JP3079604B2 - Water treatment equipment - Google Patents
Water treatment equipmentInfo
- Publication number
- JP3079604B2 JP3079604B2 JP03054601A JP5460191A JP3079604B2 JP 3079604 B2 JP3079604 B2 JP 3079604B2 JP 03054601 A JP03054601 A JP 03054601A JP 5460191 A JP5460191 A JP 5460191A JP 3079604 B2 JP3079604 B2 JP 3079604B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- membrane
- liquid
- solid
- membrane separation
- 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 - Lifetime
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は河川水や湖沼水を原水と
して産業用水や飲料水などを造水する場合に好適な水処
理装置に係り、特に凝集処理装置と膜分離装置とを備え
た水処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment apparatus suitable for producing industrial water or drinking water using river water or lake water as raw water, and particularly to a water treatment apparatus provided with a coagulation treatment apparatus and a membrane separation apparatus. It relates to a water treatment device.
【0002】[0002]
【従来の技術】河川水や湖沼水を原水として産業用水や
飲用水を造水する装置として、原水を凝集処理した後、
膜分離装置に導入し、膜分離装置の透過水を生産水とし
て得るものがある。2. Description of the Related Art As an apparatus for producing industrial water and drinking water using river water or lake water as raw water, the raw water is subjected to coagulation treatment,
In some cases, the water is introduced into a membrane separation device and the permeated water of the membrane separation device is obtained as product water.
【0003】この場合、膜分離装置の濃縮液の一部を必
要に応じさらに濃縮した後、凝集処理槽に戻し、種晶と
して利用する。[0003] In this case, a part of the concentrated liquid of the membrane separation device is further concentrated if necessary, and then returned to the coagulation treatment tank and used as a seed crystal.
【0004】[0004]
【発明が解決しようとする課題】上記従来の水処理装置
においては、膜不透過性の粘着物質(主として微小な有
機物質よりなる。)が濃縮側に蓄積してしまい、膜透過
速度が経時的に低下するという問題がある。In the above-mentioned conventional water treatment apparatus, an adhesive substance that is impermeable to a membrane (mainly composed of a minute organic substance) accumulates on the concentration side, and the permeation rate of the membrane increases with time. There is a problem that it decreases.
【0005】特に、河川水などの有機汚濁の少ない原水
を対象とする場合ほど、かかる問題が顕著になる。[0005] In particular, such a problem becomes more remarkable when raw water having little organic pollution such as river water is targeted.
【0006】[0006]
【課題を解決するための手段】本発明の水処理装置は、
浄水用原水を凝集処理する凝集処理手段と、該凝集処理
手段からの凝集液を膜分離する膜分離装置と、膜分離装
置の濃縮水を固液分離する固液分離手段と、該固液分離
手段で分離された汚泥分を系外に排出する手段と、前記
膜分離装置の透過水及び固液分離手段で分離された清澄
水を生産水として系外に取り出す手段と、を備えてなる
ものである。The water treatment apparatus of the present invention comprises:
Coagulation treatment means for coagulating raw water for water purification, a membrane separation device for membrane-separating the condensed liquid from the coagulation treatment means, a solid-liquid separation means for solid-liquid separation of concentrated water of the membrane separation device, and the solid-liquid separation Means for discharging the sludge separated by the means to the outside of the system, and means for removing permeated water of the membrane separation device and clarified water separated by the solid-liquid separation means to the outside of the system as production water. It is.
【0007】[0007]
【作用】かかる本発明の水処理装置においては、凝集処
理され更に膜分離処理された透過水が生産水として得ら
れる。膜分離装置の濃縮液は固液分離され、清澄水が生
産水とされ、汚泥分は系外に排出される。In the water treatment apparatus of the present invention, the permeated water subjected to the coagulation treatment and the membrane separation treatment is obtained as the production water. The concentrated liquid of the membrane separation device is separated into solid and liquid, clarified water is used as production water, and sludge is discharged out of the system.
【0008】このように、原水は一過式に処理される。
そして、濃縮水の凝集処理工程への返送が行なわれない
から、濃縮側での粘着性物質の蓄積がない。この結果、
膜透過速度が長時間、高いものとなる。[0008] Thus, the raw water is treated in a one-time manner.
Then, since the concentrated water is not returned to the coagulation treatment step, there is no accumulation of the sticky substance on the concentration side. As a result,
The membrane permeation rate is high for a long time.
