[go: up one dir, main page]

JP2003112180A - Water purification device - Google Patents

Water purification device

Info

Publication number
JP2003112180A
JP2003112180A JP2001307323A JP2001307323A JP2003112180A JP 2003112180 A JP2003112180 A JP 2003112180A JP 2001307323 A JP2001307323 A JP 2001307323A JP 2001307323 A JP2001307323 A JP 2001307323A JP 2003112180 A JP2003112180 A JP 2003112180A
Authority
JP
Japan
Prior art keywords
water
flow path
electrolyzer
cleaning
magnetic
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
Application number
JP2001307323A
Other languages
Japanese (ja)
Inventor
Norihide Saho
典英 佐保
Yuko Okada
祐子 岡田
Takashi Mizumori
隆司 水守
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP2001307323A priority Critical patent/JP2003112180A/en
Publication of JP2003112180A publication Critical patent/JP2003112180A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

(57)【要約】 【課題】通水濾過分離膜への異物の固定化を防止し、通
水濾過分離膜の通水性能が低下しない水浄化装置を提供
する。 【解決手段】前処理水12に含まれる被除去物及び磁性
物質を捕捉し濾過して前処理水12を浄化する濾過手段
15と、この濾過手段15の表面に捕捉されて堆積した
被除去物及び磁性物質を洗浄水で洗浄することによって
濾過手段15から剥離する洗浄手段31と、剥離された
被除去物及び磁性物質を前処理水12の液面上に移動さ
せる移動手段37とを備える水浄化装置において、濾過
された後の浄化水25の流れる流路98を分岐し、この
分岐した流路98に、浄化水25を酸性水とアリカリイ
オン水とに電気分解する電気分解装置105を設け、こ
の電気分解装置105で生成された酸性水を再び洗浄水
12に戻す流路30を設ける。
(57) Abstract: Provided is a water purification device which prevents immobilization of foreign substances on a water filtration separation membrane and does not deteriorate water passage performance of the water filtration separation membrane. A filter means (15) for purifying the pretreatment water (12) by trapping and filtering a substance to be removed and a magnetic substance contained in the pretreatment water (12), and a substance to be trapped and deposited on the surface of the filtration means (15) And a cleaning means 31 for removing the magnetic substance from the filtration means 15 by washing the cleaning substance with the cleaning water, and a moving means 37 for moving the removed object and the magnetic substance onto the liquid surface of the pretreatment water 12. In the purification device, a flow path 98 through which the purified water 25 after being filtered flows is branched, and an electrolysis device 105 for electrolyzing the purified water 25 into acidic water and alkaline ionized water is provided in the branched flow path 98. A flow path 30 is provided for returning the acidic water generated by the electrolyzer 105 to the washing water 12 again.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、水質浄化や固液分
離等を行う水浄化装置に係り、特に汚濁粒子の膜分離を
連続的に行うことができる水浄化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purification device for water purification, solid-liquid separation and the like, and more particularly to a water purification device capable of continuously performing membrane separation of pollutant particles.

【0002】[0002]

【従来の技術】従来、水質浄化や固液分離等を行う浄化
装置として、細めの金網や高分子繊維で編んだ網、微粒
子物質をポーラスな薄い層に成形した膜、あるいは高分
子繊維を和紙のように接合して微細な孔を形成した膜を
通水濾過分離膜として使用することによって、粒子を濾
過分離し除去する浄化装置が知られている。この浄化装
置の構造は,例えば化学技術誌MOLVol.22,No.12 p47
-51(1984)に記載されている。
2. Description of the Related Art Conventionally, as a purifying device for purifying water quality or solid-liquid separation, a fine wire net or a net woven with polymer fibers, a membrane formed by forming fine particles into a porous thin layer, or polymer fibers with Japanese paper There is known a purifying device that filters and removes particles by using the membrane bonded as described above as a water filtration separation membrane to form fine pores. The structure of this purification device is, for example, MOL Vol.22, No.12 p47
-51 (1984).

【0003】ステンレス鋼の細線やポリエステル繊維等
で膜や網(以下、単に膜という)を構成することによっ
て、被処理水中の水は、例えば網や膜の数ミクロンメー
トルから数十、数百ミクロンメートルの目開きを有した
開口部を通過して浄化されるが、アオコ、有機物などの
汚濁物質は、その投影面積(投影直径)が開口部の投影
面積や投影直径よりも大きい場合、当然通過できずに捕
捉分離される。このまま、同じ膜面に被処理水を通水し
続けると、膜の通水側面に被処理物が堆積して通水抵抗
が増大し、通水量が極端に低下して浄化操作に支障をき
たす。
By constructing a film or net (hereinafter simply referred to as a film) from stainless steel thin wires or polyester fibers, the water in the water to be treated is, for example, from several microns to several tens to several hundreds of microns of the net or film. Although it is purified by passing through an opening with a meter opening, if the projected area (projected diameter) of water pollutants, organic matter, etc. is larger than the projected area or projected diameter of the opening, it naturally passes. It cannot be captured and separated. If water to be treated continues to flow through the same membrane surface as it is, substances to be treated will accumulate on the water-permeable side of the membrane, increasing water resistance, and the amount of water passing will be extremely reduced, impeding purification operations. .

【0004】従来、膜面が被処理水の液面以下の部位に
ある水浄化装置では、この堆積物の蓄積した膜面を被処
理水の液面上(大気部)まで移動させ、シャワー状の浄
化水を噴射することによって膜を洗浄して再生し、再び
膜面を液面下に戻して使用する操作が行われている。
Conventionally, in a water purifying apparatus in which the film surface is located below the liquid surface of the water to be treated, the film surface on which the deposits have accumulated is moved to the liquid surface of the water to be treated (atmosphere), and a shower shape is obtained. The membrane is cleaned and regenerated by spraying purified water, and the membrane surface is returned to below the liquid surface for use.

【0005】また、開口部の投影面積(投影直径)より
も小さい微細な汚濁物質も分離する必要がある場合に
は、予め被処理水に凝集剤として硫酸バン土、ポリ塩化
アルミニウム、ポリ硫酸鉄などを加えて撹絆し、原水中
の微細な固形浮遊物、藻類、菌類、微生物などを凝縮剤
によって数百ミクロンメートル程度の大きさに結合さ
せ、いわゆるフロックを形成している。したがって、こ
のフロックは、数十ミクロンメートルの目開の開口部を
通過できないため高い除去率で捕捉分離され、さらに水
質の高い浄化水が得られる。
When it is necessary to separate fine pollutants smaller than the projected area (projected diameter) of the opening, vanadium sulfate, polyaluminum chloride or polyiron sulfate is previously added to the water to be treated as a coagulant. The mixture is mixed with other substances, and fine solid suspended matter in the raw water, algae, fungi, microorganisms, etc. are combined with a condensing agent to a size of several hundreds of micrometers to form so-called flocs. Therefore, since this floc cannot pass through the opening of the aperture of several tens of micrometers, it is captured and separated with a high removal rate, and purified water of higher water quality is obtained.

