JP4742671B2 - Water treatment method and apparatus by membrane filtration - Google Patents

Water treatment method and apparatus by membrane filtration Download PDF

Info

Publication number
JP4742671B2
JP4742671B2 JP2005143151A JP2005143151A JP4742671B2 JP 4742671 B2 JP4742671 B2 JP 4742671B2 JP 2005143151 A JP2005143151 A JP 2005143151A JP 2005143151 A JP2005143151 A JP 2005143151A JP 4742671 B2 JP4742671 B2 JP 4742671B2
Authority
JP
Japan
Prior art keywords
backwash
water
filtration
membrane
tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2005143151A
Other languages
Japanese (ja)
Other versions
JP2006314974A (en
Inventor
角川  功明
本山  信行
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP2005143151A priority Critical patent/JP4742671B2/en
Publication of JP2006314974A publication Critical patent/JP2006314974A/en
Application granted granted Critical
Publication of JP4742671B2 publication Critical patent/JP4742671B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Description

この発明は、上水道、下水道、工業用水または廃水処理水など、原水中に含まれる汚濁物質をろ過膜により分離除去して浄化処理する、膜ろ過による水処理方法および水処理装置に関する。   The present invention relates to a water treatment method and a water treatment apparatus by membrane filtration, in which contaminants contained in raw water such as water supply, sewerage, industrial water, or wastewater treatment water are separated and removed by a filtration membrane and purified.

ろ過膜を用いた水処理装置では、長時間の運転によってファウリングが起こり、ろ過性能が低下する。そのため運転サイクルにおいて、所定時間のろ過工程後に、物理洗浄を実施し、ファウリングを低減するようにしている。物理洗浄には、膜ろ過後の処理水を逆流させる逆流洗浄(逆洗)、膜の一次側での水流によるフラッシング、空気により膜を振動させるエアースクラビングなどがあり、物理的な作用によって付着物質を取り除いている。   In a water treatment apparatus using a filtration membrane, fouling occurs due to long-time operation, and the filtration performance deteriorates. Therefore, in the operation cycle, after a filtering process for a predetermined time, physical cleaning is performed to reduce fouling. Physical cleaning includes backflow cleaning (backwashing) that reverses the treated water after membrane filtration, flushing by water flow on the primary side of the membrane, and air scrubbing that vibrates the membrane with air. Has been removed.

逆洗や水流によるフラッシング等の場合、物理洗浄間隔を短くすることによりファウリング抑制の効果を向上することができるが、これら物理洗浄は処理した水を用いて洗浄することから、回収率(原水量に対する処理水量の比率)が低下するという課題がある。この観点から従来の運転においては、物理洗浄間隔と回収率とのバランスのよいところで運転されていた。   In the case of backwashing or flushing with water flow, the effect of suppressing fouling can be improved by shortening the physical cleaning interval. However, since these physical cleanings are performed using treated water, the recovery rate (raw material) There is a problem that the ratio of the amount of treated water to the amount of water decreases. From this point of view, in the conventional operation, the operation was performed at a good balance between the physical cleaning interval and the recovery rate.

回収率を向上する一つの方法として逆洗排水を再利用する方法がある(特許文献1参照)。特許文献1は、その要約の記載からも明らかなように、「洗浄排水中の濁質量が所定値を上回らない範囲で洗浄排水を洗浄水として再利用する。」旨を開示する。即ち、特許文献1に記載された発明の場合、洗浄に再利用した洗浄排水は、濁質量が所定値を上回った場合には、廃水として処理されており、廃水の量に応じて回収率が低い問題がある。   One method for improving the recovery rate is a method of reusing backwash wastewater (see Patent Document 1). As is clear from the summary description, Patent Document 1 discloses that “wash wastewater is reused as wash water in a range in which the turbid mass in the wash wastewater does not exceed a predetermined value”. That is, in the case of the invention described in Patent Document 1, the cleaning wastewater reused for cleaning is treated as wastewater when the turbid mass exceeds a predetermined value, and the recovery rate depends on the amount of wastewater. There is a low problem.

回収率をさらに向上する方法としては、逆洗排水を膜ろ過して処理水を得る方法または逆洗排水を膜ろ過した水を原水側に返送する(返送して原水に混合させた後に膜ろ過して処理水を得る)方法が知られている。また、上記のように、逆洗排水を膜ろ過する方法としては、次のような方法が提案されている。   As a method of further improving the recovery rate, a method of obtaining treated water by membrane filtration of backwash wastewater or returning water obtained by membrane filtration of backwash wastewater to the raw water side (membrane filtration after returning and mixing with raw water) To obtain treated water). Further, as described above, the following method has been proposed as a method for membrane filtration of backwash wastewater.