【0009】[0009]
【実施例】以下図面を参照して実施例について説明す
る。Embodiments will be described below with reference to the drawings.
【0010】第1図は本発明の実施例に係る水処理装置
の系統図である。FIG. 1 is a system diagram of a water treatment apparatus according to an embodiment of the present invention.
【0011】河川水、湖沼水、市水、前処理済工業用
水、かん水、地下水などの原水は取水槽10に供給さ
れ、送水ポンプ12を経て凝集槽14へ送られる。この
凝集槽14へは、ポリ塩化アルミニウム(PAC)など
の凝集剤のほか、硫酸などのpH調整剤、あるいは次亜
塩素酸ナトリウムなどの塩素剤がそれぞれの貯槽16、
18、20からポンプ16a、18a、20aを経て供
給可能とされている。22は撹拌装置である。Raw water such as river water, lake water, city water, pre-treated industrial water, brackish water, and groundwater is supplied to an intake tank 10 and sent to a coagulation tank 14 via a water pump 12. Into the coagulation tank 14, a pH adjusting agent such as sulfuric acid, or a chlorine agent such as sodium hypochlorite, as well as a coagulant such as polyaluminum chloride (PAC) are stored in respective storage tanks 16,
It can be supplied from pumps 16a, 18a and 20a from pumps 18 and 20. 22 is a stirring device.
【0012】凝集槽14内において凝集フロックが生じ
た液は、加圧ポンプ24を経て膜分離装置26へ送られ
る。28は分離膜を示す。この分離膜28としては、精
密濾過膜、限外濾過膜、逆浸透膜など各種のものが用い
られる。The liquid in which flocculation floc has occurred in the flocculation tank 14 is sent to a membrane separation device 26 via a pressure pump 24. Reference numeral 28 denotes a separation membrane. As the separation membrane 28, various types such as a microfiltration membrane, an ultrafiltration membrane, and a reverse osmosis membrane are used.
【0013】この膜分離装置26の透過水は生産水とし
て生産水槽30へ送られる。濃縮水は沈降槽32へ送ら
れ、固液分離処理される。沈降した汚泥は系外に排出さ
れる。沈降槽32の上澄液はさらに濾過器(濾過材は、
砂、アンスラサイトなど任意である。)34へ送られ、
濾過処理された後生産水槽30へ送られる。The permeated water of the membrane separation device 26 is sent to a production water tank 30 as production water. The concentrated water is sent to the settling tank 32 and subjected to solid-liquid separation processing. The settled sludge is discharged out of the system. The supernatant of the sedimentation tank 32 is further filtered (filter material is
Sand, anthracite, etc. are optional. ) 34,
After being filtered, it is sent to the production water tank 30.
【0014】このように、本実施例装置にあっては原水
が一過式に処理され、膜分離装置26の濃縮液は凝集槽
14へ返送されない。このため、膜分離装置26の分離
膜28よりも上流側における粘着性物質の蓄積がない。
このため、膜分離装置26の膜面への粘着性物質の付着
速度がきわめて小さなものとなり、長時間にわたって安
定した膜分離処理を行なうことができ、装置全体として
の稼働安定性も著しく向上する。As described above, in the apparatus of this embodiment, the raw water is treated in a one-time manner, and the concentrated liquid in the membrane separation device 26 is not returned to the coagulation tank 14. Therefore, there is no accumulation of the sticky substance on the upstream side of the separation membrane 28 of the membrane separation device 26.
For this reason, the rate of adhesion of the adhesive substance to the membrane surface of the membrane separation device 26 is extremely low, and a stable membrane separation process can be performed for a long time, and the operation stability of the entire device is significantly improved.
【0015】上記実施例では、固液分離手段として沈降
槽32と濾過器34が用いられているが、沈降槽32と
濾過器34の一方だけを設けるようにしても良い。ま
た、固液分離手段としてはこのような沈降槽や濾過器の
ほか、加圧浮上分離装置など各種の固液分離手段を用い
ることができる。もちろん、沈殿槽や濾過器としても各
種のものを採用できる。In the above embodiment, the sedimentation tank 32 and the filter 34 are used as the solid-liquid separation means. However, only one of the sedimentation tank 32 and the filter 34 may be provided. As the solid-liquid separating means, various kinds of solid-liquid separating means such as a pressurized flotation device can be used in addition to the sedimentation tank and the filter. Of course, various things can be adopted also as a sedimentation tank and a filter.