【0006】さらに、特開平10−470号公報、特開
平10−328514号公報、特開平11−29085
4号公報などに記載されるように、浴槽水を浄化する技
術も知られている。
[0006] Further, JP-A-10-470, JP-A-10-328514, and JP-A-11-29085.
As described in Japanese Patent No. 4 etc., a technique for purifying bath water is also known.

【0007】[0007]

【発明が解決しようとする課題】しかし、通水濾過分離
膜は連続的(もしくは断続的に長時間)に水中に浸漬さ
れると、水中の微生物、バクテリヤ、稚貝、有機物、無
機物などが通水濾過分離膜に付着する。この結果、好気
生物類は有機物を消化して発育群生し、また、微生物か
ら発生する粘着性物質は、無機物を通水濾過分離膜に固
定化して膜の開口部を閉塞してしまう。したがって、通
水濾過分離膜の通水性能が低下し、浄化処理能力が低下
する。
However, when a water filtration separation membrane is continuously (or intermittently) immersed in water for a long time, microorganisms, bacteria, juveniles, organic substances, inorganic substances and the like in the water pass through. It adheres to the water filtration separation membrane. As a result, aerobic organisms digest organic matter to form growth colonies, and sticky substances generated from microorganisms immobilize inorganic substances on a water filtration separation membrane and block the openings of the membrane. Therefore, the water-passing performance of the water-passing filtration separation membrane is lowered, and the purification treatment ability is lowered.

【0008】特に、浄化する対象原水が、プランクトン
等を有する湖沼、河川、溜池、海水・有機物を多量に含
む食品工場の排水や、バクテリヤ等を有する下水などの
場合、膜の繊維に微生物が繁殖し、浄化水量を低下させ
る。このような場合、従来、水酸化ナトリウム等の強ア
ルカリ液で膜を洗浄し、微生物を除去する方法が採られ
ている。しかし、このような方法では、使用したアルカ
リ水溶液を別途保留し、環境を汚染させないために酸を
添加して中和処理した後に汚泥を廃棄するための設備が
必要となる。また、公報記載の技術は洗浄処理中に浄化
運転をすることについては、配慮されていない。
Especially, when the target raw water to be purified is a effluent of a lake, river, reservoir, seawater containing a large amount of organic matter such as plankton, or sewage containing bacteria etc. And reduce the amount of purified water. In such a case, conventionally, a method of washing the membrane with a strong alkaline liquid such as sodium hydroxide to remove microorganisms has been adopted. However, such a method requires a facility for separately storing the used alkaline aqueous solution, adding an acid to neutralize the environment and then discarding the sludge in order not to pollute the environment. Further, the technique described in the publication does not consider performing the cleaning operation during the cleaning process.

【0009】本発明の目的は、通水濾過分離膜の洗浄水
の一部をイオン化して洗浄水に殺菌作用や凝集作用を持
たせることにより、通水濾過分離膜への異物の固定化を
防止し、通水濾過分離膜の通水性能が低下せず、また洗
浄処理をしながら水の浄化運転が可能な水浄化装置を提
供することにある。
An object of the present invention is to immobilize foreign matter to the water filtration / separation membrane by ionizing a part of the wash water of the water filtration / separation membrane so that the wash water has a sterilizing action and an aggregating action. It is to provide a water purifying device that prevents the deterioration of the water permeation performance of the water permeation filtration separation membrane, and that can perform the water purifying operation while performing the cleaning process.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するた
め、本発明に係る水浄化装置の発明は、前処理水に含ま
れる被除去物及び磁性物質を捕捉し濾過して前記前処理
水を浄化する濾過手段と、この濾過手段の表面に捕捉さ
れて堆積した被除去物及び磁性物質を洗浄水で洗浄する
ことによって前記濾過手段から剥離する洗浄手段と、剥
離された被除去物及び磁性物質を前記前処理水の液面上
に移動させる移動手段とを備える水浄化装置において、
前記濾過された後の浄化水の流れる流路を分岐し、この
分岐した流路に、浄化水を酸性水とアリカリイオン水と
に電気分解する電気分解装置を設け、この電気分解装置
で生成された酸性水を前記洗浄水に戻す流路を設けるも
のである。
In order to achieve the above-mentioned object, the invention of a water purification apparatus according to the present invention provides a method for capturing pre-treated water by capturing and filtering substances to be removed and magnetic substances contained in the pre-treated water. Filtering means for purifying, cleaning means for removing the object to be removed and magnetic substance trapped and deposited on the surface of the filtering means from the filtering means by washing with wash water, and the object to be removed and magnetic substance to be removed In a water purifying apparatus comprising a moving means for moving the above-mentioned pretreated water on the liquid surface,
The flow path of the purified water after filtering is branched, and an electrolyzer for electrolyzing the purified water into acidic water and alkaline water is provided in the branched flow path. A flow path for returning the acidic water to the washing water is provided.

【0011】上記目的を達成するため、本発明に係る水
浄化装置の他の発明は、前処理水に含まれる被除去物及
び磁性物質を捕捉し濾過して前記前処理水を浄化する濾
過手段と、この濾過手段の表面に捕捉されて堆積した被
除去物及び磁性物質を洗浄水で濾過手段から剥離する洗
浄手段と、剥離した被除去物及び磁性物質を前記処理水
の液面上まで移動させる移動手段とを備える水浄化装置
において、前記濾過された後の浄化水の流れる流路を分
岐し、この分岐した流路に、浄化水を酸性水とアリカリ
イオン水とに電気分解する電気分解装置を設け、この電
気分解装置で生成されたアリカリイオン水を、前記濾過
された後の浄化水に合流する流路を設けるものである。
In order to achieve the above-mentioned object, another invention of the water purifying apparatus according to the present invention is a filtering means for purifying the pretreated water by capturing and filtering substances to be removed and magnetic substances contained in the pretreated water. And a cleaning means for separating the object to be removed and the magnetic substance trapped and accumulated on the surface of the filtering means from the filtering means with cleaning water, and the separated object to be removed and the magnetic substance moved to the liquid surface of the treated water. In the water purifying apparatus including a moving unit for moving the filtered purified water, the flow path of the filtered purified water is branched, and the branched flow path is electrolyzed to electrolyze the purified water into acidic water and alkaline ionized water. A device is provided, and a flow path for joining the alkaline water generated by the electrolyzer with the filtered purified water is provided.

【0012】上記目的を達成するため、本発明に係る水
浄化装置のさらに他の発明は、前処理水に含まれる被除
去物及び磁性物質を捕捉し濾過して前記前処理水を浄化
する濾過手段と、この濾過手段の表面に捕捉されて堆積
した被除去物及び磁性物質を洗浄水で濾過手段から剥離
する洗浄手段と、剥離した被除去物及び磁性物質を前記
処理水の液面上まで移動させる移動手段とを備える水浄
化装置において、前記濾過された後の浄化水の流れる流
路を分岐し、この分岐した流路に、浄化水を酸性水とア
リカリイオン水とに電気分解する電気分解装置を設け、
この電気分解装置で生成されたアリカリイオン水を、前
記前処理水に合流させる流路を設けるものである。
In order to achieve the above-mentioned object, still another invention of the water purifying apparatus according to the present invention is a filtration for purifying the pretreated water by capturing and filtering substances to be removed and magnetic substances contained in the pretreated water. Means, a cleaning means for separating the object to be removed and the magnetic substance trapped and deposited on the surface of the filtering means from the filtering means with cleaning water, and the separated object to be removed and the magnetic substance to the liquid surface of the treated water. In a water purifying apparatus including a moving means for moving, a flow path through which the purified water after the filtration flows is branched, and an electricity for electrolyzing the purified water into acidic water and alkaline water With a disassembly device,
A flow path is provided for joining the alkaline water generated by the electrolyzer with the pretreated water.