その一つは、原水を膜ろ過する装置とは別にもう一台膜ろ過装置を設置する方法(所謂、2段ろ過方法)である。この場合は、設置スペースが増えることや装置増設によるメンテナンスの増加などの問題があった。もう一つの方法としは、本願発明者等が、特願2003−305705号によって出願した方法であって、逆洗排水を膜ろ過工程の開始時に原水に先立ってろ過する方法である。この方法は逆洗排水を膜ろ過することにより回収率を上げるのみならず、逆洗排水中の凝集フロックにより膜目詰まりをも抑制できるメリットを有した運転方法(所謂、プレコートろ過方法)であるが、この方法においても、以下のような問題があった。即ち、逆洗排水を膜ろ過した水は水道水質基準を満足する清澄な原水ではあるが、ろ過膜から異物を剥離させた逆洗排水、すなわち汚れた逆洗排水をろ過して得られた水を処理水とすることになるので、処理水のユーザーにとっては、衛生面、精神面でのマイナスイメージがあり、普及を妨げる要因となっていた。
特開2002−224542号公報
One of them is a method (so-called two-stage filtration method) in which another membrane filtration device is installed separately from the device for membrane filtration of raw water. In this case, there are problems such as an increase in installation space and an increase in maintenance due to the expansion of the apparatus. Another method is a method applied by the inventors of the present invention according to Japanese Patent Application No. 2003-305705, in which backwash wastewater is filtered prior to raw water at the start of a membrane filtration step. This method is an operation method (so-called precoat filtration method) having the merit of not only increasing the recovery rate by membrane filtration of the backwash wastewater but also suppressing membrane clogging by the coagulation flock in the backwash wastewater. However, this method also has the following problems. In other words, water obtained by membrane filtration of backwash wastewater is clear raw water that satisfies the tap water quality standards, but water obtained by filtering backwash wastewater from which foreign matters have been peeled off from the filtration membrane, that is, dirty backwash wastewater. Therefore, for users of treated water, there is a negative image in terms of hygiene and spirit, which has been a factor that hinders its spread.
JP 2002-224542 A

この発明は、上記のような問題点に鑑みてなされたもので、この発明の課題は、逆洗排水を膜ろ過して再利用することにより、水処理の回収率向上を図り、かつ、省スペースでありながら処理水としての衛生面等の問題を解消した膜ろ過による水処理方法および装置を提供することにある。   The present invention has been made in view of the above-described problems, and an object of the present invention is to improve the recovery rate of water treatment by recycling the backwash wastewater by membrane filtration and saving the wastewater. An object of the present invention is to provide a water treatment method and apparatus by membrane filtration that solves problems such as sanitary aspects as treated water in a space.

前述の課題を解決するため、この発明は、ろ過膜を有する膜モジュールと、前記膜モジュールの2次側に連通し逆洗水を貯留する逆洗水タンクと、前記膜モジュールの1次側から排出された逆洗排水を貯留する逆洗排水回収タンクと、原水を貯留する原水タンクの原水または前記逆洗排水回収タンクの逆洗排水を前記膜モジュールの1次側へ供給する主ポンプと、前記逆洗水タンクの逆洗水を前記膜モジュールの2次側へ供給する逆洗ポンプと、前記膜モジュールの2次側に連通し前記逆洗水タンクに逆洗水を供給するラインと、前記膜モジュールの2次側に連通し前記逆洗水タンクを経由しないで処理水を取り出すラインとを備え、前記逆洗水を供給するラインと前記処理水を取り出すラインを切り替え可能な水処理装置の水処理方法において、原水をろ過膜の1次側から2次側へろ過して前記逆洗水タンクを経由しないで処理水を得る原水ろ過工程と、前記処理水を取り出すラインを止めて逆洗水を供給するラインを開けて逆洗水タンクに貯留した逆洗水で前記ろ過膜の2次側から1次側へ逆洗して前記2次側から排出される逆洗排水を逆洗排水回収タンクに貯留する逆洗工程と、前記逆洗排水回収タンクに貯留した逆洗排水のみを、前記ろ過膜の1次側から2次側へろ過して前記逆洗水タンクに貯留する逆洗排水ろ過工程とを順に行い、前記逆洗排水ろ過工程後に前記原水ろ過工程に戻ることを特徴とする(請求項1の発明)。 In order to solve the above-described problems, the present invention includes a membrane module having a filtration membrane, a backwash water tank that communicates with the secondary side of the membrane module and stores backwash water, and a primary side of the membrane module. A main pump for supplying the backwash wastewater recovery tank for storing the drained backwash wastewater, the raw water for storing the raw water or the backwash wastewater for the backwash wastewater recovery tank to the primary side of the membrane module; A backwash pump for supplying backwash water from the backwash water tank to the secondary side of the membrane module; a line for communicating backwash water to the secondary side of the membrane module; A water treatment device comprising a line that communicates with the secondary side of the membrane module and takes out treated water without going through the backwash water tank, and is capable of switching between a line that supplies the backwash water and a line that takes out the treated water Water treatment method The raw water is filtered from the primary side to the secondary side of the filtration membrane to obtain treated water without going through the backwash water tank, and the backwash water is supplied by stopping the line for taking out the treated water. Backwash water stored in the backwash water tank and backwashed from the secondary side of the filtration membrane to the primary side and discharged from the secondary side into the backwash drainage recovery tank. A backwashing step of storing, and a backwashing drainage filtration step of filtering only the backwashing wastewater stored in the backwashing wastewater recovery tank from the primary side to the secondary side of the filtration membrane and storing it in the backwashing water tank. And the process returns to the raw water filtration step after the backwash drainage filtration step (invention of claim 1).

