JPH06292818A - Air closing preventive device for membrane filtration for waterworks - Google Patents
Air closing preventive device for membrane filtration for waterworksInfo
- Publication number
- JPH06292818A JPH06292818A JP9651093A JP9651093A JPH06292818A JP H06292818 A JPH06292818 A JP H06292818A JP 9651093 A JP9651093 A JP 9651093A JP 9651093 A JP9651093 A JP 9651093A JP H06292818 A JPH06292818 A JP H06292818A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- air
- filtration
- water
- washing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、精密ろ過膜、限外ろ
過膜等の透過膜を利用した、上水道のろ過操作に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filtering operation for waterworks utilizing a permeable membrane such as a microfiltration membrane and an ultrafiltration membrane.
【0002】[0002]
【従来の技術】従来、精密ろ過膜、限外ろ過膜等のろ過
膜を利用して、上水道のろ過操作を行なう試みがなされ
てきた。2. Description of the Related Art Heretofore, attempts have been made to perform a filtering operation for waterworks by using a filtration membrane such as a microfiltration membrane or an ultrafiltration membrane.
【0003】その際、ろ過膜を直列2段に配置すること
により、処理水質の向上や膜破損時の安全性確保などに
効果を上げている。ところで、後段膜を全量ろ過方式と
すると、エネルギー効率は良いが、前段膜ろ過水の圧力
変化により気泡が発生し、後段の全量ろ過膜の1次側に
空気溜まりができ、後段ろ過膜の有効膜面積を低下させ
るとともに、逆流洗浄の妨げとなり、ろ過および逆流洗
浄に悪影響を及ぼしていた。At this time, by arranging the filtration membranes in two stages in series, the effects of improving the quality of treated water and ensuring safety when the membrane is damaged are enhanced. By the way, if the post-stage membrane is a total filtration type, the energy efficiency is good, but bubbles are generated due to the pressure change of the pre-stage membrane filtration water, and air can be accumulated on the primary side of the post-stage total filtration membrane, which makes the post-stage filtration membrane effective. While reducing the membrane area, it hindered backwashing, which adversely affected filtration and backwashing.
【0004】[0004]
【発明が解決しようとする課題】膜モジユ−ルケ−スで
ユニツト構成される全量ろ過方式の膜ろ過装置におい
て、上水道用に用いるろ過膜は数kg/cm2以上の高圧でな
いと空気を通さないため、供給水に含入する空気や、圧
力変化、温度変化により発生した空気は、膜モジユ−ル
の1次側に溜まる。また直列2段にろ過膜を設置し、後
段ろ過膜を全量ろ過方式で処理すると、前段ろ過水から
発生した気泡は、後段ろ過膜モジユ−ルの1次側に溜ま
り、ろ過膜面積の低下を引き起こしている。さらにこの
気泡が、前段ろ過膜2次側配管中に残つた場合、前段ろ
過膜逆流洗浄時空気溜まりが発生し、ろ過膜に逆流洗浄
水が供給されない部分ができ、洗浄不良を引き起こす。DISCLOSURE OF THE INVENTION In a membrane filtration device of a total volume filtration system composed of a membrane module case as a unit, the filtration membrane used for water supply cannot pass air unless it has a high pressure of several kg / cm 2 or more. Therefore, the air contained in the supplied water and the air generated by the pressure change and the temperature change are accumulated on the primary side of the membrane module. Also, when the filtration membranes are installed in two stages in series and the post-filtration membrane is treated by the total filtration method, the bubbles generated from the pre-stage filtration water accumulate on the primary side of the post-filtration membrane module, and the filtration membrane area is reduced. Is causing. Further, when the air bubbles remain in the upstream pipe of the upstream filtration membrane, an air pool is generated during the upstream cleaning of the upstream filtration membrane, and a portion where the backwash water is not supplied is formed in the filtration membrane, resulting in poor cleaning.
【0005】[0005]
【課題を解決するための手段】ここにおいてこの発明
は、精密ろ過もしくは限外ろ過膜などのろ過膜を直列に
設置し、少なくとも後段ろ過膜を全量ろ過方式とした上
水道用膜ろ過装置において、前段ろ過膜ろ過後、後段ろ
過膜までの間で、前段ろ過膜ろ過水から発生する気泡を
自動的に系外に排出することにより、後段ろ過膜1次側
に空気溜まりが発生して有効ろ過面積が低下することを
防止するとともに、逆流洗浄時に洗浄配管経路の空気閉
塞を防止することを特徴とした上水道用膜ろ過における
空気閉塞防止装置を提案するものである。Means for Solving the Problems Here, the present invention provides a membrane filtration apparatus for waterworks in which filtration membranes such as microfiltration or ultrafiltration membranes are installed in series, and at least the latter-stage filtration membrane is a total-volume filtration system. After the filtration membrane filtration, the air bubbles generated from the upstream filtration membrane filtered water are automatically discharged to the outside of the system between the downstream filtration membrane, and the air is generated on the primary side of the downstream filtration membrane, and the effective filtration area. The present invention proposes an air blockage prevention device for membrane filtration for waterworks, which is characterized in that it prevents a decrease in water flow rate and prevents air blockage in a cleaning pipe path during backwashing.