【0013】好ましくは、前記分岐した流路に、電気分
解装置に流れる浄化水を加圧する手段と、電気分解装置
に流れる浄化水の流量を調整する流量調整弁を設けるも
のである。
Preferably, the branched flow path is provided with a means for pressurizing the purified water flowing to the electrolyzer and a flow rate adjusting valve for adjusting the flow rate of the purified water flowing to the electrolyzer.

【0014】また、前記電気分解装置も電力の一部もし
くは全部を、太陽電池で発生する電力で賄うものであ
る。また、前記電気分解装置で発生する水素ガスを空気
中の酸素と化学反応させ、この化学反応によって発電す
る燃料電池発電手段を備えるものである。
Further, the electrolyzer also supplies a part or all of the electric power with the electric power generated by the solar cell. Further, the fuel cell power generation means is provided for chemically reacting hydrogen gas generated in the electrolyzer with oxygen in the air and generating power by this chemical reaction.

【0015】[0015]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1は、本発明に係る水浄化装置
の使用状況を示す図、図2は、水浄化装置の要部拡大横
断面図、図3は、図2のX−X線に沿う断面図で、一部
平面図で示してある。図1に示すように原水を、例えば
貯水池1から、配管2、大きなゴミを取るためのフィル
タ3を通した後、ポンプ4で原水貯槽5に汲み上げ、こ
の原水6にシーディング剤調整装置7から、四三酸化鉄
等の磁性粉、pH調整剤、ポリ塩化アルミニウムや塩化
鉄、硫酸第二鉄などの水溶液のアルミニュウムイオンも
しくは鉄イオンなどに分離して凝集作用を行う凝集剤、
高分子補強剤等が配管8を通じて加えられる。撹絆槽9
では、これら磁性粉、pH調整剤、凝集剤、高分子補強
剤などをモータ10の回転にともなって回転する攪拌翼
11によって撹絆して、数百ミクロンメートル〜数ミリ
メートル程度の大きさの、いわゆる磁性フロックを含む
前処理水12をつくる。この前処理水12は、矢印Aで
示すように配管13を通じて膜磁気分離装置14に送ら
れる。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a diagram showing a usage state of a water purifying apparatus according to the present invention, FIG. 2 is an enlarged transverse sectional view of a main part of the water purifying apparatus, and FIG. 3 is a sectional view taken along line XX of FIG. A partial plan view is shown. As shown in FIG. 1, raw water is passed from a reservoir 1, for example, through a pipe 2 and a filter 3 for removing large dust, and then pumped up to a raw water storage tank 5 by a pump 4, and the raw water 6 is fed from a seeding agent adjusting device 7 to the raw water 6. , Magnetic powder such as ferric tetroxide, pH adjusting agent, flocculant that separates into aluminum ion or iron ion of aqueous solution of polyaluminum chloride, iron chloride, ferric sulfate, etc.
A polymer reinforcing agent or the like is added through the pipe 8. Stirring tank 9
Then, the magnetic powder, the pH adjuster, the coagulant, the polymer reinforcing agent, and the like are agitated by the stirring blade 11 that rotates with the rotation of the motor 10 to have a size of several hundreds of micrometers to several millimeters. The pretreated water 12 containing so-called magnetic flocs is prepared. The pretreated water 12 is sent to the membrane magnetic separation device 14 through the pipe 13 as shown by an arrow A.

【0016】図2、図3により膜磁気分離装置14の構
造を詳細に説明する。ステンレス鋼の細線、銅の細線も
しくはポリエステル繊維で数ミクロンメートルから数十
ミクロンメートルの目開きの開口部を有する膜15(濾
過手段)をドラム状に形成する。膜15の両端は目開き
のないドラム状のシェル16、17に接合される。その
一端(図示下端)は、フランジ18に接合されて一体化
され、フランジ18の中央部にはロッド19を介してモ
ータ20が取り付けられ、このモータ20の回転にとも
なってフランジ18、シェル16、ドラム状の膜15、
シェル17が回転する構成になっている。
The structure of the film magnetic separation device 14 will be described in detail with reference to FIGS. A membrane 15 (filtering means) having openings of several micrometers to several tens of micrometers is formed in a drum shape from stainless steel thin wires, copper thin wires or polyester fibers. Both ends of the membrane 15 are joined to drum-shaped shells 16 and 17 having no openings. One end (lower end in the drawing) is joined and integrated with the flange 18, and the motor 20 is attached to the central portion of the flange 18 via the rod 19, and as the motor 20 rotates, the flange 18, the shell 16, Drum-shaped membrane 15,
The shell 17 is configured to rotate.

【0017】シェル17と固定フランジ21とは、接合
によって水密性を有して一体化されている。固定フラン
ジ21に溶接、接着等で一体化されたノズル28は、摺
動抵抗の小さい高分子材料のリング状摺動体22、23
で水密性を維持してケーシング27によって支持され、
固定フランジ21の回転中心がぶれない構成になってい
る。
The shell 17 and the fixed flange 21 are watertightly integrated by joining. The nozzle 28, which is integrated with the fixed flange 21 by welding, adhesion, or the like, has ring-shaped sliding bodies 22 and 23 made of a polymer material having a low sliding resistance.
Supported by the casing 27 while maintaining watertightness at
The rotation center of the fixed flange 21 does not move.

【0018】浄化水槽を形成するケーシング27内に、
膜15が取り付けられている。前処理水12は、配管1
3からケーシング27内に流入して膜15を通過する。
この時、前処理水12に含まれる磁性フロック24は膜
15外面に捕捉される。膜15を通過し磁性フロック2
4を分離した前処理水12は浄化水25となり、矢印B
で示すようにノズル28を通って浄化水槽29に貯水さ
れ、ノズル96から配管(流路)26を通って、再び貯
水池1に戻される。前処理水12が膜15を通過する動
力は前処理水12と浄化水25との液面位差である。
In the casing 27 forming the purified water tank,
Membrane 15 is attached. Pretreated water 12 is pipe 1
3 flows into the casing 27 and passes through the membrane 15.
At this time, the magnetic flocs 24 contained in the pretreated water 12 are captured on the outer surface of the film 15. Magnetic flock 2 passing through the membrane 15
The pretreated water 12 from which 4 has been separated becomes purified water 25, and arrow B
As shown in FIG. 5, water is stored in the purified water tank 29 through the nozzle 28, is returned from the nozzle 96 through the pipe (flow path) 26 to the water reservoir 1 again. The power of the pretreated water 12 passing through the membrane 15 is the difference in liquid level between the pretreated water 12 and the purified water 25.