上記発明によれば、逆洗排水はろ過膜により膜ろ過して逆洗水タンクに貯留し、逆洗に再利用するのみで処理水としてユーザーに供されることはないので、前述の処理水としての衛生面等の問題が解消できる。さらに、前記2段ろ過方法とは異なり、原水ろ過用のろ過膜により逆洗排水をろ過するので、省スペースにも拘らず、回収率の向上と衛生面等の問題の解消が実現できる。   According to the above invention, the backwash wastewater is filtered through a filtration membrane and stored in the backwash water tank, and only reused for backwashing and not provided to the user as treated water. As a result, problems such as hygiene can be solved. Further, unlike the two-stage filtration method, the backwash wastewater is filtered by a raw water filtration membrane, so that it is possible to realize improvement in recovery rate and elimination of problems such as hygiene in spite of space saving.

また、上記請求項1の発明の実施態様としては、下記請求項2ないし3の発明が好ましい。即ち、前記請求項1に記載の水処理方法において、前記逆洗排水ろ過工程と前記原水ろ過工程との間に、前記原水を前記ろ過膜の1次側から2次側へろ過して前記ろ過膜に残留している水を前記逆洗水タンクへ通水し、残留逆洗水排水工程を行うこととする(請求項2の発明)。 As an embodiment of the invention of claim 1, the inventions of claims 2 to 3 are preferable. That is, in the water treatment method according to claim 1, the raw water is filtered from the primary side to the secondary side of the filtration membrane between the backwash drainage filtration step and the raw water filtration step. The water remaining in the membrane is passed through the backwash water tank, and the residual backwash water draining step is performed (invention of claim 2).

さらに、前記請求項1または2に記載の水処理方法において、前記逆洗工程と前記逆洗排水ろ過工程を入れ替えることとする(請求項3の発明) Furthermore, in the water treatment method according to claim 1 or 2, the backwashing step and the backwash drainage filtration step are interchanged (invention of claim 3) .

また、上記水処理方法を実施するための水処理装置の発明としては、下記請求項4の発明が好ましい。即ち、前記請求項1ないし3のいずれか1つに記載の水処理方法を実施するための装置であって、原水を貯留する原水タンクと、ろ過膜を有する膜モジュールと、
前記膜モジュールの2次側に連通し逆洗水を貯留する逆洗水タンクと、前記膜モジュールの2次側に連通し前記逆洗水タンクに逆洗水を供給するラインと、前記膜モジュールの2次側に連通し前記逆洗水タンクを経由しないで処理水を取り出すラインと、前記逆洗水を供給するラインと前記処理水を取り出すラインを切り替えるバルブと、前記膜モジュールの1次側から排出された逆洗排水を貯留する逆洗排水回収タンクと、前記原水タンクの原水または前記逆洗排水回収タンクの逆洗排水を前記膜モジュールの1次側へ供給する主ポンプと、前記逆洗水タンクの逆洗水を前記膜モジュールの2次側へ供給する逆洗ポンプと、
を備えたことを特徴とする(請求項4の発明)。
Moreover, as invention of the water treatment apparatus for enforcing the said water treatment method, invention of the following Claim 4 is preferable. That is, an apparatus for carrying out the water treatment method according to any one of claims 1 to 3 , wherein a raw water tank for storing raw water, a membrane module having a filtration membrane,
A backwash water tank that communicates with the secondary side of the membrane module and stores backwash water, a line that communicates with the secondary side of the membrane module and supplies the backwash water to the backwash water tank, and the membrane module A line for communicating treated water without passing through the backwash water tank, a valve for switching between a line for supplying the backwash water and a line for removing the treated water, and a primary side of the membrane module A backwash wastewater recovery tank for storing backwash wastewater discharged from the main water tank, a main pump for supplying the raw water of the raw water tank or the backwash wastewater of the backwash wastewater recovery tank to the primary side of the membrane module, and the reverse A backwash pump for supplying backwash water from the wash tank to the secondary side of the membrane module;
(Invention of claim 4).