【0006】[0006]
【作用】通常、膜モジユ−ルのケ−シングに空気抜きを
付設する例が多いが、自動空気抜弁等を直接取り付ける
ことは困難なこともある。ここで中空糸型のように、円
筒形のモジユ−ルの場合、両端に配管接続できる形状の
ものが多いので、接続した配管に空気を抜く装置を接続
する。In general, in many cases, an air vent is attached to the casing of the membrane module, but it may be difficult to directly attach an automatic air vent valve or the like. Here, in the case of a cylindrical module such as a hollow fiber type, many of them have a shape in which both ends can be connected to a pipe, so an apparatus for removing air is connected to the connected pipe.
【0007】空気は水に対し比重が軽いので、膜モジユ
−ルに接続する配管のモジユ−ルにできるだけ近く、ま
た上方に空気抜きを設置し、空気排出に圧力を加えた方
が抜けやすいのも考慮し、供給水供給配管をモジユ−ル
の下方向に取り付ける。なお空気抜きには、フロ−ト式
空気抜弁(排出空気量小)、急速吸排気弁、電動弁(排
出空気量大)などを用いる。Since the specific gravity of air is lighter than that of water, it is easier to get rid of it by putting air vents near the module of the pipe connected to the membrane module and by installing an air vent at the top. Considering this, install the supply water supply pipe in the downward direction of the module. A float type air vent valve (small exhaust air amount), a quick intake / exhaust valve, an electric valve (large exhaust air amount), etc. are used for air venting.
【0008】[0008]
【実施例】本実施例はろ過膜2段方式で処理する場合
で、前段を限外ろ過によるクロスフロ−ろ過、後段を精
密ろ過による全量ろ過で処理している装置に、空気抜弁
を設置した場合である。[Examples] This example is a case where a two-stage filtration membrane system is used, in which an air vent valve is installed in a device in which the former stage is a cross flow filtration by ultrafiltration and the latter stage is a total volume filtration by microfiltration. Is.
【0009】ろ過工程時、原水管1から原水を受水槽2
に流入させる。供給ポンプ3により前段膜モジユ−ル6
へ原水が供給され、クロスフロ−流は弁7、配管8を経
由して受水槽2へもどる。前段膜でろ過された処理水
は、配管10を経由し、弁11は開、弁12は閉として
おき、後段膜モジユ−ル13へ流入する。後段膜処理水
は配管15、流量計器16を経由して、洗浄水槽19に
流入し、さらに配管20によつて配水される。During the filtration process, the raw water pipe 1 receives the raw water from the water tank 2
Flow into. The front-stage membrane module 6 by the supply pump 3
Raw water is supplied to the water, and the cross flow returns to the water receiving tank 2 via the valve 7 and the pipe 8. The treated water filtered by the pre-stage membrane flows into the post-stage membrane module 13 after leaving the valve 11 open and the valve 12 closed via the pipe 10. The post-stage membrane-treated water flows into the washing water tank 19 via the pipe 15 and the flow meter 16, and is further distributed via the pipe 20.
【0010】ここで、前段膜の処理水は、原水に対しク
ロスフロ−のエネルギーを加えているために水温の上昇
があることや、膜を通過するときに圧力差が生じるた
め、気泡が発生しやすい。ここで発生した気泡は流水経
路内に溜まり、さらに後段膜モジユ−ル13内の1次側
に流れ溜まり続ける。そこで空気抜弁14によりこの空
気を排除し、後段膜の面積低下を防止する。Here, the treated water in the pre-stage membrane has bubbles because the water temperature rises because cross-flow energy is applied to the raw water and a pressure difference occurs when passing through the membrane. Cheap. The bubbles generated here accumulate in the flowing water path, and further continue to flow and accumulate in the primary side in the post-stage membrane module 13. Therefore, this air is removed by the air vent valve 14 to prevent a reduction in the area of the latter-stage membrane.