【0019】一方、磁性フロック24は図2で、時計回
りに回転する膜15外面から通水されることによって濾
過されて付着し、堆積物となって水面近傍に回転移動す
る。浄化水25の一部(5%程度)は、浄化水槽29に
設けられた前記配管26から分岐したノズル97から配
管98でポンプ99に導かれ、加圧されて洗浄水とな
る。この加圧された洗浄水は、配管100の途中に設置さ
れた流量調整用バイパス弁101、及び配管102の途
中に設置された流量調整弁103で洗浄流量を調整し、
配管30からシャワー管31(洗浄手段)に送り、孔か
らシャワー水32が膜15内表面から外面側に向けて吹
き付けられる。
On the other hand, in FIG. 2, the magnetic flocs 24 are filtered and adhered by passing water from the outer surface of the membrane 15 which rotates clockwise, and become a deposit and rotate and move near the water surface. A part (about 5%) of the purified water 25 is guided to a pump 99 by a pipe 98 from a nozzle 97 branched from the pipe 26 provided in the purified water tank 29, and is pressurized to be wash water. The pressurized cleaning water has a cleaning flow rate adjusted by a flow rate adjusting bypass valve 101 installed in the middle of the pipe 100 and a flow adjusting valve 103 installed in the middle of the pipe 102.
The shower water 32 is sent from the pipe 30 to the shower pipe 31 (cleaning means), and shower water 32 is sprayed from the inner surface of the membrane 15 toward the outer surface side.

【0020】配管104の途中には電気分解装置105
を配置し、洗浄水の一部を電気分解装置105に導く。電
気分解装置105への導入流量は、流量調整弁106と
103とで調整する。電気分解装置105に導入された
洗浄水は電気分解され、陽極(図示せず)にOH負イオン
を多く含むアルカリイオン水を発生し、これを配管10
7から、流量調整弁108を介して配管26に接続し、貯
水池1に戻す。一方、陰極(図示せず)には、H正イオンを
多く含む酸性水が発生し、これを配管104から配管3
0に供給し、洗浄水内に酸性水を混入させる。膜15の内
表面に蓄積した堆積物は内面から吹き付けられたシャワ
ー水32によって剥離され、膜15面は堆積物が剥離さ
れることによって再生され、磁性フロック24は前処理
水12の水面に浮遊する。また、同時にシャワー水32
中の酸性水で膜15を洗浄し、酸性水の殺菌作用によっ
て膜15上に付着したバクテリア等の微生物は殺菌さ
れ、膜15上で微生物が繁殖することを防止する。 また、
微生物が繁殖するのを防止することにより、微生物が体
内から発生する粘液性の体液の発生も無くなり、この結
果、体液により膜15上に汚濁微粒子が捕捉され、固着
することを防止できる。配管30は、ケーシング27か
ら支持具(図示せず)によって固定支持される。膜15か
ら剥離され水面に浮遊する磁性フロック24は、例えば
表面磁場強度0.5テスラの永久磁石35及び支持体3
6で構成された磁場発生手段に近づくと、その外部の磁
気勾配により吸引され永久磁石35方向に移動する。移
動した磁性フロック38は、磁場発生手段の外側を回転
する非磁性のステンレス鋼製やプラスチック製等の回転
体の薄肉のシェル37面上に付着する。図において、反
時計回りに回転するシェル37(移動手段)上に付着し
た磁性フロック38は水面の大気部に露出される。この
時、磁性フロック38中の余分な水分は重力分離されて
シェル37面から流下し、もしくは滴下して、磁性フロ
ック38は含水率95%程度まで濃縮される。なお、永
久磁石35に代えて、コイル式常電導磁石やコイル式超
電導磁石、超電導バルク磁石等を用いても同様な効果が
得られる。シェル37は、その端部をフランジ39に接
合され、このフランジ39に接合されたロッド40がモ
ータ41によって回転駆動される。ロッド40はOリン
グ43で水密性を維持しながらケーシング27に支持さ
れる。モータ41はケーシング27に図示しない手段に
よって固定支持されている。シェル37の他端は、Oリ
ング43で水密性を維持しながらケーシング27に回転
可能に支持され、シェル37の内部は大気に開放されて
いる。永久磁石35は大気側から支持部材44を介し
て、ケーシング27に対し若干の隙間を有してボルト等
により固定支持される。この構造により、磁場発生手段
を容易にケーシング27の外部から自由に配置できる。
An electrolyzer 105 is provided in the middle of the pipe 104.
Is placed, and a part of the washing water is guided to the electrolyzer 105. The flow rate introduced into the electrolyzer 105 is adjusted by the flow rate adjusting valves 106 and 103. The washing water introduced into the electrolyzer 105 is electrolyzed to generate alkaline ionized water containing a large amount of OH negative ions in the anode (not shown), and the alkaline ionized water is supplied to the pipe 10
7 is connected to the pipe 26 via the flow rate adjusting valve 108 and returned to the reservoir 1. On the other hand, acidic water containing a large amount of H positive ions is generated at the cathode (not shown), and the acidic water is supplied from the pipe 104 to the pipe 3
0 to mix acidic water in the wash water. The deposits accumulated on the inner surface of the film 15 are separated by the shower water 32 sprayed from the inner surface, the surface of the film 15 is regenerated by separating the deposits, and the magnetic flocs 24 float on the surface of the pretreatment water 12. To do. At the same time, shower water 32
The membrane 15 is washed with the inside acidic water, and microorganisms such as bacteria attached to the membrane 15 are sterilized by the sterilizing action of the acidic water, and the microorganisms are prevented from propagating on the membrane 15. Also,
By preventing the microorganisms from propagating, the generation of a mucous body fluid generated from the body by the microorganisms is eliminated, and as a result, it is possible to prevent the polluted fine particles from being trapped and fixed on the membrane 15 by the body fluid. The pipe 30 is fixedly supported from the casing 27 by a support tool (not shown). The magnetic flocs 24 separated from the film 15 and floating on the water surface are, for example, the permanent magnet 35 having a surface magnetic field strength of 0.5 Tesla and the support body 3.
When approaching the magnetic field generating means configured by 6, the magnetic field is attracted by a magnetic gradient outside the magnetic field generating means and moves toward the permanent magnet 35. The moved magnetic flock 38 adheres to the surface of the thin shell 37 of the non-magnetic stainless steel or plastic rotating body that rotates outside the magnetic field generating means. In the figure, the magnetic flocs 38 attached on the shell 37 (moving means) rotating counterclockwise are exposed to the atmospheric portion of the water surface. At this time, excess water in the magnetic flocs 38 is gravity-separated and flows down or drops from the surface of the shell 37, so that the magnetic flocs 38 are concentrated to a water content of about 95%. The same effect can be obtained by using a coil type normal conducting magnet, a coil type superconducting magnet, a superconducting bulk magnet or the like instead of the permanent magnet 35. The shell 37 has its end portion joined to a flange 39, and a rod 40 joined to this flange 39 is rotationally driven by a motor 41. The rod 40 is supported by the casing 27 while maintaining watertightness by an O-ring 43. The motor 41 is fixedly supported by the casing 27 by means not shown. The other end of the shell 37 is rotatably supported by the casing 27 while maintaining watertightness by an O-ring 43, and the inside of the shell 37 is open to the atmosphere. The permanent magnet 35 is fixedly supported by bolts or the like from the atmosphere side through the support member 44 with a slight gap with respect to the casing 27. With this structure, the magnetic field generating means can be easily arranged freely from outside the casing 27.

