1 of the filtration device shown in FIGS. 1 to 10, the air inlet valve V 1 and the backwash outlet valve V 4 are opened, the filtration outlet valve V 3 , and the cation exchange inlet are kept operating the raw water pump P 1. The valve V 10 , the cation exchange outlet valve V 15 and the treated water tank inlet valve V 9 are closed (that is, only the air inlet valve V 1 , the filtration inlet valve V 2 and the backwash outlet valve V 4 are opened, and the other valves are closed). ), Compressed air is injected into the water supply pipe 12 from the air injection pipe 16, a gas-liquid mixed fluid of raw water and air is passed through the water supply pipe 12 for air cleaning, and cleaning wastewater is discharged from the pipe 17.
In the air cleaning step, the raw water flows through the water supply pipe 12 in a normal filtration operation at the same flow rate, but the air blown from the air injection pipe 16 provided in the immediate vicinity of the raw water pump P 1 raw water Metropolitan mixture By flowing through the water supply pipe 12 as a fluid, a turbulent flow is generated in the pipe 12, and contaminants such as microorganisms attached to the inner wall of the pipe 12 are peeled and removed. The gas-liquid mixed flow containing impurities such as the separated microbial mass flows through the filtration inlet valve V 2 and further flows into the pipe 13, but the backwash outlet valve V 4 is opened, and the other Since the valves V 3 , V 5 , and V 6 are closed, they hardly enter the filter 2 and are discharged out of the system through the pipe 17.

この空気洗浄工程により、濾過器2の給水配管のうち、前述の接続部Xの上流側の配管12が空気洗浄される。
なお、この空気洗浄工程1における空気混合水用の洗浄水は、原水に限らず、濾過処理水や、他系統の水であっても良い。
By this air cleaning step, of the water supply pipe of the filter 2, the upstream side of the pipe 12 of the aforementioned connecting portion X 2 is an air purifier.
Note that the cleaning water for the air-mixed water in the air cleaning step 1 is not limited to raw water, but may be filtered water or water of another system.

(2) 休止工程1
上記空気洗浄工程1後は、直ちに次工程を実施しても良く、休止工程を介在させても良い。休止工程の有無は、洗浄効果に特に影響しない。
休止工程を行なう場合は、すべての弁を閉とすると共に、原水ポンプP、逆洗ポンプP,Pを停止する。
(2) Pause process 1
After the air cleaning step 1, the next step may be performed immediately or a pause step may be interposed. The presence or absence of the pause process does not particularly affect the cleaning effect.
When performing the pause process, all the valves are closed and the raw water pump P 1 and the backwash pumps P 2 and P 3 are stopped.

(3)空気洗浄工程2(濾過処理水配管空気洗浄工程)(図13)
空気洗浄工程2においては、図6〜10に示す濾過装置の空気洗浄工程2と同様に、濾過入口弁V、濾過出口弁V、空気入口弁V、カチオン交換入口弁V10、及び洗浄出口弁Vを開、その他の弁を閉として、原水ポンプPを作動させ(逆洗ポンプP,Pは停止)、空気流入配管21より、処理水配管15に圧縮空気を注入すると共に、原水槽1内の原水を配管11、配管12及び配管13を経て濾過器2に導入し、配管14からの処理水と空気との空気混合水を処理水配管15に流して空気洗浄し、洗浄排水を配管22より排出することにより、濾過処理水配管15内の汚染物質を剥離除去して系外へ排出する。
(3) Air washing process 2 (filtered water piping air washing process) (FIG. 13)
In the air washing step 2, the filtration inlet valve V 2 , the filtration outlet valve V 3 , the air inlet valve V 7 , the cation exchange inlet valve V 10 , and the air washing step 2 of the filtration device shown in FIGS. washed outlet valve V 8 opens, the other valve is closed, by operating the raw water pump P 1 (backwash pump P 2, P 3 is stopped), from the air inlet pipe 21, injecting compressed air into the treated water pipe 15 At the same time, the raw water in the raw water tank 1 is introduced into the filter 2 through the pipe 11, the pipe 12 and the pipe 13, and the mixed water of the treated water and air from the pipe 14 is caused to flow into the treated water pipe 15 for air cleaning. Then, by discharging the cleaning waste water from the pipe 22, the pollutants in the filtered water pipe 15 are peeled off and discharged out of the system.

この空気洗浄工程2は、必ずしも逆洗工程1の前に行う必要はなく、逆洗工程1後であってもよい。また、空気洗浄工程1の前に行ってもよく、仕上げ洗浄工程後に行ってもよい。また、実施形態2と同様、この空気洗浄工程2は適宜省略することができる。  This air washing step 2 does not necessarily have to be performed before the back washing step 1 and may be after the back washing step 1. Moreover, you may perform before the air washing | cleaning process 1 and you may carry out after a finishing washing | cleaning process. Further, as in the second embodiment, the air cleaning step 2 can be omitted as appropriate.

(4) 休止工程2
上記空気洗浄工程2後は、直ちに次の洗浄工程を実施しても良く、休止工程を介在させても良い。休止工程の有無は、洗浄効果に特に影響しない。
休止工程を行なう場合は、すべての弁を閉とすると共に、原水ポンプP、逆洗ポンプP,Pを停止する。
(4) Pause process 2
After the air cleaning step 2, the next cleaning step may be performed immediately or a pause step may be interposed. The presence or absence of the pause process does not particularly affect the cleaning effect.
When performing the pause process, all the valves are closed and the raw water pump P 1 and the backwash pumps P 2 and P 3 are stopped.