この発明によれば、膜ろ過による水処理方法および装置において、逆洗排水を膜ろ過して再利用することにより、水処理の回収率向上を図り、かつ、省スペースでありながら処理水としての衛生面等の問題を解消できる。   According to this invention, in the water treatment method and apparatus by membrane filtration, the backwash wastewater is membrane-filtered and reused to improve the recovery rate of water treatment, and as the treated water while saving space It can solve problems such as hygiene.

図1に基づき、本発明の実施の形態について以下に述べる。なお、本発明はこの実施例によって限定されるものではない。   An embodiment of the present invention will be described below based on FIG. In addition, this invention is not limited by this Example.

図1は、本発明の実施の形態に係る膜ろ過による水処理装置のシステム系統図である。図1において、1は原水、2は凝集剤PAC、3は硫酸、4は原水タンク、5は原水供給バルブ、6は逆洗排水供給バルブ、7は主ポンプ、8は膜モジュール、9は処理水バルブ、10は逆洗水バルブ、11は処理水、12は逆洗水、13は逆洗水タンク、14は逆洗ポンプ、15は逆洗バルブ、16は逆洗排水、17は逆洗排水回収タンク、18は原水返送ライン、19は捨水バルブ、20は汚泥を示す。なお、図1においては、捨水バルブ19の開閉を制御する制御装置の図示を省略している。   FIG. 1 is a system diagram of a water treatment apparatus using membrane filtration according to an embodiment of the present invention. In FIG. 1, 1 is raw water, 2 is flocculant PAC, 3 is sulfuric acid, 4 is raw water tank, 5 is raw water supply valve, 6 is backwash drainage supply valve, 7 is main pump, 8 is membrane module, 9 is treatment Water valve 10 is a backwash water valve, 11 is treated water, 12 is a backwash water, 13 is a backwash water tank, 14 is a backwash pump, 15 is a backwash valve, 16 is a backwash drain, 17 is a backwash A waste water recovery tank, 18 is a raw water return line, 19 is a drain valve, and 20 is sludge. In FIG. 1, illustration of a control device that controls opening and closing of the water discharge valve 19 is omitted.

次に、図1に示す膜ろ過による水処理装置のろ過工程と逆洗工程の流れ等について説明する。まず、ろ過工程について述べる。原水タンク4に流入した原水1に凝集剤PAC2とpH調整のための硫酸3を注入して攪拌された水を、ろ過膜への供給水として原水供給バルブ5を介して、主ポンプ7にて膜モジュール8へと通水する。膜ろ過された水は処理水バルブ9を介して処理水11として次工程へと供せられる。なお、初回のろ過工程においては、前記処理水の一部が、逆洗水12として逆洗水バルブ10を介して、逆洗水タンク13に貯留され、この貯留した水(逆洗水)を用いて所定の膜ろ過処理時間後にろ過膜の逆洗(初回の逆洗工程)を行う。   Next, the flow of the filtration process and backwashing process of the water treatment apparatus by membrane filtration shown in FIG. 1 will be described. First, the filtration process will be described. The water agitated by injecting the flocculant PAC2 and sulfuric acid 3 for pH adjustment into the raw water 1 flowing into the raw water tank 4 is supplied to the filtration membrane by the main pump 7 via the raw water supply valve 5. Water is passed through the membrane module 8. The membrane-filtered water is supplied to the next step as treated water 11 through the treated water valve 9. In the first filtration step, a part of the treated water is stored as backwash water 12 in the backwash water tank 13 via the backwash water valve 10, and this stored water (backwash water) is used. The filtration membrane is backwashed after the predetermined membrane filtration treatment time (first backwashing step).

初回の逆洗工程においては、従来の逆洗と同様に、逆洗水タンク13から逆洗バルブ15を介して逆洗ポンプ14により、膜モジュール8の二次側(処理水側)から一次側(原水側)に逆洗水を通流し、膜モジュール8からの逆洗排水16を逆洗排水回収タンク17に貯留する。この逆洗工程の後、再度、前記ろ過工程を行なう。   In the first backwashing process, the secondary side of the membrane module 8 (from the treated water side) to the primary side by the backwashing pump 14 from the backwashing water tank 13 through the backwashing valve 15 as in the conventional backwashing. The backwash water is passed through (raw water side), and the backwash drainage 16 from the membrane module 8 is stored in the backwash drainage recovery tank 17. After the back washing step, the filtration step is performed again.

次に、2回目以降の逆洗工程、即ち、逆洗排水を再利用する逆洗工程について述べる。   Next, the backwash process for the second and subsequent times, that is, the backwash process for reusing the backwash waste water will be described.