【0021】シェル37面上の濃縮された磁性フロック
38は、シェル37とともに回転移動し、磁場発生手段
から遠ざかることによって磁気吸引力が小さくなり、掻
き取り手段としての平板状のへら42でシェル37面か
ら剥離され、スラッジ槽43にスラッジとして分離捕集
される。スラッジ槽43内のスラッジは、スラッジ槽4
3下部に配置したかき寄せ板44群とこれに結合された
ロッド45とをモータ46によって回転させ、図示上方
に移送して出口47から排出される。排出されたスラッ
ジは、配管48(図1参照)を通ってスラッジ槽49に
貯められる。スラッジ槽49に貯められたスラッジは、
含水率に約85%になるように、またコンポスト時の有
機物を分解する微生物の活性化を図れるように含水率が
約75%になるように、それぞれ運搬前もしくはコンポ
スト処理前に遠心分離機やベルトプレス機等の脱水手段
50によって濃縮される。スラッジは、例えばトラック
などで処分場や焼却場に運搬されるが、脱水手段50の
後段には堆肥化槽51が設けられ、堆肥化槽51に流路
52を通じて移送し、コンポスト化される。堆肥化した
後、堆肥を粉状に破砕し肥料中の磁性粉や生成磁性物質
を磁気分離装置(図示せず)で回収して再利用すること
もできる。
The concentrated magnetic flocs 38 on the surface of the shell 37 rotate together with the shell 37, and the magnetic attraction force becomes smaller as the magnetic flocs 38 move away from the magnetic field generating means, and the shell 37 is removed by a flat plate-like spatula 42 as scraping means. It is separated from the surface and separated and collected as sludge in the sludge tank 43. The sludge in the sludge tank 43 is the sludge tank 4
A group of scraping plates 44 arranged at the lower part of 3 and a rod 45 connected thereto are rotated by a motor 46, transferred to the upper side in the drawing, and discharged from an outlet 47. The discharged sludge is stored in the sludge tank 49 through the pipe 48 (see FIG. 1). The sludge stored in the sludge tank 49 is
A centrifuge or a centrifuge before transporting or composting so that the water content is about 85%, and the water content is about 75% so that the microorganisms that decompose organic matter during composting can be activated. It is concentrated by a dehydrating means 50 such as a belt press. The sludge is transported to a disposal site or an incineration site by, for example, a truck, and a composting tank 51 is provided after the dewatering means 50 and is transferred to the composting tank 51 through a flow path 52 to be composted. After composting, the compost can be crushed into powder, and the magnetic powder and the generated magnetic substance in the fertilizer can be recovered by a magnetic separator (not shown) and reused.

【0022】へら42の両側には側壁53を取り付け、
スラッジがケーシング27内に落下するのを防止する。
側壁53とへら42とはケーシング27に水密性を有し
て取り付けられ、へら42はスプリング等(図示せず)
で弾性的に先端をシェル37面上に押し付けられてい
る。へら42の先端は、例えば硬質ゴム等で構成する。
Side walls 53 are attached to both sides of the spatula 42,
It prevents sludge from falling into the casing 27.
The side wall 53 and the spatula 42 are watertightly attached to the casing 27, and the spatula 42 is a spring or the like (not shown).
The tip is elastically pressed against the surface of the shell 37. The tip of the spatula 42 is made of, for example, hard rubber or the like.

【0023】シャワー水32の水流がシェル37面上に
かかり、磁性フロック38が再び水を含むことのないよ
うに、ケーシング27から固定支持された非磁性物質の
仕切壁54を配置する。また、シェル37下部に、ケー
シング27から固定支持された非磁性物質の仕切壁55
を配置し、シャワー水32で膜15から剥離した磁性フ
ロック38が剥離場所から遠方に移動することを防止す
る。これによって、磁性フロック38は発生磁場内に浮
遊し、再度、磁気吸引されてシェル37面上に磁気捕捉
されるようになる。
A partition wall 54 of non-magnetic material fixedly supported by the casing 27 is arranged so that the water flow of the shower water 32 does not impinge on the surface of the shell 37 and the magnetic flocs 38 do not contain water again. In addition, a partition wall 55 of a non-magnetic material fixedly supported by the casing 27 is provided below the shell 37.
Is arranged to prevent the magnetic flocs 38 separated from the film 15 by the shower water 32 from moving away from the separation place. As a result, the magnetic flocs 38 float in the generated magnetic field, are magnetically attracted again, and are magnetically captured on the surface of the shell 37.

【0024】また、膜15内の浄化水をポンプ56の取
水口57から吸い込み、配管58を通ってシャワー管5
9に送り、孔から高圧のシャワー水60を、膜15内表
面から外面側に吹き付ける。膜15の外表面に残留蓄積
した堆積物はシャワー水で剥離されて膜15面は再生さ
れ、外側に設けたトレイ61に堆積物を含む洗浄水が溜
められる。この溜まった洗浄水は、排水口62から矢印
Cに示すように流れ(図1参照)、ポンプ63、配管6
4を通って原水貯槽5の上流側に戻され、再磁性化して
膜磁気分離装置14により汚泥として回収される。
Further, the purified water in the membrane 15 is sucked in from the intake port 57 of the pump 56, passes through the pipe 58, and the shower pipe 5
9, high pressure shower water 60 is sprayed from the inner surface of the film 15 to the outer surface side through the holes. The deposits remaining and accumulated on the outer surface of the film 15 are peeled off by shower water, the surface of the film 15 is regenerated, and the cleaning water containing the deposits is stored in the tray 61 provided outside. The accumulated cleaning water flows from the drain port 62 as shown by an arrow C (see FIG. 1), the pump 63, and the pipe 6
It is returned to the upstream side of the raw water storage tank 5 through 4 and re-magnetized to be recovered as sludge by the membrane magnetic separation device 14.