(5) 逆洗工程(図14)
空気洗浄工程1において、濾過器2の給水配管12部分の剥離洗浄は行えるが、給水配管のうち、逆洗排水配管17の接続部Xの下流側の配管13部分の洗浄は行うことはできない上に、この配管13部分や濾過器2内の入口部分に、空気洗浄時の洗浄水が剥離された微生物等と共に一部流入する恐れがある。
同様に、空気洗浄工程2において、カチオン交換塔4の給水配管となる濾過処理水配管15部分の剥離洗浄は行えるが、この配管のうち、接続部Xの下流側の配管23部分の洗浄は行うことはできない。
従って、本発明においては、上述の空気洗浄工程1,2又は空気洗浄工程1を行った後、逆洗工程を行って、濾過器2内及び配管13,23部分及びカチオン交換塔4内を洗浄する。
(5) Backwash process (Figure 14)
In the air cleaning process 1, but allows the stripping and cleaning of the feed water pipe 12 portion of the filter 2, of the feed water pipe, can not be carried out cleaning of the downstream pipe 13 portion of the connecting portion X 2 of the backwash drain pipe 17 Furthermore, there is a risk that the washing water at the time of air washing partially flows into the pipe 13 and the inlet portion in the filter 2 together with microorganisms and the like from which the washing water has been peeled off.
Similarly, in the air cleaning step 2, perform the stripping and cleaning of the filtration treatment water pipe 15 portion that becomes the feed water pipe cation exchange column 4, but of the pipe, the cleaning of the downstream pipe 23 portion of the connecting portion X 5 Can't do it.
Therefore, in this invention, after performing the above-mentioned air washing process 1, 2, or the air washing process 1, a back washing process is performed, and the inside of the filter 2, the piping 13,23 part, and the inside of the cation exchange tower 4 are washed. To do.

逆洗工程では、逆洗入口弁V,V13及び逆洗出口弁V,Vを開、その他の弁を閉として、逆洗ポンプP,P作動、原水ポンプP停止で、系外からの逆洗水を、配管19及び配管14を経て濾過器2に逆流させ、逆洗排水を配管13及び配管17を経て系外へ排出する。また、逆洗水を配管30,24を経てカチオン交換塔4に逆流させ、配管23及び配管22を経て系外へ排出する。
これにより、濾過器2内及びカチオン交換塔4内と空気洗浄工程1,2で洗浄できなかった配管13,23部分を洗浄し、汚染物を系外へ排出することができる。
In the backwash process, the backwash inlet valves V 5 and V 13 and the backwash outlet valves V 4 and V 8 are opened, the other valves are closed, and the backwash pumps P 2 and P 3 are activated and the raw water pump P 1 is stopped. The backwash water from outside the system is caused to flow back to the filter 2 via the pipe 19 and the pipe 14, and the backwash waste water is discharged outside the system via the pipe 13 and the pipe 17. Further, the backwash water is caused to flow back to the cation exchange tower 4 through the pipes 30 and 24 and discharged out of the system through the pipes 23 and 22.
As a result, the inside of the filter 2 and the cation exchange tower 4 and the pipes 13 and 23 that could not be washed in the air washing steps 1 and 2 can be washed, and the contaminants can be discharged out of the system.

なお、上記濾過器2の逆洗とカチオン交換塔4の逆洗は同時に行ってもよく、別々に行ってもよい。別々に行う場合、どちらを先に行ってもよい。
また、配管23及びカチオン交換塔4は、原水よりも微生物増殖の問題の少ない濾過処理水が流通するため、これらは、配管13や濾過器2ほど頻繁に空気洗浄を行う必要はないことから、このカチオン交換塔4及びその給水配管となる配管23の逆洗は適宜省略したり、配管13や濾過器2の逆洗よりも低頻度で行ってもよい。
The backwashing of the filter 2 and the backwashing of the cation exchange column 4 may be performed simultaneously or separately. When performed separately, either may be performed first.
In addition, since the pipe 23 and the cation exchange tower 4 circulate filtered water having less problem of microbial growth than the raw water, they do not need to be cleaned as frequently as the pipe 13 and the filter 2. The back washing of the cation exchange tower 4 and the pipe 23 serving as the water supply pipe may be omitted as appropriate, or may be performed less frequently than the back washing of the pipe 13 and the filter 2.

(6) 休止工程3
上記逆洗工程後は、直ちに濾過運転を再開しても良く、後述の仕上げ洗浄工程1,2や空気洗浄工程3を行った後、水処理運転を再開しても良く、水処理運転又は後述の洗浄工程との間に休止工程を介在させても良い。
休止工程の有無は、洗浄効果に特に影響しない。休止工程を行なう場合は、すべての弁を閉とすると共に、原水ポンプP、逆洗ポンプP,Pを停止する。
(6) Pause process 3
After the back washing step, the filtration operation may be resumed immediately, and after performing the finishing washing steps 1 and 2 and the air washing step 3 described later, the water treatment operation may be resumed. A pause process may be interposed between the cleaning process and the cleaning process.
The presence or absence of the pause process does not particularly affect the cleaning effect. When performing the pause process, all the valves are closed and the raw water pump P 1 and the backwash pumps P 2 and P 3 are stopped.