【0016】上記実施例では凝集剤としてポリ塩化アル
ミニウムが示されているが、硫酸バンドや含鉄硫酸バン
ドなど各種のものを用いることができる。なお、このよ
うなアルミニウム系の無機凝集剤を用いる場合、水質に
もよるが通常の場合アルミニウムイオンとして1〜10
mg/lの割合で添加するのが好適である。In the above embodiment, polyaluminum chloride is shown as the flocculant, but various types such as a sulfuric acid band and an iron-containing sulfuric acid band can be used. When such an aluminum-based inorganic coagulant is used, although it depends on the water quality, usually 1 to 10 aluminum ions are used.
It is preferred to add at a rate of mg / l.
【0017】また、pH調整剤としても硫酸のほか各種
の酸やアルカリを用いることができる。Further, as the pH adjuster, various acids and alkalis can be used in addition to sulfuric acid.
【0018】[0018]
【発明の効果】以上の通り、本発明の水処理装置による
と、原水が一過式で凝集及び膜分離処理され、この膜分
離処理の濃縮液の返送を行なわないようにしている。従
って、濃縮側での粘着性物質の蓄積がなく、膜分離装置
の膜透過速度が長時間にわたって高いものとなり、安定
した水処理操作を行なうことができる。As described above, according to the water treatment apparatus of the present invention, the raw water is subjected to the coagulation and membrane separation processing in a transient manner, and the concentrated liquid in the membrane separation processing is not returned. Accordingly, there is no accumulation of the sticky substance on the concentration side, the membrane permeation rate of the membrane separation device is high for a long time, and a stable water treatment operation can be performed.
【0019】本発明は、SS(懸濁物質)の少ない原水
でも効率良く処理することができる。According to the present invention, raw water having a low SS (suspended substance) can be efficiently treated.
【図1】本発明装置の実施例装置の系統図である。FIG. 1 is a system diagram of an apparatus according to an embodiment of the present invention.
10 取水槽 14 凝集槽 26 膜分離装置 30 生産水槽 32 沈降槽 34 濾過器 DESCRIPTION OF SYMBOLS 10 Intake tank 14 Coagulation tank 26 Membrane separation apparatus 30 Production water tank 32 Sedimentation tank 34 Filter
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C02F 9/00 503 C02F 9/00 503A ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI C02F 9/00 503 C02F 9/00 503A
Claims (1)
と、該凝集処理手段からの凝集液を膜分離する膜分離装
置と、膜分離装置の濃縮水を固液分離する固液分離手段
と、該固液分離手段で分離された汚泥分を系外に排出す
る手段と、前記膜分離装置の透過水及び固液分離手段で
分離された清澄水を生産水として系外に取り出す手段
と、を備えてなる水処理装置。1. An aggregating means for aggregating raw water for water purification, a membrane separation device for membrane-separating an aggregating liquid from the aggregating means, and a solid-liquid separation means for solid-liquid separating concentrated water of the membrane separation device. Means for discharging the sludge separated by the solid-liquid separation means out of the system, and means for removing permeated water of the membrane separation device and clarified water separated by the solid-liquid separation means out of the system as production water, A water treatment device comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03054601A JP3079604B2 (en) | 1991-03-19 | 1991-03-19 | Water treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03054601A JP3079604B2 (en) | 1991-03-19 | 1991-03-19 | Water treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04290591A JPH04290591A (en) | 1992-10-15 |
JP3079604B2 true JP3079604B2 (en) | 2000-08-21 |
Family
ID=12975252
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03054601A Expired - Lifetime JP3079604B2 (en) | 1991-03-19 | 1991-03-19 | Water treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3079604B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05185095A (en) * | 1992-01-10 | 1993-07-27 | Ngk Insulators Ltd | Water purifying treatment using membrane |
JP2010000474A (en) * | 2008-06-23 | 2010-01-07 | Kobelco Eco-Solutions Co Ltd | Operation method of combined filtration equipment |
JP5174548B2 (en) * | 2008-06-23 | 2013-04-03 | 株式会社神鋼環境ソリューション | Operation method of combined filtration equipment |
-
1991
- 1991-03-19 JP JP03054601A patent/JP3079604B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH04290591A (en) | 1992-10-15 |
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