【0025】また、前処理水12の水位は、超音波液面計
200の信号を信号処理し、液面制御装置201に取り
込み、液面が所定値よりも上昇した場合、電源線202で
回転数制御されるモータ20の回転数を増し、前処理水
12中の膜15の滞留時間を短縮して膜15の濾過処理
量を増加させ、前処理水12の水位を低下させる制御を
行う。 逆に液面が所定値よりも下がった場合、モータ2
0の回転数を減らし、前処理水12中の膜15の滞留時
間を長くして膜15の濾過処理量を減少させ、前処理水
12の水位を上昇させる制御を行う。ここで、電気分解装
置105により酸性水を発生させる運転は、連続的でも
よく、またタイマー等によって断続的、周期的に運転する
方法でもよい。また、電気分解用の電力は太陽電池10
9、電源線110から受けてもよく、このため電気分解装
置105に蓄電池(図示せず)を搭載し、太陽電池109
からの電力を蓄え、雨天時に放電して電気分解を行うよ
うにしてもよい。また、アルカリイオン水を配管107か
ら配管113に弁112を介して合流させ、アルカリイ
オン水の凝集作用によって前処理水12中の凝集しなか
った浮遊粒子を予め凝集させ、これによって浮遊粒子が
膜15に付着することを防止することができる。さらに、
アルカリイオン水を配管107から原水貯槽5に弁11
2、配管113を介して合流させ、アルカリイオン水の凝
集作用によって原水中の浮遊粒子の一部を凝集させ、シ
ーディング剤調整装置7から供給する凝集剤の使用量を
低減することができる。さらに、電気分解槽105の陰極
から発生する水素ガスを配管205で燃料電池206に
導き、ここで大気中の酸素と化学反応させて発電し、蓄電
機能を有する電気分解槽105に電線207によって供
給して、電気分解槽105で発生する水素を有効に利用
することができる。このように水素を有効に利用するこ
とによって、電気分解槽の消費電力を低減できる効果が
あり、また水素ガスを装置外に放出しないことにより、水
素爆発などの危険を防止できる効果もある。以上に説明
する本実施例によれば、洗浄水の一部を電気分解槽に導
いて電気分解し、陽極側にOHイオンを多く含むアルカリ
イオン水と、陰極側にHイオンを多く含む酸性水を生成
させ、殺菌作用がある酸性水を再び洗浄水に混ぜ、通水
濾過分離膜をこの洗浄水で連続もしくは定期的に洗浄す
ることにより、水の浄化運転をしながら酸性水の殺菌作
用で膜上に付着したバクテリア等の微生物を殺菌し、微
生物が繁殖するのを防止することができる。また、微生物
が繁殖するのを防止することにより、微生物が体内から
発生する粘液性の体液の発生も無くなり、この体液によ
り網上に汚濁微粒子が捕捉、固着されることを防止する
ことができる。これらによって、通水濾過分離膜への異
物の固定化を防いで膜の目詰まりを防止し、通水濾過分
離膜の通水性能の低下を防ぐことができる、という効果
が生じる。
The water level of the pretreated water 12 is processed by the signal of the ultrasonic liquid level gauge 200 and taken into the liquid level control device 201, and when the liquid level rises above a predetermined value, it is rotated by the power line 202. The number of rotations of the motor 20 controlled by the number is increased, the residence time of the membrane 15 in the pretreated water 12 is shortened, the filtration treatment amount of the membrane 15 is increased, and the water level of the pretreated water 12 is lowered. On the contrary, if the liquid level drops below the specified value, the motor 2
The number of rotations of 0 is reduced, the residence time of the membrane 15 in the pretreated water 12 is lengthened to reduce the filtration treatment amount of the membrane 15, and the water level of the pretreated water 12 is increased. Here, the operation of generating acidic water by the electrolyzer 105 may be continuous, or may be a method of intermittently and periodically operating with a timer or the like. The power for electrolysis is the solar cell 10.
9, may receive from the power line 110, for this reason a storage battery (not shown) is mounted on the electrolyzer 105, and the solar cell 109
It is also possible to store the electric power from the battery and discharge it in the rain to perform electrolysis. Further, alkaline ionized water is joined from the pipe 107 to the pipe 113 via the valve 112, and the unaggregated suspended particles in the pretreated water 12 are aggregated in advance by the aggregation action of the alkaline ionized water, whereby the suspended particles form a film. It is possible to prevent the adhesion to 15. further,
Valve 11 for alkaline ionized water from pipe 107 to raw water storage tank 5
2. It is possible to reduce the amount of the coagulant supplied from the seeding agent adjusting device 7 by causing the particles to join through the pipe 113 to coagulate a part of the suspended particles in the raw water by the coagulation action of the alkaline ionized water. Further, hydrogen gas generated from the cathode of the electrolysis tank 105 is led to a fuel cell 206 through a pipe 205, where it chemically reacts with oxygen in the atmosphere to generate electricity, and is supplied to the electrolysis tank 105 having a power storage function by an electric wire 207. Then, the hydrogen generated in the electrolysis tank 105 can be effectively used. By effectively using hydrogen in this way, there is an effect that the power consumption of the electrolysis tank can be reduced, and there is also an effect that the danger of hydrogen explosion or the like can be prevented by not releasing the hydrogen gas outside the apparatus. According to the present embodiment described above, a part of the washing water is introduced into the electrolysis tank and electrolyzed, and alkaline ionized water containing a large amount of OH ions on the anode side and acidic water containing a large amount of H ions on the cathode side. By mixing the acidic water having a sterilizing action with the wash water again and continuously or periodically washing the water filtration separation membrane with the wash water, the sterilizing action of the acidic water can be achieved while purifying the water. Microorganisms such as bacteria attached to the membrane can be sterilized to prevent the microorganisms from propagating. Further, by preventing the microorganisms from propagating, the generation of mucous body fluid generated from the body by the microorganisms is eliminated, and it is possible to prevent the polluted fine particles from being trapped and fixed on the net by the body fluid. As a result, it is possible to prevent immobilization of foreign matter on the water filtration / separation membrane, prevent clogging of the membrane, and prevent deterioration of water permeability of the water filtration / separation membrane.

【0026】また、水中の浮遊粒子の付着防止作用を有
するアルカリイオン水を洗浄水に戻して混ぜ、通水濾過
分離膜をこの洗浄水で連続もしくは定期的に洗浄するこ
とによっても、膜の目詰まりを防止し、通水濾過分離膜の
通水性能の低下を防止できる、という効果が生じる。
The alkaline ionized water, which has the effect of preventing the adherence of suspended particles in water, is returned to the wash water and mixed, and the water filtration separation membrane is continuously or periodically washed with the wash water to form a membrane. It is possible to prevent clogging and prevent the deterioration of the water flow performance of the water filtration separation membrane.

【0027】一方、このアルカリイオン水は、魚等の微
生物に比べ大型の生物にとっては、体内の活性水として
有効であり、浄化水に混入することにより、浄化水を放
流する湖や河川の魚等の生物の発育を促進する効果もあ
る。
On the other hand, this alkaline ionized water is effective as active water in the body for organisms larger than microorganisms such as fish, and when mixed with purified water, fish in lakes and rivers that release purified water. It also has the effect of promoting the growth of organisms such as.