(7) 仕上げ洗浄工程1,2(図15,16)
濾過器2の仕上げ洗浄を行う場合は、図1〜10の濾過装置の場合と同様に、濾過入口弁V及び洗浄出口弁Vを開、その他の弁を閉とし、原水ポンプP作動、逆洗ポンプP,P停止として、原水槽1内の原水を配管11、配管12及び配管13を経て濾過器2に導入し、配管14、配管20及び配管17を経て系外へ排出する(図15)。
(7) Finishing cleaning steps 1 and 2 (Figs. 15 and 16)
When performing finish washing of the filter 2, as in the case of the filtration apparatus of FIGS. 1-10, the filtered inlet valve V 2 and washed outlet valve V 6 is opened, other valves were closed, the raw water pump P 1 operates As the backwash pumps P 2 and P 3 are stopped, the raw water in the raw water tank 1 is introduced into the filter 2 through the pipe 11, the pipe 12 and the pipe 13, and is discharged out of the system through the pipe 14, the pipe 20 and the pipe 17. (FIG. 15).

また、カチオン交換塔4の仕上げ洗浄を行う場合は、濾過入口弁V及び濾過出口弁V とカチオン交換入口弁V10及び洗浄出口弁V12を開、その他の弁を閉とし、原水ポンプP作動、逆洗ポンプP,P停止として、原水槽1内の原水を配管11、配管12及び配管13を経て濾過器2に導入し、更に配管14、配管15、及び配管23を経て、カチオン交換塔4に導入した後、配管24、配管29及び配管22を経て系外へ排出する。  In addition, when the cation exchange tower 4 is subjected to final cleaning, the filtration inlet valve V2And filtration outlet valve V 3And cation exchange inlet valve V10And washing outlet valve V12Open the other valve and close the raw water pump P1Operation, backwash pump P2, P3As a stop, the raw water in the raw water tank 1 is introduced into the filter 2 through the piping 11, the piping 12 and the piping 13, and further introduced into the cation exchange tower 4 through the piping 14, the piping 15 and the piping 23, and then the piping. 24, discharged through the piping 29 and the piping 22 to the outside of the system.

上記一連の洗浄工程を経た後は、再び濾過入口弁V及び濾過出口弁Vとカチオン交換入口弁V10及びカチオン交換出口弁V15を開、その他の弁を閉、原水ポンプP作動、逆洗ポンプP,P停止として、原水の水処理運転を再開する。After a series of the above washing step, the filtration inlet valve V 2 and filtration outlet valve V 3 and the cation exchange inlet valves V 10 and cation exchange outlet valve V 15 opens again, the other valves closed, the raw water pump P 1 operates As the backwash pumps P 2 and P 3 are stopped, the water treatment operation of the raw water is resumed.

なお、カチオン交換塔のようにカチオン交換樹脂が充填されたイオン交換塔では、塔内のカチオン交換樹脂により微生物の増殖に必要な微量金属イオンが除去されるため、イオン交換塔以降の配管については微生物の増殖が問題となることはない。従って、イオン交換塔のイオン交換処理水が流通する配管については、特に空気洗浄を行う必要はないが、微生物増殖の可能性が全くないとは言えないため、必要に応じて、或いは、他の洗浄工程よりもごく低い洗浄頻度で、イオン交換塔以降の配管についても空気洗浄を行ってもよい。  In addition, in an ion exchange tower packed with a cation exchange resin such as a cation exchange tower, trace metal ions necessary for the growth of microorganisms are removed by the cation exchange resin in the tower. Microbial growth is not a problem. Therefore, the pipe through which the ion exchange treated water of the ion exchange tower circulates does not need to be washed with air in particular, but it cannot be said that there is no possibility of microbial growth. Air cleaning may also be performed on the pipes after the ion exchange tower at a cleaning frequency much lower than that in the cleaning step.

図11〜17に示す水処理装置は、そのための空気注入配管31を設けたものであり、カチオン交換処理水配管を空気洗浄する際には、図17に示す如く、濾過入口弁V、濾過出口弁V、カチオン交換入口弁V10、カチオン交換出口弁V15、空気入口弁V 及び洗浄出口弁V11を開、その他の弁を閉とし、原水ポンプP作動させて(逆洗ポンプP,Pは停止)、原水槽1内の原水を配管11、配管12、及び配管13を経て濾過器2に導入し、濾過器2の濾過処理水を配管14、配管15、及び配管23を経てカチオン交換塔4に導入し、配管24,25からのカチオン交換処理水を、空気注入配管31からの空気と共に空気混合水として配管26を通すことによりカチオン交換処理水配管26を空気洗浄し、洗浄排水を配管28から系外へ排出する。Water treatment apparatus shown in FIG. 11 to 17, which has provided the air injection pipe 31 therefor when the air wash is a cation exchange treated water pipe, as shown in FIG. 17, filtered inlet valve V 2, filtered outlet valve V 3, the cation exchange inlet valves V 10, cation exchange outlet valve V 15, the air inlet valve V 1 4 and the cleaning outlet valve V 11 open, other valves were closed, while the raw water pump P 1 is actuated (reverse The washing pumps P 2 and P 3 are stopped), the raw water in the raw water tank 1 is introduced into the filter 2 through the pipe 11, the pipe 12, and the pipe 13, and the filtered water of the filter 2 is supplied to the pipe 14, the pipe 15, The cation exchange treated water pipe 26 is introduced into the cation exchange tower 4 through the pipe 23 and the cation exchange treated water from the pipes 24 and 25 is passed through the pipe 26 as air mixed water together with the air from the air injection pipe 31. Air wash, The purification waste water is discharged from the pipe 28 to the outside of the system.