【0011】逆洗工程時は、洗浄水槽19から配管17
を経由し、洗浄ポンプ18により加圧し、弁11は閉、
弁12は開としておき、前段膜モジユ−ル6へ流入す
る。その圧力により、前段膜モジユ−ル6の2次側に残
る空気を、空気抜弁9から排出する。前段膜モジユ−ル
6の1次側から流出する洗浄排水は、排水弁4を開とす
ることで、排水管5を経由して排出される。During the backwash process, the washing water tank 19 is connected to the pipe 17
Via the cleaning pump 18 and the valve 11 is closed,
The valve 12 is left open and flows into the anterior membrane module 6. Due to the pressure, the air remaining on the secondary side of the pre-stage membrane module 6 is discharged from the air vent valve 9. The cleaning drainage flowing out from the primary side of the upstream membrane module 6 is drained through the drain pipe 5 by opening the drain valve 4.
【0012】ここでの例は、2段式処理のため後段ろ過
膜における濁質捕捉はほとんどない。したがつて、後段
ろ過膜の自動洗浄機構は組み入れられていない。[0012] In this example, because of the two-stage treatment, there is almost no trapping of suspended matter in the post-filtration membrane. Therefore, the automatic cleaning mechanism for the latter filtration membrane is not incorporated.
【0013】[0013]
【発明の効果】この発明の上述の装置によれば、前段ろ
過膜ろ過水から発生する気泡は、自動的に系外に排出さ
れるため、後段ろ過膜の1次側に空気溜まりが発生し
て、有効ろ過面積が低下するのを防止できるとともに、
逆洗時の洗浄配管経路の空気閉塞を防止しうるものであ
る。According to the above-mentioned device of the present invention, the air bubbles generated from the filtered water of the front stage filtration membrane are automatically discharged to the outside of the system, so that the air trap is generated on the primary side of the rear stage filtration membrane. And prevent the effective filtration area from decreasing,
It is possible to prevent air clogging in the cleaning piping path during backwashing.
【図1】この発明の装置の系統図である。FIG. 1 is a system diagram of an apparatus according to the present invention.
【符号の説明】 6 前段膜モジユ−ル 9 空気抜弁 13 後段膜モジユ−ル 14 空気抜弁[Explanation of Codes] 6 Front-stage membrane module 9 Air vent valve 13 Rear-stage membrane module 14 Air vent valve
Claims (1)
過膜を直列に配置し、少なくとも後段ろ過膜を全量ろ過
方式とした上水道用膜ろ過装置において、前段ろ過膜ろ
過後、後段ろ過膜までの間で、前段ろ過膜ろ過水から発
生する気泡を自動的に系外に排出することにより、後段
ろ過膜1次側に空気溜まりが発生して有効ろ過面積が低
下することを防止するとともに、逆流洗浄時に洗浄配管
経路の空気閉塞を防止することを特徴とした上水道用膜
ろ過における空気閉塞防止装置。1. In a water supply membrane filtration device in which filtration membranes such as microfiltration membranes or ultrafiltration membranes are arranged in series, and at least the latter-stage filtration membrane is a total volume filtration system, after the first-stage filtration membrane filtration to the second-stage filtration membrane. In between, by automatically discharging the air bubbles generated from the upstream filtration membrane filtered water to the outside of the system, while preventing the occurrence of air pools on the primary side of the downstream filtration membrane and reducing the effective filtration area, An air blockage preventive device for membrane filtration for water supply, which is characterized by preventing air blockage in a cleaning pipe path during backwashing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9651093A JPH06292818A (en) | 1993-04-01 | 1993-04-01 | Air closing preventive device for membrane filtration for waterworks |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9651093A JPH06292818A (en) | 1993-04-01 | 1993-04-01 | Air closing preventive device for membrane filtration for waterworks |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06292818A true JPH06292818A (en) | 1994-10-21 |
Family
ID=14167128
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9651093A Pending JPH06292818A (en) | 1993-04-01 | 1993-04-01 | Air closing preventive device for membrane filtration for waterworks |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06292818A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004037396A1 (en) * | 2002-10-24 | 2004-05-06 | Dhv Water B.V. | Method of operating a filter unit, an apparatus to be used therewith and a capillary filtration module |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58163490A (en) * | 1982-03-23 | 1983-09-28 | Mitsubishi Rayon Co Ltd | Method and apparatus for purification of water |
-
1993
- 1993-04-01 JP JP9651093A patent/JPH06292818A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58163490A (en) * | 1982-03-23 | 1983-09-28 | Mitsubishi Rayon Co Ltd | Method and apparatus for purification of water |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004037396A1 (en) * | 2002-10-24 | 2004-05-06 | Dhv Water B.V. | Method of operating a filter unit, an apparatus to be used therewith and a capillary filtration module |
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