【0028】さらに、電気分解に使用する電力を太陽電
池で発生する電力で賄うことにより、日照強度の大きい
場合に大きな電力を発生することができて多量の酸性水
が得られる。この時、微生物の活動も活発となるので、微
生物の活動時間帯に合わせて殺菌作用を増加させること
ができ、消費電力を節減できる、という効果がある。な
お、上記実施例では膜濾過分離と磁気分離とを組み合わ
せた浄化装置について説明したが、膜濾過分離を有する
浄化装置において、膜を水道水もしくは浄化水の一部を
膜の洗浄水として使用する工場排水の浄化、下水の浄化
等の浄化装置などにも適用でき、同様な効果を得ること
ができる。
Further, by covering the electric power used for electrolysis with the electric power generated by the solar cell, it is possible to generate a large amount of electric power when the sunshine intensity is high, and a large amount of acidic water can be obtained. At this time, since the activity of the microorganisms is also active, there is an effect that the bactericidal action can be increased according to the activity time zone of the microorganisms, and the power consumption can be saved. In addition, in the above-mentioned embodiment, the purifying device in which the membrane filtration separation and the magnetic separation are combined has been described, but in the purification device having the membrane filtration separation, the membrane is used as tap water or a part of the purified water as washing water for the membrane. It can be applied to a purification device for purification of factory wastewater, purification of sewage, etc., and similar effects can be obtained.

【0029】[0029]

【発明の効果】以上説明したように本発明によれば、通
水濾過分離膜の洗浄水の一部をイオン化して洗浄水に殺
菌作用や凝集作用を持たせることにより、水の浄化運転
をしながら通水濾過分離膜への異物の固定化を防止し、
通水濾過分離膜の通水性能が低下しない水浄化装置を得
ることができる。
As described above, according to the present invention, a part of the wash water of the water filtration separation membrane is ionized to give the wash water a sterilizing action and a coagulating action, thereby performing a water purification operation. While preventing the immobilization of foreign matter on the water filtration membrane
It is possible to obtain a water purification device in which the water-passing performance of the water-passing filtration separation membrane does not deteriorate.

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

【図1】本発明に係る水浄化装置の使用状況を示す図で
ある。
FIG. 1 is a diagram showing a usage situation of a water purification apparatus according to the present invention.

【図2】水浄化装置の要部拡大横断面図である。FIG. 2 is an enlarged transverse cross-sectional view of a main part of the water purification device.

【図3】図2のX−X線に沿う断面図で、一部平面図で
ある。
3 is a cross-sectional view taken along line XX of FIG. 2 and is a partial plan view.

【符号の説明】[Explanation of symbols]

1…貯水池、3…フィルタ4,63,99…ポンプ、5
…原水貯槽、7…シーディング剤調整装置、9…攪拌
槽、10,20,41,46…モータ、11…攪拌翼、
12…前処理水、14…膜磁気分離装置、15…膜(濾
過手段)、16,17,37…シェル、18,39…フ
ランジ、24,38…磁性フロック、25…浄化水、2
7…ケーシング、28…ノズル、29…浄化水槽、3
1、59…シャワー管(洗浄手段)、32,60…シャ
ワー水、35…永久磁石、36…支持体、42…へら、
43…スラッジ槽、51…堆肥化槽、61…トレイ、1
01…流量調整用バイパス弁、103,106,108
…流量調整弁、105…電気分解装置、109…太陽電
池、200…超音波液面計、201…液面制御装置、2
06…燃料電池。
1 ... Reservoir, 3 ... Filter 4, 63, 99 ... Pump, 5
... Raw water storage tank, 7 ... Seeding agent adjusting device, 9 ... Stirring tank, 10, 20, 41, 46 ... Motor, 11 ... Stirring blade,
12 ... Pretreated water, 14 ... Membrane magnetic separation device, 15 ... Membrane (filtering means), 16, 17, 37 ... Shell, 18, 39 ... Flange, 24, 38 ... Magnetic floc, 25 ... Purified water, 2
7 ... Casing, 28 ... Nozzle, 29 ... Purified water tank, 3
1, 59 ... Shower pipe (cleaning means), 32, 60 ... Shower water, 35 ... Permanent magnet, 36 ... Support, 42 ... Spatula,
43 ... Sludge tank, 51 ... Composting tank, 61 ... Tray, 1
01 ... Flow control bypass valve, 103, 106, 108
... Flow rate adjusting valve, 105 ... Electrolyzer, 109 ... Solar cell, 200 ... Ultrasonic level gauge, 201 ... Liquid level control device, 2
06 ... Fuel cell.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 水守 隆司 茨城県土浦市神立町502番地 株式会社日 立製作所機械研究所内 Fターム(参考) 4D006 GA02 HA93 KA01 KA13 KA33 KB14 KC03 KC13 KC16 KC17 KD08 KD11 KD30 MA03 MB02 MC48 PA01 PB08 PB22 4D061 DA02 DB07 DB08 EA02 EB02 FA09    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Takashi Mizumori             502 Kintatemachi, Tsuchiura City, Ibaraki Japan             Tate Seisakusho Mechanical Research Center F-term (reference) 4D006 GA02 HA93 KA01 KA13 KA33                       KB14 KC03 KC13 KC16 KC17                       KD08 KD11 KD30 MA03 MB02                       MC48 PA01 PB08 PB22                 4D061 DA02 DB07 DB08 EA02 EB02                       FA09