所定のろ過時間、例えば20分から120分のろ過時間が経過した時点で、原水供給バルブ5を閉じて逆洗排水供給バルブ6を開き、逆洗排水回収タンク17内の逆洗排水16を主ポンプ7にて膜モジュール8へと通水する工程へと切り替える。この時、処理水バルブ9は閉とする。そして、膜ろ過された水は逆洗水バルブ10を介して、逆洗水12として逆洗水タンク13へ貯留される。   When a predetermined filtration time, for example, 20 to 120 minutes, has passed, the raw water supply valve 5 is closed and the backwash drainage supply valve 6 is opened, and the backwash drainage 16 in the backwash drainage recovery tank 17 is supplied to the main pump. 7, the process is switched to the step of passing water to the membrane module 8. At this time, the treated water valve 9 is closed. The membrane-filtered water is stored in the backwash water tank 13 as backwash water 12 through the backwash water valve 10.

ここで、逆洗排水を再利用するために、逆洗排水回収タンク17内の逆洗排水16を膜モジュール8にてろ過して逆洗水12として逆洗水タンク13へ貯留する工程を実施する時期については、逆洗工程を開始する前までに実施していれば良いが、特に好ましい形態としては、上述した例のように、前記請求項の発明のようなタイミングで、逆洗排水回収タンク17内の逆洗排水16をろ過して逆洗水12として逆洗水タンク13へ貯留すれば良い。 Here, in order to reuse the backwash wastewater, the backwash wastewater 16 in the backwash wastewater recovery tank 17 is filtered through the membrane module 8 and stored as backwash water 12 in the backwash water tank 13. About the time to perform, what is necessary is just to have implemented before the start of the backwashing process, but as a particularly preferable form, as in the example described above, the backwash drainage is performed at the timing as in the invention of claim 3. The backwash waste water 16 in the recovery tank 17 may be filtered and stored in the backwash water tank 13 as backwash water 12.

なお、逆洗排水回収タンク17内の逆洗排水16をろ過する際に、逆洗排水回収タンク17内を攪拌して逆洗排水16を供給することが好ましい。   In addition, when filtering the backwash wastewater 16 in the backwash wastewater collection tank 17, it is preferable to stir the backwash wastewater collection tank 17 and supply the backwash wastewater 16.

所定時間逆洗排水16を膜ろ過した時点で、逆洗排水再利用のためのろ過工程を停止する。逆洗排水を膜ろ過する時間は逆洗に使用した水量をろ過する時間となるため膜ろ過流束に依存することとなり、その時間は通常であれば1分から10分の間となる。   When the backwash wastewater 16 is subjected to membrane filtration for a predetermined time, the filtration process for reusing the backwash wastewater is stopped. The time for membrane filtration of backwash wastewater is the time to filter the amount of water used for backwashing, and therefore depends on the membrane filtration flux, and the time is usually between 1 and 10 minutes.

逆洗排水を再利用するためのろ過工程に続いて、逆洗排水を再利用する逆洗工程を実施する。逆洗ポンプ14を用いて逆洗水タンク13内の水を逆洗バルブ15を介して膜モジュール8の二次側より一次側へと通水する。一次側より排出される逆洗排水16は、逆洗排水回収タンク17へ再び貯留されて次回の逆洗工程前に膜ろ過されるためにスタンバイする。なお、逆洗に使用する水量と逆洗排水の回収ろ過水量をなるべく等しくする方が運転は容易となる。   Following the filtration process for reusing the backwash wastewater, a backwash process for reusing the backwash wastewater is performed. Water in the backwash water tank 13 is passed from the secondary side of the membrane module 8 to the primary side through the backwash valve 15 using the backwash pump 14. The backwash wastewater 16 discharged from the primary side is stored again in the backwash wastewater recovery tank 17 and is put on standby because it is membrane filtered before the next backwash process. The operation becomes easier when the amount of water used for backwashing and the amount of recovered filtered water of backwash wastewater are made as equal as possible.

ところで逆洗排水は、回収膜ろ過する逆洗排水中の濁質量に加えて原水ろ過時に膜に補足される濁質分が増加することからその濃度の上昇を抑制することが必要となる。そのため、逆洗排水中の汚泥を重力沈降などにより5〜20倍に濃縮(原水性状および重力沈降時間により異なる)し、定期的に逆洗排水回収タンク17の下部より逆洗排水16の濃縮汚泥20を捨水バルブ19より引き抜いて汚泥処理などに供する。なお、捨水バルブ19の開閉制御は、図示しない制御装置により行う。開閉制御は、原水の水質が比較的安定している場合には、予め実験的に定めた所定の時間間隔による開閉制御とすることができるが、水質が比較的変動する場合には、例えば、逆洗排水回収タンク内に濁度計を設けて、濁度が所定値に到達した際に開閉制御するようにすることもできる。   By the way, in the backwash wastewater, in addition to the turbid mass in the backwash wastewater to be recovered and membrane filtered, the turbid component captured by the membrane during raw water filtration increases, so it is necessary to suppress the increase in concentration. Therefore, the sludge in the backwash drainage is concentrated 5 to 20 times by gravity sedimentation (depending on the raw water condition and the gravity sedimentation time), and the concentrated sludge of the backwash wastewater 16 is periodically fed from the lower part of the backwash wastewater recovery tank 17. 20 is pulled out from the water discharge valve 19 and used for sludge treatment or the like. In addition, opening / closing control of the water discharge valve 19 is performed by a control device (not shown). When the water quality of the raw water is relatively stable, the open / close control can be an open / close control with a predetermined time interval determined experimentally in advance, but when the water quality varies relatively, for example, It is also possible to provide a turbidity meter in the backwash waste water recovery tank so as to control opening and closing when the turbidity reaches a predetermined value.