このカチオン交換処理水配管26の空気洗浄に際しても、原水槽1からの原水を濾過処理及びカチオン交換処理して得られた処理水に限らず、系外からの工水等の水を用いて空気洗浄してもよく、また、処理水槽3内の水で空気洗浄してもよい。  The air washing of the cation exchange treated water pipe 26 is not limited to the treated water obtained by subjecting the raw water from the raw water tank 1 to the filtration treatment and the cation exchange treatment, and air using water such as industrial water from outside the system. You may wash | clean and air wash with the water in the treated water tank 3.

なお、空気注入配管31は逆洗水配管30に接続して、系外からの水を用いた空気混合水でカチオン交換処理水配管を洗浄するようにしてもよい。  The air injection pipe 31 may be connected to the backwash water pipe 30 to wash the cation exchange treated water pipe with air mixed water using water from outside the system.

[空気洗浄条件]
濾過器やカチオン交換塔等の水処理装置の給水配管を洗浄する前述の空気洗浄工程1において、空気の注入量が少ないと微生物の剥離効果が弱く、十分な洗浄効果を得るためには、空気洗浄工程を長くする必要が生じ、運転効率が低下すると共に、排水量が増えて好ましくない。しかし、空気注入量を多くすると、圧縮空気注入のためのコンプレッサー等の装置の大型化、消費電力の増加など、経済性が損なわれる。従って、空気注入量、空気洗浄工程の洗浄時間は、洗浄コストを抑えた上で高い洗浄効果が得られるように調整することが望ましい。
[Air cleaning conditions]
In the above-described air cleaning step 1 for cleaning the water supply piping of a water treatment device such as a filter or a cation exchange tower, if the amount of injected air is small, the effect of removing microorganisms is weak, and in order to obtain a sufficient cleaning effect, It is not preferable because the cleaning process needs to be lengthened, the operation efficiency is lowered, and the amount of drainage is increased. However, if the air injection amount is increased, the economic efficiency is impaired such as an increase in the size of a device such as a compressor for injecting compressed air and an increase in power consumption. Therefore, it is desirable to adjust the air injection amount and the cleaning time of the air cleaning process so that a high cleaning effect can be obtained while suppressing the cleaning cost.

本発明における空気洗浄工程1において、空気の注入量は洗浄対象の給水配管の配管断面積1cm当たり4〜10L/min、好ましくは4〜5L/minで、また、空気洗浄工程の洗浄時間は、下記式(I)で算出される基準時間T(分)の3倍以上であることが好ましい。
T={S×L×0.001/W} …(I)
(ただし、Sは給水配管の断面積(cm)、Lは空気混合水が流れる給水配管の長さ(図1における給水配管12の長さ)(cm)、Wは洗浄時の通水量(L/min)である。)
In the air cleaning step 1 of the present invention, the amount of air injected is 4 to 10 L / min, preferably 4 to 5 L / min per 1 cm 2 of the cross-sectional area of the water supply pipe to be cleaned, and the cleaning time of the air cleaning step is The reference time T (minute) calculated by the following formula (I) is preferably three times or more.
T = {S × L × 0.001 / W} (I)
(Where S is the cross-sectional area of the water supply pipe (cm 2 ), L is the length of the water supply pipe through which the air-mixed water flows (length of the water supply pipe 12 in FIG. 1) (cm), W is the amount of water flow during cleaning ( L / min).)

空気注入量が上記範囲よりも少ないと十分な洗浄効果が得られず、多いと不経済である。  If the air injection amount is less than the above range, a sufficient cleaning effect cannot be obtained, and if it is large, it is uneconomical.

また、洗浄時間が、上記基準時間Tの3倍未満では十分な洗浄効果が得られない。ただし、洗浄時間が過度に長くても不利であるため、洗浄時間は、上記基準時間Tの5倍以下とすることが好ましい。  Further, if the cleaning time is less than three times the reference time T, a sufficient cleaning effect cannot be obtained. However, since it is disadvantageous even if the cleaning time is excessively long, the cleaning time is preferably set to be not more than 5 times the reference time T.

なお、空気洗浄時の通水速度は、通常0.5〜2m/s程度とされ、空気洗浄時の通水量は配管の断面積によって異なる。  In addition, the water flow rate at the time of air washing is normally set to about 0.5 to 2 m / s, and the amount of water flow at the time of air washing varies depending on the cross-sectional area of the pipe.

逆洗水配管や処理水配管の空気洗浄を行う空気洗浄工程2,3における空気洗浄条件については、これらの配管が給水配管ほど微生物の増殖の問題がないことから、給水配管の空気洗浄条件よりも洗浄力の低い洗浄条件でもよく、また、空気洗浄工程1の洗浄条件と同等で行ってもよい。  Regarding the air cleaning conditions in the air cleaning processes 2 and 3 for performing air cleaning of the backwash water pipe and the treated water pipe, these pipes are less prone to microbial growth than the water supply pipes. May be performed under the same cleaning conditions as in the air cleaning step 1.