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】前処理水に含まれる被除去物及び磁性物質
を捕捉し濾過して前記前処理水を浄化する濾過手段と、
この濾過手段の表面に捕捉されて堆積した被除去物及び
磁性物質を洗浄水で洗浄することによって前記濾過手段
から剥離する洗浄手段と、剥離された被除去物及び磁性
物質を前記前処理水の液面上に移動させる移動手段とを
備える水浄化装置において、 前記濾過された後の浄化水の流れる流路を分岐し、この
分岐した流路に、浄化水を酸性水とアリカリイオン水と
に電気分解する電気分解装置を設け、 この電気分解装置で生成された酸性水を前記洗浄水に戻
す流路を設けることを特徴とする水浄化装置。
1. Filtering means for purifying the pretreated water by capturing and filtering substances to be removed and magnetic substances contained in the pretreated water,
Cleaning means for separating the object to be removed and the magnetic substance trapped and deposited on the surface of the filtering means from the filtering means by cleaning with cleaning water, and the separated object to be removed and the magnetic substance to be removed from the pretreatment water. In a water purifying apparatus including a moving unit that moves the liquid to a liquid surface, a flow path through which the purified water after the filtration flows is branched, and the purified water is divided into acidic water and alkaline water in the branched flow path. A water purifying device comprising: an electrolyzer for electrolyzing, and a flow path for returning the acidic water produced by the electrolyzer to the washing water.
【請求項2】前処理水に含まれる被除去物及び磁性物質
を捕捉し濾過して前記前処理水を浄化する濾過手段と、
この濾過手段の表面に捕捉されて堆積した被除去物及び
磁性物質を洗浄水で濾過手段から剥離する洗浄手段と、
剥離した被除去物及び磁性物質を前記処理水の液面上ま
で移動させる移動手段とを備える水浄化装置において、 前記濾過された後の浄化水の流れる流路を分岐し、この
分岐した流路に、浄化水を酸性水とアリカリイオン水と
に電気分解する電気分解装置を設け、 この電気分解装置で生成されたアリカリイオン水を、前
記濾過された後の浄化水に合流させる流路を設けること
を特徴とする水浄化装置。
2. A filtering means for purifying the pretreated water by capturing and filtering substances to be removed and magnetic substances contained in the pretreated water,
Cleaning means for separating the object to be removed and the magnetic substance trapped and deposited on the surface of the filtering means from the filtering means with cleaning water,
In a water purifying apparatus comprising a moving means for moving the removed object to be removed and the magnetic substance to the liquid surface of the treated water, a flow path through which the purified water after the filtration flows is branched, and the branched flow path Is provided with an electrolyzer for electrolyzing purified water into acidic water and alkaline water, and a flow path is provided for joining the alkaline water produced by this electrolytic device with the filtered purified water. A water purification device characterized in that.
【請求項3】前処理水に含まれる被除去物及び磁性物質
を捕捉し濾過して前記前処理水を浄化する濾過手段と、
この濾過手段の表面に捕捉されて堆積した被除去物及び
磁性物質を洗浄水で濾過手段から剥離する洗浄手段と、
剥離した被除去物及び磁性物質を前記処理水の液面上ま
で移動させる移動手段とを備える水浄化装置において、 前記濾過された後の浄化水の流れる流路を分岐し、この
分岐した流路に、浄化水を酸性水とアリカリイオン水と
に電気分解する電気分解装置を設け、 この電気分解装置で生成されたアリカリイオン水を、前
記前処理水に合流させる流路を設けることを特徴とする
水浄化装置。
3. Filtering means for purifying the pretreated water by capturing and filtering the substances to be removed and magnetic substances contained in the pretreated water,
Cleaning means for separating the object to be removed and the magnetic substance trapped and deposited on the surface of the filtering means from the filtering means with cleaning water,
In a water purifying apparatus comprising a moving means for moving the removed object to be removed and the magnetic substance to the liquid surface of the treated water, a flow path through which the purified water after the filtration flows is branched, and the branched flow path In the above, an electrolyzer for electrolyzing purified water into acidic water and alkaline water is provided, and a channel for joining the alkaline water generated by the electrolytic apparatus with the pretreated water is provided. Water purification device.
【請求項4】前記分岐した流路に、電気分解装置に流れ
る浄化水を加圧する手段と、電気分解装置に流れる浄化
水の流量を調整する流量調整弁とを設けることを特徴と
する請求項1ないし3記載のいずれかの水浄化装置。
4. A means for pressurizing the purified water flowing into the electrolyzer and a flow rate adjusting valve for adjusting the flow rate of the purified water flowing into the electrolyzer are provided in the branched flow path. The water purifier according to any one of 1 to 3.
【請求項5】前記電気分解装置の電力の一部もしくは全
部を、太陽電池で発生する電力で賄うことを特徴とする
請求項1ないし3記載のいずれかの水浄化装置。
5. The water purifier according to claim 1, wherein a part or all of the electric power of the electrolyzer is covered by electric power generated by a solar cell.
【請求項6】前記電気分解装置で発生する水素ガスを空
気中の酸素と化学反応させ、この化学反応によって発電
する燃料電池発電手段を備えることを特徴とする請求項
1ない3記載のいずれかの水浄化装置。
6. The fuel cell power generation means for chemically reacting hydrogen gas generated in the electrolyzer with oxygen in the air to generate electricity by the chemical reaction, according to claim 1. Water purification equipment.
JP2001307323A 2001-10-03 2001-10-03 Water purification device Pending JP2003112180A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001307323A JP2003112180A (en) 2001-10-03 2001-10-03 Water purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001307323A JP2003112180A (en) 2001-10-03 2001-10-03 Water purification device

Publications (1)

Publication Number Publication Date
JP2003112180A true JP2003112180A (en) 2003-04-15

Family

ID=19126801

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001307323A Pending JP2003112180A (en) 2001-10-03 2001-10-03 Water purification device

Country Status (1)

Country Link
JP (1) JP2003112180A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004002900A1 (en) * 2002-06-26 2004-01-08 Hitachi, Ltd. Waste water purification apparatus and waste water purification method including the regeneration of used coagulant
JP2010005491A (en) * 2008-06-24 2010-01-14 Tokyo Metropolis Electrolytic phosphorus recovery device and sewage treatment system using it
CN110357368A (en) * 2019-08-15 2019-10-22 青岛富勒姆科技有限公司 A kind of laboratory integration wastewater treatment equipment and method
CN115092986A (en) * 2022-08-26 2022-09-23 山东北华环保股份有限公司 High-efficient environmental protection sewage treatment plant

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004002900A1 (en) * 2002-06-26 2004-01-08 Hitachi, Ltd. Waste water purification apparatus and waste water purification method including the regeneration of used coagulant
US7410573B2 (en) 2002-06-26 2008-08-12 Hitachi, Ltd. Waste water purification apparatus and waste water purification method including the regeneration of used coagulant
JP2010005491A (en) * 2008-06-24 2010-01-14 Tokyo Metropolis Electrolytic phosphorus recovery device and sewage treatment system using it
CN110357368A (en) * 2019-08-15 2019-10-22 青岛富勒姆科技有限公司 A kind of laboratory integration wastewater treatment equipment and method
CN115092986A (en) * 2022-08-26 2022-09-23 山东北华环保股份有限公司 High-efficient environmental protection sewage treatment plant

Similar Documents

Publication Publication Date Title
JP4186523B2 (en) Waste water purification device and waste water purification system
CN101460408B (en) Method and device for wastewater purification
CN100553785C (en) Magnetic separation and purification device and magnetic separation and purification method
JP4317668B2 (en) Membrane magnetic separator
KR101702345B1 (en) Apparatus and Method for Removing Algae
CN107572715A (en) A kind of industrial wastewater treatment system
JP2000176455A (en) Treatment device and method for phosphate ion- containing water
CN109095692A (en) A kind of processing system and processing method of electroplating wastewater bio-chemical effluent
JP2005111424A (en) Method and apparatus for removing object to be removed from fluid and sludge separation and recovery device
CN102145949A (en) Tanning advanced treatment wastewater recycling device and method
JP2005218887A (en) Shipboard pollution water purification system
JP2003112180A (en) Water purification device
KR101913754B1 (en) Apparatus of solid-liquid separation comprising settling tank and floatation separation tank and method using the same
CN108975565A (en) A kind of steel and iron industry strong brine processing unit and method
CN113856254A (en) Inclined tube sedimentation tank capable of being cleaned on line
KR20180005955A (en) Movable Vehicle Type Desalination Apparatus of Brackish Water and Method of Converting Brackish Water to Agricultural Water Using the Same
RU2376248C1 (en) Method of removing suspended particles from liquids and device for removing suspended particles from liquids
CN109987815A (en) A kind of purification of circulating water pool dirt and bottom of pond mud Hand scarf system and method
JP3423386B2 (en) Sludge dewatering method by direct electrolytic treatment and dewatering device therefor
CN207435202U (en) A kind of wastewater treatment unit
JP3309736B2 (en) Sewage treatment method and sewage treatment device
CN113443758A (en) Full-quantitative pretreatment device, treatment system and treatment method for landfill leachate
CN202089868U (en) Recycled water manufacturing device based on electrolysis and double-film technology
CN207451820U (en) A kind of industrial wastewater treatment system
JP2000176482A (en) Sewage treatment device