また、重力沈降によって逆洗排水を濃縮することや高濁度時における引抜汚泥量を考慮して、逆洗排水回収タンク17の容量は、逆洗に使用する水量の2倍以上の大きさとすることが好ましく、許容できる範囲で大きいタンクとするのが好ましい。また、逆洗排水タンク17を複数個設置するようにしてもよい。   Also, considering the concentration of backwash wastewater by gravity sedimentation and the amount of extracted sludge at high turbidity, the capacity of the backwash wastewater recovery tank 17 is at least twice the amount of water used for backwashing. It is preferable to use a large tank within an allowable range. A plurality of backwash drainage tanks 17 may be installed.

上記逆洗排水を再利用する逆洗工程終了後に、再び原水のろ過工程へと移行するが、膜モジュール内には逆洗に使用された水が残留していることから、前記請求項の発明のように、ろ過開始直後の水は逆洗水バルブ10より逆洗水タンク13へと通水することが好ましい。また、別の方法として、上記逆洗排水を再利用する逆洗工程終了後に、先ず逆洗排水回収タンク17内の逆洗排水16を膜モジュール8にてろ過して逆洗水12として逆洗水タンク13へ貯留する工程を実施し、続いて再び原水のろ過工程へと移行する時に、前記請求項3の発明のように、ろ過開始直後の水は逆洗水バルブ10より逆洗水タンク13へと通水した後、処理水を得るための原水のろ過工程の実施に移行することもできる。
After backwashing process is completed to recycle the backwash waste water, the process proceeds back to raw water filtration process, but since it is in the membrane module remaining water used for backwash of claim 2 As in the invention, the water immediately after the start of filtration is preferably passed through the backwash water valve 10 to the backwash water tank 13. As another method, after the backwashing step for reusing the backwash wastewater, the backwash wastewater 16 in the backwash wastewater recovery tank 17 is first filtered through the membrane module 8 to obtain backwash water 12. When the process of storing in the water tank 13 is carried out and then the process proceeds to the raw water filtration process again, the water immediately after the start of filtration is supplied from the backwash water valve 10 to the backwash water tank as in the invention of claim 3. After passing through the water 13, the raw water filtering step for obtaining treated water can be carried out.

なお、逆洗水タンク13の容量が比較的小さい場合であって、逆洗水タンク13内の水がオーバーフローする場合には、原水返送ライン18より原水槽へと返送してもよい。ろ過膜の二次側に滞留している水は、逆洗排水をろ過した水であるが、これを原水槽へ返送して再度ろ過する場合には、精神面でのマイナスイメージの問題は生じないと考えられる。   In addition, when the capacity | capacitance of the backwash water tank 13 is comparatively small, and the water in the backwash water tank 13 overflows, you may return to a raw | natural water tank from the raw | natural water return line 18. FIG. The water staying on the secondary side of the filter membrane is the water from which the backwash wastewater is filtered. However, when this is returned to the raw water tank and filtered again, a mental negative image problem arises. It is not considered.

本発明の実施の形態に係る膜ろ過による水処理装置のシステム系統図。The system system | strain diagram of the water treatment apparatus by the membrane filtration which concerns on embodiment of this invention.

符号の説明Explanation of symbols

1:原水、4:原水タンク、5:原水供給バルブ、6:逆洗排水供給バルブ、7:主ポンプ、8:膜モジュール、9:処理水バルブ、10:逆洗水バルブ、11:処理水、12:逆洗水、13:逆洗水タンク、14:逆洗ポンプ、15:逆洗バルブ、16:逆洗排水、17:逆洗排水回収タンク、18:原水返送ライン、19:捨水バルブ、20:汚泥

1: Raw water, 4: Raw water tank, 5: Raw water supply valve, 6: Backwash drainage supply valve, 7: Main pump, 8: Membrane module, 9: Treated water valve, 10: Backwash water valve, 11: Treated water , 12: Backwash water, 13: Backwash water tank, 14: Backwash pump, 15: Backwash valve, 16: Backwash drainage, 17: Backwash drainage recovery tank, 18: Raw water return line, 19: Waste water Valve, 20: Sludge

Claims (4)