例えば、本発明における空気洗浄工程2,3において、空気の注入量は洗浄対象の逆洗水配管又は処理水配管の配管断面積1cm当たり4〜10L/minで、また、空気洗浄工程の洗浄時間は、下記式(I’)で算出される基準時間T’(分)の3倍以上であることが好ましい。
T’={S’×L’×0.001/W’} …(I’)
(ただし、S’は逆洗水配管又は処理水配管の断面積(cm)、L’は空気混合水が流れる逆洗水配管又は処理水配管の長さ(図1における配管19,15の長さ)(cm)、W’は洗浄時の通水量(L’/min)である。)
For example, in the air cleaning steps 2 and 3 in the present invention, the air injection amount is 4 to 10 L / min per 1 cm 2 of the cross-sectional area of the backwash water pipe or the treated water pipe to be cleaned. The time is preferably at least three times the reference time T ′ (minute) calculated by the following formula (I ′).
T ′ = {S ′ × L ′ × 0.001 / W ′} (I ′)
(However, S ′ is the cross-sectional area (cm 2 ) of the backwash water pipe or treated water pipe, and L ′ is the length of the backwash water pipe or treated water pipe through which the air-mixed water flows (the pipes 19 and 15 in FIG. 1). (Length) (cm), W ′ is the amount of water flow (L ′ / min) during cleaning.)

空気注入量が上記範囲よりも少ないと十分な洗浄効果が得られず、多いと不経済である。  If the air injection amount is less than the above range, a sufficient cleaning effect cannot be obtained, and if it is large, it is uneconomical.

また、洗浄時間が、上記基準時間T’の3倍未満では十分な洗浄効果が得られない。ただし、洗浄時間が過度に長くても不利であるため、洗浄時間は、上記基準時間T’の5倍以下とすることが好ましい。  Further, if the cleaning time is less than 3 times the reference time T ′, a sufficient cleaning effect cannot be obtained. However, since it is disadvantageous that the cleaning time is excessively long, it is preferable that the cleaning time is not more than 5 times the reference time T ′.

なお、空気洗浄時の通水速度は、通常0.5〜2m/s程度とされ、空気洗浄時の通水量は配管の断面積によって異なる。  In addition, the water flow rate at the time of air washing is normally set to about 0.5 to 2 m / s, and the amount of water flow at the time of air washing varies depending on the cross-sectional area of the pipe.

[各洗浄工程の時間]
本発明に係る上述の空気洗浄工程1〜3、逆洗工程、及び必要に応じて行われる仕上げ洗浄工程、休止工程の具体的な時間については特に制限はないが、通常、次のような時間とすることが好ましい。
[Time for each cleaning step]
There are no particular restrictions on the specific times of the air washing steps 1 to 3, the back washing step, and the finishing washing step and the pause step performed as necessary according to the present invention. It is preferable that

空気洗浄工程1:1〜10分
空気洗浄工程2,3:1〜10分
逆洗工程:5〜15分
休止工程:5分以下
仕上げ洗浄工程:5〜10分
Air washing process 1: 1 to 10 minutes Air washing process 2, 3: 1 to 10 minutes Back washing process: 5 to 15 minutes Pause process: 5 minutes or less Finish washing process: 5 to 10 minutes

[水処理装置の処理対象原水]
このような本発明の水処理装置給水配管の洗浄方法は、微生物が増殖し易い、有機物を多く含む排水、特に微生物の栄養塩となるリン及び/又は窒素を含む排水を処理する水処理装置の給水配管の洗浄に有効であり、適用される有機物含有排水の水質としては、例えば次のようなものが挙げられる。
[Raw water to be treated by water treatment equipment]
Such a water treatment apparatus water supply pipe cleaning method of the present invention is a water treatment apparatus for treating wastewater containing a large amount of organic matter, in particular, phosphorus and / or nitrogen serving as nutrient salts of microorganisms, in which microorganisms are likely to grow. Examples of the water quality of the organic matter-containing wastewater that is effective for cleaning the water supply pipe and are applied include the following.

<有機物含有排水水質>
有機物濃度:0.1〜100mg/L(as TOC)
SS濃度;0〜10mg/L
リン濃度:0.1〜1000mg/L(as P)
窒素濃度:0.1〜20mg/L(as N)
<Organic-containing wastewater quality>
Organic substance concentration: 0.1 to 100 mg / L (as TOC)
SS concentration: 0 to 10 mg / L
Phosphorus concentration: 0.1 to 1000 mg / L (as P)
Nitrogen concentration: 0.1-20 mg / L (as N)

[水処理装置]
本発明で洗浄対象となる水処理装置の構成等には特に制限はなく、内部に水処理材が充填され、定期的に又は必要に応じて逆洗が行われる水処理装置本体と、その逆洗機構を備える水処理装置であれば、給水配管に空気注入配管を接続することにより、或いは更に処理水配管に空気注入配管を接続することにより、いずれも有効に適用することができる。
[Water treatment equipment]
There is no particular limitation on the configuration or the like of the water treatment device to be cleaned in the present invention, and the water treatment device main body filled with water treatment material and backwashed periodically or as necessary, and vice versa. Any water treatment apparatus provided with a washing mechanism can be effectively applied by connecting an air injection pipe to the water supply pipe, or by further connecting an air injection pipe to the treated water pipe.

また、水処理装置本体への通水方向にも特に制限はなく、上向流方式であっても、下向流方式で良い。  Moreover, there is no restriction | limiting in particular also in the water flow direction to a water treatment apparatus main body, Even if it is an upward flow system, a downward flow system may be sufficient.

また、水処理材についても、砂、アントラサイト、不活性樹脂の他、廃イオン交換樹脂等の各種の濾材を用いることができ、また、イオン交換樹脂や活性炭であっても良い。  As the water treatment material, various filter media such as sand, anthracite, inert resin, waste ion exchange resin and the like can be used, and ion exchange resin and activated carbon may be used.

本発明の水処理装置給水配管の洗浄方法が適用される水処理装置の水処理装置本体としては、次のようなものが挙げられるが、何らこれらに限定されるものではない。
(1) 内部に水処理材として濾材が充填された濾過器
(2) 内部に水処理材としてイオン交換樹脂が充填されたイオン交換塔
(3) 内部に水処理材としてイオン交換樹脂が充填された軟水器
(4) 内部に水処理材として活性炭が充填された活性炭塔
Examples of the water treatment apparatus main body of the water treatment apparatus to which the water treatment apparatus water supply pipe cleaning method of the present invention is applied include the following, but are not limited thereto.
(1) Filter with a filter medium filled as a water treatment material
(2) Ion exchange tower filled with ion exchange resin as water treatment material
(3) Water softener filled with ion exchange resin as water treatment material
(4) Activated carbon tower filled with activated carbon as water treatment material

以下に実験例及び実施例を挙げて本発明をより具体的に説明する。  Hereinafter, the present invention will be described in more detail with reference to experimental examples and examples.

[実験例1]
空気洗浄時の空気注入量、通水量、空気洗浄時間と、給水配管の長さとの関係を調べるために、15Aの透明塩化ビニル配管(断面積1.8cm)に有機物含有排水を通水し、2日に1回の頻度で空気を注入して空気洗浄する実験を行った。なお、有機物含有排水の通水量は8.3L/minで一定とし、空気注入量と注入時間(空気洗浄工程の時間)は、種々変更して行った。
[Experimental Example 1]
In order to investigate the relationship between the amount of injected air, the amount of water flow, the time of air cleaning, and the length of the water supply pipe, the organic wastewater was passed through a 15A clear polyvinyl chloride pipe (cross-sectional area 1.8 cm 2 ). An experiment was conducted in which air was injected once every two days for air cleaning. In addition, the water flow rate of the organic substance-containing waste water was made constant at 8.3 L / min, and the air injection amount and the injection time (time of the air cleaning step) were variously changed.

この実験を2ヶ月行った後、空気注入点からの距離が5m、15m、30mの各ポイントで、配管内壁の微生物の付着状況を目視にて観察し、微生物の付着が認められず十分な洗浄効果が得られている場合は「○」、微生物の付着が認められ、洗浄効果が十分でない場合は「×」として評価し、結果を表1〜3に示した。  After conducting this experiment for 2 months, the distance from the air injection point is 5 m, 15 m, and 30 m, and visually observe the state of microorganisms on the inner wall of the pipe. When the effect was acquired, it was evaluated as “◯”, the adhesion of microorganisms was observed, and when the cleaning effect was not sufficient, it was evaluated as “x”, and the results are shown in Tables 1 to 3.

表1〜3より、十分な空気洗浄効果を得るための空気注入量や空気洗浄時間には下限があり、洗浄時間については、T={配管断面積(1.8cm)×配管長(500cm、1500cm又は3000cm)×0.001÷通水量(8.3L/min)}(分)の3倍以上とすることが好ましいことが分かる。From Tables 1 to 3, there are lower limits to the air injection amount and the air cleaning time for obtaining a sufficient air cleaning effect. The cleaning time is T = {pipe cross-sectional area (1.8 cm 2 ) × pipe length (500 cm (1500 cm or 3000 cm) × 0.001 ÷ water flow rate (8.3 L / min)} (min) It is understood that it is preferably 3 times or more.

Figure 2009116479
Figure 2009116479

Figure 2009116479
Figure 2009116479

Figure 2009116479
Figure 2009116479

[実施例1]
下記水質の濾過原水を濾過処理している図1の濾過装置(濾材:アンスラサイト)において、ポンプと弁の開閉を下記表4に示すタイムチャートで行って、空気洗浄工程1、休止工程1、空気洗浄工程2、休止工程2、逆洗工程、休止工程3、及び仕上げ洗浄工程の一連の洗浄を、原水の濾過運転2日毎に1回の頻度で行った。
[Example 1]
In the filtration device (filter medium: anthracite) of FIG. 1 that is filtering raw water of the following water quality, the pump and valve are opened and closed according to the time chart shown in Table 4 below, and the air washing step 1, the pause step 1, A series of washings of the air washing step 2, the pause step 2, the back washing step, the pause step 3, and the finish washing step was performed once every two days of the raw water filtration operation.

<濾過原水水質>
有機物濃度:5mg/L(as TOC)
SS濃縮:1mg/L
リン濃度:500mg/L(as P)
窒素濃度:5mg/L(as N)
<Filtration raw water quality>
Organic substance concentration: 5 mg / L (as TOC)
SS concentration: 1 mg / L
Phosphorus concentration: 500 mg / L (as P)
Nitrogen concentration: 5 mg / L (as N)

Figure 2009116479
Figure 2009116479

なお、給水配管の断面積は1.8cm、空気混合水が通水される給水配管の長さ(配管12の長さ)は500cm、非空気洗浄部の給水配管の長さ(配管13の長さ)は20cmであり、濾過時通水量は2L/min、空気注入量は4L/min、逆洗時通水量は2L/minとした(基準時間Tは0.45分)。The cross-sectional area of the water supply pipe is 1.8 cm 2 , the length of the water supply pipe through which the air-mixed water is passed (the length of the pipe 12) is 500 cm, and the length of the water supply pipe of the non-air cleaning unit (the pipe 13). The length) was 20 cm, the water flow rate during filtration was 2 L / min, the air injection rate was 4 L / min, and the water flow rate during backwashing was 2 L / min (reference time T was 0.45 minutes).

また、逆洗配管の断面積は1.8cm、処理水配管の断面積は1.8cm、空気混合水が通水される逆洗給水配管及び処理水配管の長さ(配管19及び配管15の合計の長さ)は500cm、非空気洗浄部の処理水配管14の長さは10cm、配管23の長さは5cmであり、空気洗浄工程2における処理水通水量は2L/min、空気注入量は4L/minとした(基準時間T’は0.45分)。The cross-sectional area of the backwash pipe is 1.8 cm 2 , the cross-sectional area of the treated water pipe is 1.8 cm 2 , and the length of the backwash water supply pipe and the treated water pipe through which the air-mixed water is passed (pipe 19 and the pipe 15) is 500 cm, the length of the treated water pipe 14 of the non-air washing unit is 10 cm, the length of the pipe 23 is 5 cm, the treated water flow rate in the air washing step 2 is 2 L / min, air The injection amount was 4 L / min (reference time T ′ was 0.45 minutes).

その結果、6ヵ月の運転を継続した後も、給水配管に微生物の付着、増殖は認められず、安定に運転を継続することができた。  As a result, even after the operation was continued for 6 months, the microorganisms did not adhere to or grow on the water supply pipe, and the operation could be continued stably.

本発明を特定の態様を用いて詳細に説明したが、本発明の意図と範囲を離れることなく様々な変更が可能であることは当業者に明らかである。
なお、本出願は、2008年3月21日付で出願された日本特許出願(特願2008−073918)に基づいており、その全体が引用により援用される。
Although the present invention has been described in detail using specific embodiments, it will be apparent to those skilled in the art that various modifications can be made without departing from the spirit and scope of the invention.
In addition, this application is based on the Japanese patent application (Japanese Patent Application No. 2008-073918) for which it applied on March 21, 2008, The whole is used by reference.

Claims (11)