ろ過膜を有する膜モジュールと、A membrane module having a filtration membrane;
前記膜モジュールの2次側に連通し逆洗水を貯留する逆洗水タンクと、A backwash water tank that communicates with the secondary side of the membrane module and stores backwash water;
前記膜モジュールの1次側から排出された逆洗排水を貯留する逆洗排水回収タンクと、A backwash drainage recovery tank for storing backwash drainage discharged from the primary side of the membrane module;
原水を貯留する原水タンクの原水または前記逆洗排水回収タンクの逆洗排水を前記膜モジュールの1次側へ供給する主ポンプと、A main pump for supplying raw water from a raw water tank for storing raw water or backwash wastewater from the backwash wastewater recovery tank to the primary side of the membrane module;
前記逆洗水タンクの逆洗水を前記膜モジュールの2次側へ供給する逆洗ポンプと、A backwash pump for supplying backwash water from the backwash water tank to the secondary side of the membrane module;
前記膜モジュールの2次側に連通し前記逆洗水タンクに逆洗水を供給するラインと、A line that communicates with the secondary side of the membrane module and supplies backwash water to the backwash water tank;
前記膜モジュールの2次側に連通し前記逆洗水タンクを経由しないで処理水を取り出すラインとを備え、前記逆洗水を供給するラインと前記処理水を取り出すラインを切り替え可能な水処理装置の水処理方法において、A water treatment device comprising a line that communicates with the secondary side of the membrane module and takes out treated water without going through the backwash water tank, and is capable of switching between a line that supplies the backwash water and a line that takes out the treated water In the water treatment method of
原水をろ過膜の1次側から2次側へろ過して前記逆洗水タンクを経由しないで処理水を得る原水ろ過工程と、A raw water filtration step of filtering raw water from the primary side of the filtration membrane to the secondary side to obtain treated water without going through the backwash water tank;
前記処理水を取り出すラインを止めて逆洗水を供給するラインを開けて逆洗水タンクに貯留した逆洗水で前記ろ過膜の2次側から1次側へ逆洗して前記2次側から排出される逆洗排水を逆洗排水回収タンクに貯留する逆洗工程と、Stop the line for taking out the treated water, open the line for supplying backwash water, backwash from the secondary side of the filtration membrane to the primary side with the backwash water stored in the backwash water tank, and the secondary side A backwash process for storing backwash wastewater discharged from the backwash wastewater recovery tank;
前記逆洗排水回収タンクに貯留した逆洗排水のみを、前記ろ過膜の1次側から2次側へろ過して前記逆洗水タンクに貯留する逆洗排水ろ過工程とを順に行い、Only the backwash drainage stored in the backwash drainage recovery tank is filtered from the primary side to the secondary side of the filtration membrane and stored in the backwash water tank, and the backwash drainage filtration step is sequentially performed.
前記逆洗排水ろ過工程後に前記原水ろ過工程に戻ることを特徴とする膜ろ過による水処理方法。A water treatment method by membrane filtration, wherein the process returns to the raw water filtration step after the backwash drainage filtration step.
請求項1に記載の水処理方法において、The water treatment method according to claim 1,
前記逆洗排水ろ過工程と前記原水ろ過工程との間に、前記原水を前記ろ過膜の1次側から2次側へろ過して前記ろ過膜に残留している水を前記逆洗水タンクへ通水し、残留逆洗水排水工程を行うことを特徴とする膜ろ過による水処理方法。Between the backwash drainage filtration step and the raw water filtration step, the raw water is filtered from the primary side to the secondary side of the filtration membrane, and the water remaining on the filtration membrane is transferred to the backwash water tank. A water treatment method by membrane filtration, characterized by passing water and performing a residual backwash water drainage step.
請求項1または2に記載の水処理方法において、The water treatment method according to claim 1 or 2,
前記逆洗工程と前記逆洗排水ろ過工程を入れ替えたことを特徴とする膜ろ過による水処理方法。A water treatment method by membrane filtration, wherein the backwashing step and the backwashing drainage filtration step are interchanged.
請求項1ないし3のいずれか1つに記載の水処理方法を実施するための装置であって、An apparatus for carrying out the water treatment method according to any one of claims 1 to 3,
原水を貯留する原水タンクと、A raw water tank for storing raw water;
ろ過膜を有する膜モジュールと、A membrane module having a filtration membrane;
前記膜モジュールの2次側に連通し逆洗水を貯留する逆洗水タンクと、A backwash water tank that communicates with the secondary side of the membrane module and stores backwash water;
前記膜モジュールの2次側に連通し前記逆洗水タンクに逆洗水を供給するラインと、A line that communicates with the secondary side of the membrane module and supplies backwash water to the backwash water tank;
前記膜モジュールの2次側に連通し前記逆洗水タンクを経由しないで処理水を取り出すラインと、A line that communicates with the secondary side of the membrane module and removes treated water without going through the backwash water tank;
前記逆洗水を供給するラインと前記処理水を取り出すラインを切り替えるバルブと、A valve for switching a line for supplying the backwash water and a line for taking out the treated water;
前記膜モジュールの1次側から排出された逆洗排水を貯留する逆洗排水回収タンクと、A backwash drainage recovery tank for storing backwash drainage discharged from the primary side of the membrane module;
前記原水タンクの原水または前記逆洗排水回収タンクの逆洗排水を前記膜モジュールの1次側へ供給する主ポンプと、A main pump for supplying raw water in the raw water tank or backwash wastewater in the backwash wastewater recovery tank to the primary side of the membrane module;
前記逆洗水タンクの逆洗水を前記膜モジュールの2次側へ供給する逆洗ポンプと、A backwash pump for supplying backwash water from the backwash water tank to the secondary side of the membrane module;
を備えたことを特徴とする膜ろ過による水処理装置。A water treatment apparatus using membrane filtration, comprising:
JP2005143151A 2005-05-16 2005-05-16 Water treatment method and apparatus by membrane filtration Expired - Fee Related JP4742671B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2005143151A JP4742671B2 (en) 2005-05-16 2005-05-16 Water treatment method and apparatus by membrane filtration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2005143151A JP4742671B2 (en) 2005-05-16 2005-05-16 Water treatment method and apparatus by membrane filtration