内部に水処理材が充填され、定期的又は必要に応じて逆洗が行われる水処理装置本体と、該水処理装置本体に原水を供給する給水配管と、該水処理装置本体から処理水を取り出す処理水配管と、該水処理装置本体に逆洗水を供給する逆洗水配管と、逆洗排水を系外へ排出する該給水配管に接続された逆洗排水配管とを有する水処理装置の該給水配管を洗浄する方法において、
該逆洗排水配管と該給水配管との該接続部よりも上流側に空気混合水を供給し、この空気混合水を、前記接続部を経て前記逆洗排水配管から排出する空気洗浄工程と、
その後、該水処理装置本体に逆洗水を供給し、該水処理装置本体からの逆洗排水を、前記接続部を経て前記逆洗排水配管から排出する逆洗工程と
によって該給水配管を洗浄することを特徴とする水処理装置給水配管の洗浄方法。
A water treatment device main body filled with water treatment material and backwashed periodically or as necessary, a water supply pipe for supplying raw water to the water treatment device main body, and treated water from the water treatment device main body A water treatment apparatus having a treated water pipe to be taken out, a backwash water pipe for supplying backwash water to the main body of the water treatment apparatus, and a backwash drainage pipe connected to the water supply pipe for discharging backwash wastewater to the outside of the system In the method of cleaning the water supply pipe of
An air washing step of supplying air-mixed water upstream of the connection between the backwash drainage pipe and the water supply pipe, and discharging the air-mixed water from the backwash drainage pipe through the connection;
Thereafter, backwash water is supplied to the main body of the water treatment device, and the backwater drainage from the main body of the water treatment device is washed out through the backwashing drainage pipe through the connecting portion and the water supply pipe is washed. A method for cleaning a water supply pipe of a water treatment device.
請求項1において、前記空気洗浄工程における前記給水配管への空気注入量が、該給水配管の断面積1cm当たり4〜10L/minであり、該空気洗浄工程の洗浄時間が、下記式(I)で算出される基準時間T(分)の3倍以上であることを特徴とする水処理装置給水配管の洗浄方法。
T={S×L×0.001/W} …(I)
(ただし、Sは給水配管の断面積(cm)、Lは空気混合水が流れる給水配管の長さ(cm)、Wは洗浄時の通水量(L/min)である。)
In Claim 1, the amount of air injected into the water supply pipe in the air cleaning step is 4 to 10 L / min per 1 cm 2 of the cross-sectional area of the water supply pipe, and the cleaning time of the air cleaning process is expressed by the following formula (I The water treatment apparatus water supply pipe cleaning method is characterized in that it is at least three times the reference time T (minutes) calculated in (1).
T = {S × L × 0.001 / W} (I)
(However, S is the cross-sectional area (cm 2 ) of the water supply pipe, L is the length (cm) of the water supply pipe through which the air-mixed water flows, and W is the water flow rate (L / min) during cleaning.)
請求項1又は2において、前記逆洗工程後に、前記給水配管を介して前記水処理装置本体に原水を供給し、該水処理装置本体からの流出水を系外に排出する仕上げ洗浄工程を行うことを特徴とする水処理装置給水配管の洗浄方法。  3. The finishing cleaning step according to claim 1 or 2, wherein after the back washing step, raw water is supplied to the main body of the water treatment device via the water supply pipe, and discharged water from the main body of the water treatment device is discharged out of the system. A method for cleaning a water supply pipe of a water treatment apparatus. 請求項1ないし3のいずれか1項において、更に、前記処理水配管に空気混合水を供給して系外へ排出する処理水配管空気洗浄工程を行うことを特徴とする水処理装置給水配管の洗浄方法。  The water treatment apparatus water supply pipe according to any one of claims 1 to 3, further comprising a process water pipe air cleaning step of supplying an air mixed water to the process water pipe and discharging it to the outside of the system. Cleaning method. 請求項1ないし5のいずれか1項において、前記水処理装置は、前記処理水配管からの処理水を貯留する処理水槽と、該処理水槽内の処理水を前記逆洗水として前記水処理装置本体に供給する逆洗水配管とを有し、前記逆洗工程に先立ち、該逆洗水配管に空気混合水を供給して系外へ排出する逆洗水配管空気洗浄工程を行うことを特徴とする水処理装置給水配管の洗浄方法。  6. The water treatment device according to claim 1, wherein the water treatment device stores the treated water from the treated water pipe, and the water treatment device uses the treated water in the treated water bath as the backwash water. A backwash water pipe for supplying to the main body, and performing a backwash water pipe air washing process for supplying air mixed water to the backwash water pipe and discharging it outside the system prior to the backwash process. A water treatment device water supply pipe cleaning method. 請求項5において、前記逆洗水配管は、前記水処理装置本体の処理水排出口近傍で前記処理水配管に接続されており、前記逆洗工程に先立ち、空気混合水を、該逆洗水配管から該処理水配管と逆洗水配管との接続部を経て該処理水配管に処理水流通方向に通水させた後系外へ排出する逆洗水配管及び処理水配管空気洗浄工程を行うことを特徴とする水処理装置給水配管の洗浄方法。  6. The backwash water pipe according to claim 5, wherein the backwash water pipe is connected to the treated water pipe in the vicinity of a treated water discharge port of the water treatment apparatus main body, and prior to the backwashing process, the mixed water is supplied with the backwash water. A backwash water pipe and a treated water pipe air washing process for discharging water from the pipe through the connecting portion of the treated water pipe and the backwash water pipe to the treated water pipe in the direction of the treated water flow and then discharging to the outside of the system is performed. A method for cleaning a water supply pipe of a water treatment apparatus. 請求項1ないし6のいずれか1項において、前記水処理装置本体は、内部に前記水処理材として濾材が充填された濾過器であることを特徴とする水処理装置給水配管の洗浄方法。  7. The water treatment apparatus water supply pipe cleaning method according to claim 1, wherein the water treatment apparatus main body is a filter in which a filter medium is filled as the water treatment material. 請求項1ないし6のいずれか1項において、前記水処理装置本体は、内部に前記水処理材としてイオン交換樹脂が充填されたイオン交換塔であることを特徴とする水処理装置給水配管の洗浄方法。  The water treatment device water supply pipe according to any one of claims 1 to 6, wherein the water treatment device main body is an ion exchange tower filled with an ion exchange resin as the water treatment material. Method. 請求項1ないし6のいずれか1項において、前記水処理装置本体は、内部に前記水処理材としてイオン交換樹脂が充填された軟水器であることを特徴とする水処理装置給水配管の洗浄方法。  7. The water treatment apparatus water supply pipe cleaning method according to claim 1, wherein the water treatment apparatus main body is a water softener filled with an ion exchange resin as the water treatment material. . 請求項1ないし6のいずれか1項において、前記水処理装置本体は、内部に前記水処理材として活性炭が充填された活性炭塔であることを特徴とする水処理装置給水配管の洗浄方法。  7. The water treatment device water supply pipe cleaning method according to any one of claims 1 to 6, wherein the water treatment device main body is an activated carbon tower filled with activated carbon as the water treatment material. 請求項1ないし10のいずれか1項において、前記原水が有機物含有水であることを特徴とする水処理装置給水配管の洗浄方法。  11. The water treatment apparatus water supply pipe cleaning method according to any one of claims 1 to 10, wherein the raw water is organic substance-containing water.
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PCT/JP2009/055004 WO2009116479A1 (en) 2008-03-21 2009-03-16 Method for washing water supply pipeline of water-treating system
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CN110102100B (en) * 2019-05-30 2021-04-23 王密 Aquaculture inlet tube filter screen clearance ware
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