Publications (2)

Publication Number Publication Date
JP2006314974A JP2006314974A (en) 2006-11-24
JP4742671B2 true JP4742671B2 (en) 2011-08-10

Family

ID=37536100

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2005143151A Expired - Fee Related JP4742671B2 (en) 2005-05-16 2005-05-16 Water treatment method and apparatus by membrane filtration

Country Status (1)

Country Link
JP (1) JP4742671B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7441108B2 (en) 2020-04-23 2024-02-29 オルガノ株式会社 Water treatment method and water treatment equipment

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06262173A (en) * 1993-03-15 1994-09-20 Daicel Chem Ind Ltd Membrane purifying method for surface water with improved recovery rate and operation method of its device
JP2001017966A (en) * 1999-07-09 2001-01-23 Hitachi Plant Eng & Constr Co Ltd Process and equipment for producing purified water
JP2004130197A (en) * 2002-10-09 2004-04-30 Fuji Electric Systems Co Ltd Water treatment method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06262173A (en) * 1993-03-15 1994-09-20 Daicel Chem Ind Ltd Membrane purifying method for surface water with improved recovery rate and operation method of its device
JP2001017966A (en) * 1999-07-09 2001-01-23 Hitachi Plant Eng & Constr Co Ltd Process and equipment for producing purified water
JP2004130197A (en) * 2002-10-09 2004-04-30 Fuji Electric Systems Co Ltd Water treatment method

Also Published As

Publication number Publication date
JP2006314974A (en) 2006-11-24

Similar Documents

Publication Publication Date Title
JP4920990B2 (en) Separation membrane cleaning method
JP5453711B2 (en) Cleaning method for external pressure hollow fiber membrane module
JP5245216B2 (en) Hollow fiber membrane water treatment method and water treatment apparatus
JP2019209324A (en) Wastewater treatment system and wastewater treatment method
JP4742671B2 (en) Water treatment method and apparatus by membrane filtration
JP2014091070A (en) Method for processing organic waste water
JP4569200B2 (en) Water treatment method and membrane filtration water treatment device operation method
JP2007330899A (en) Filtering system and its controlling method
JP2007301469A (en) Water treatment method
JP6101099B2 (en) Cleaning method for sand filter
JP3856376B2 (en) Water treatment device and its operation method
KR101162614B1 (en) Water reclamation and reusing equipment
KR100785911B1 (en) Equipment and method of thickening reuse drain water sand filters useing pipe membrane
JP2007111576A (en) Back-washing method of membrane module
JP5277519B2 (en) Water treatment method
CN211133571U (en) Circulating cleaning water tank of ultrafiltration system
KR100496878B1 (en) Apparatus for treating washing water in pretreating of plating process and method thereof
JP4125390B2 (en) Waste water recycling equipment
CN210065394U (en) Desulfurization waste water treatment equipment of self-cleaning
JP5165932B2 (en) Operation method of membrane treatment apparatus
JP2007245063A (en) Water treatment apparatus by filtration membrane, its operation method and washing method for filtration membrane
KR100210656B1 (en) The water purifier apparatus of a washing machine
KR20100004402A (en) Equipment and method of thickening and reuse for the sand filters backwashing water by using submerged hollow fiber membrane
JPH10337410A (en) Water purifying method and device therefor
JP2007245093A (en) Automatic washing method of strainer for water treatment apparatus by membrane filtration

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20080313

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20091005

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20110118

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20110322

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20110412

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20110425

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140520

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4742671

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees