JPH05305281A - Water purifier - Google Patents

Water purifier

Info

Publication number
JPH05305281A
JPH05305281A JP4109493A JP10949392A JPH05305281A JP H05305281 A JPH05305281 A JP H05305281A JP 4109493 A JP4109493 A JP 4109493A JP 10949392 A JP10949392 A JP 10949392A JP H05305281 A JPH05305281 A JP H05305281A
Authority
JP
Japan
Prior art keywords
water
purification cartridge
water purifier
water purification
porous
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
JP4109493A
Other languages
Japanese (ja)
Inventor
Juichi Nishikawa
壽一 西川
Hideo Iwata
秀雄 岩田
Mikio Shinagawa
幹夫 品川
Norihiko Kawamura
典彦 河村
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP4109493A priority Critical patent/JPH05305281A/en
Publication of JPH05305281A publication Critical patent/JPH05305281A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/36Organic compounds containing halogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Water Treatment By Sorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To provide a water purifier which uses a porous adsorbent resin as an adsorbent for removing moldy odor and trihalomethane, further, regenerating the porous adsorbent resin using an electrolytic device and is capable of bacteriostatic with long service life. CONSTITUTION:The subject water purifier comprises a water purification cartridge 7 filled with porous adsorbent resin 10-A and a regeneration device of the water purification cartridge 7.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、浄水器に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purifier.

【0002】[0002]

【従来の技術】浄水器は家庭用から業務用に至るまで広
く使用されており,その多くは活性炭を用いて処理する
ものである。そして、これらの浄水器に使用される活性
炭はカートリッジとして組み込まれ、塩素やかび臭を除
去する能力がなくなったときに活性炭カートリッジを交
換するというものである。特に家庭用の浄水器では活性
炭カートリッジが小さいため1カ月から半年毎に活性炭
カートリッジの交換が必要となり面倒であるという欠点
があった。さらに、近年活性炭で塩素を除去するために
雑菌が繁殖するということから中空糸膜フィルターを組
み込んだ物、抗菌活性炭等を使用した物など高価な活性
炭カートリッジが増えておりランニングコストが高くつ
いている。
2. Description of the Related Art Water purifiers are widely used for household and commercial purposes, and most of them are treated with activated carbon. The activated carbon used in these water purifiers is incorporated as a cartridge, and when the ability to remove chlorine and musty odor is lost, the activated carbon cartridge is replaced. In particular, the water purifier for home use has a drawback that the activated carbon cartridge is small, and the activated carbon cartridge needs to be replaced every six months, which is troublesome. Further, in recent years, since various bacteria propagate to remove chlorine with activated carbon, expensive activated carbon cartridges, such as those incorporating a hollow fiber membrane filter and those using antibacterial activated carbon, are increasing in number, resulting in high running costs.

【0003】ところで、多孔性吸着樹脂については、水
処理や食品の脱色に用いられた例はあるが、浄水器、特
に家庭用の浄水器では、多孔性吸着樹脂が乾燥すると収
縮してしまい細孔が潰れて、吸着力が無くなってしまう
ことと、湿潤状態では嫌気性の細菌が繁殖してしまうこ
とがあり実用化されていなかった。
There are some examples of porous adsorbent resins used for water treatment and decolorization of foods, but in water purifiers, especially household water purifiers, when the porous adsorbent resin dries, it shrinks. Since the pores are crushed and the adsorptivity is lost, and anaerobic bacteria may grow in a wet state, they have not been put into practical use.

【0004】[0004]

【発明が解決しようとする課題】本発明は、以上の欠点
を解決するために提案されたもので、カートリッジ寿命
の長い浄水器を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been proposed to solve the above drawbacks, and an object thereof is to provide a water purifier having a long cartridge life.

【0005】[0005]

【課題を解決するための手段】本発明の要旨とするとこ
ろは、請求項1記載のように多孔性吸着樹脂10−Aを
充填してなる浄水カートリッジ7及び前記浄水カートリ
ッジ7の再生装置を有することを特徴とする浄水器であ
り、また請求項2に記載のように多孔性吸着樹脂10−
Aの下流側に活性炭10−B層を設けたことを特徴とす
る請求項1記載の浄水器であり、また請求項3に記載の
ように浄水カートリッジ7の再生装置が陽極と陰極12
−a、12−b、及び電解隔膜11により構成される電
気分解装置であることを特徴とする請求項1記載の浄水
器である。
SUMMARY OF THE INVENTION The gist of the present invention is to have a water purification cartridge 7 filled with a porous adsorption resin 10-A as set forth in claim 1 and a regeneration device for the water purification cartridge 7. A water purifier characterized in that the porous adsorbent resin 10-as described in claim 2.
The water purifier according to claim 1, wherein an activated carbon 10-B layer is provided on the downstream side of A, and the regeneration device of the water purification cartridge 7 according to claim 3 has an anode and a cathode 12.
The water purifier according to claim 1, which is an electrolyzer configured by -a, 12-b, and the electrolytic diaphragm 11.

【0006】上水中に含まれる物質で除去すべき物質と
して、塩素臭、かび臭、トリハロメタン、鉄錆、有機物
質があり、飲料水として特に問題になるのは塩素臭であ
る次亜塩素酸、2−MIB(2−Methylisob
orneol)やジオスミン等のかび臭、トリハロメタ
ンである。
The substances contained in the tap water that should be removed include chlorine odor, musty odor, trihalomethane, iron rust, and organic substances. The problem of drinking water is the chlorine odor of hypochlorous acid, 2 -MIB (2-Methylisob
mustard odor such as orneol) and diosmin, and trihalomethane.

【0007】本発明では、上水処理用の吸着剤として多
孔性吸着樹脂を用いる。そのことにより塩素臭は下記の
式 Cl2 +H2 O ←→ HClO+HCl (1−1) HClO → HCl+(O) (1−2) に示すように無臭の塩素イオンへと分解され、かび臭、
トリハロメタン及び有機物はそれぞれ吸着除去される。
In the present invention, a porous adsorption resin is used as an adsorbent for treating clean water. As a result, the chlorine odor is decomposed into odorless chlorine ions as shown in the following formula Cl 2 + H 2 O ← → HClO + HCl (1-1) HClO → HCl + (O) (1-2), and musty odor,
Trihalomethane and organic matter are adsorbed and removed, respectively.

【0008】ここで、多孔性吸着樹脂について説明を加
える。イオン交換樹脂のようなポリマーに溶質を吸着さ
せる時、溶質はその表面のみならず内部にも拡散、浸透
して吸着される。この拡散、浸透はポリマーの持つ細孔
が溶質の通路の役目を果たし、この細孔の容積の大きい
ものが多孔性吸着樹脂と言われる。また、この細孔は高
分子鎖相互の間、又は高分子鎖と架橋との間で形成さ
れ、イオン交換樹脂において典型的に起きるが、電解室
濃度や、溶媒の性質、イオン交換基に吸着されているイ
オンの性質、さらに温度等、さまざまな因子により影響
を受ける。そのため多孔性吸着樹脂の特性により様々な
再生方法が採られている。
Here, the porous adsorption resin will be described. When a solute is adsorbed by a polymer such as an ion exchange resin, the solute diffuses and permeates not only the surface but also the inside and is adsorbed. For this diffusion and permeation, the pores of the polymer play the role of solute passages, and the one having a large volume of this pore is called a porous adsorption resin. Also, these pores are formed between polymer chains or between polymer chains and crosslinks, which typically occurs in ion exchange resins, but they are adsorbed on the concentration of the electrolytic chamber, the nature of the solvent, and the ion exchange groups. It is affected by various factors such as the nature of the ions being formed and temperature. Therefore, various regeneration methods are adopted depending on the characteristics of the porous adsorption resin.

【0009】本発明では飲料水中の有機物の除去を考え
ており、芳香族ポリマーの表面にアミン基等の塩基性
基、及びフェノール性OH基等の酸性基が共存する多孔
性吸着樹脂を使用する。そして、この多孔性樹脂の再生
は図3に示すように多孔性吸着樹脂の吸着特性が酸性か
ら弱アルカリにかけて吸着量が大きく、強アルカリにな
ると急激に小さくなるというpH依存性が大きいことを
利用して行う。
In the present invention, removal of organic substances in drinking water is considered, and a porous adsorption resin in which basic groups such as amine groups and acidic groups such as phenolic OH groups coexist on the surface of the aromatic polymer is used. . As shown in FIG. 3, the regeneration of the porous resin utilizes the fact that the adsorption characteristics of the porous adsorption resin have a large adsorption amount from acidic to weak alkali and sharply decrease when it becomes strong alkali, which is highly dependent on pH. Then do.

【0010】また、多孔性吸着樹脂は活性炭と比べて比
表面積は約3分の1と小さく、家庭用の浄水器のように
小型化が必要な場合、トリハロメタンや微小有機物を処
理しきれない。そのような場合、多孔性吸着樹脂の下流
側に活性炭層を設けるシステムとする。
Further, the porous adsorbent resin has a small specific surface area, which is about one-third of that of activated carbon, and cannot treat trihalomethane and minute organic substances when it is required to be downsized as in a domestic water purifier. In such a case, the activated carbon layer is provided on the downstream side of the porous adsorption resin.

【0011】従って、本発明の浄水器では多孔性吸着樹
脂の充填された浄水カートリッジにより、また、場合に
よって、多孔性吸着樹脂と直列に活性炭層を設けて上水
を浄化し、さらに、前記浄水カートリッジの再生装置を
有する構成とする。
Therefore, in the water purifier of the present invention, an activated carbon layer is provided in series with the water adsorption cartridge filled with the porous adsorption resin, and in some cases, in series with the porous adsorption resin to purify tap water. It is configured to have a cartridge reproducing device.

【0012】再生装置は、コンパクトで、さらに廃液処
理の簡単な電気分解装置とする。雑菌対策については、
浄水器が長時間使用されない場合、電気分解により製造
される酸性の水を浄水カートリッジへ送ることにより静
菌を行う。
The regenerator is an electrolyzer which is compact and easy for waste liquid treatment. About measures against various bacteria,
When the water purifier is not used for a long time, bacteriostatic is performed by sending acidic water produced by electrolysis to a water purification cartridge.

【0013】[0013]

【実施例】次に本発明の実施例について説明する。尚、
実施例は一つの例示であって、本発明の精神を逸脱しな
い範囲で種々の変更あるいは改良を行いうることは言う
までもない。
EXAMPLES Next, examples of the present invention will be described. still,
Needless to say, the embodiment is merely an example, and various modifications and improvements can be made without departing from the spirit of the present invention.

【0014】まず、図1に従って本発明の第1の実施例
の浄水器の構成について説明する。本体1背面に水道水
取り入れ用の流入口2、及び浄水カートリッジ7及び、
電気分解装置8から出る排水を排出するの排水口3が設
けられている。本体1内部には浄水カートリッジ7、電
気分解装置8、本体1内部の上部に位置する電気コント
ローラー9及び電磁弁13、14、15、逆止弁16を
含む配管系が収納されている。浄水カートリッジ7は鉛
直方向に設置される筒体で、下部に流入口、上部に流出
口を有する。そして、前記浄水カートリッジ7内に多孔
性吸着樹脂10−Aが充填されている。電気分解装置8
は鉛直方向に設置されており、その内部は電解隔膜11
により2つの部屋に仕切られ、それぞれ電極12−a、
12−bが設けられている。この電解隔膜11は下方に
隙間があり下部の流入口より入った水は2つの部屋に通
じるが、電解隔膜11のある高さではイオンは電解隔膜
11を通じて相互の部屋に移動するが、水は移動しない
ような構成にされている。また、それぞれの部屋の上方
には流出口が設けられている。電極12−a、12−b
は電気コントローラ9に接続されており各電極を陰極に
でも陽極にでも切り替え可能となっている。浄水カート
リッジ7と電気分解装置8は給水スイッチ5、電磁弁1
3、14、15、逆止弁16を介して図2のようにそれ
ぞれ配管されている。 他に、図2に本発明の第2の実
施例の浄水器の構成について示す。構成は第1の実施例
の浄水器とほぼ同じであり、浄水カートリッジ7の内部
が多孔板で上下に仕切られ、下方に多孔性吸着樹脂10
−A、上方に活性炭10−Bが充填された構造となって
いる。第2の実施例では、活性炭10−Bによる浄化効
果も期待できる。
First, the construction of the water purifier according to the first embodiment of the present invention will be described with reference to FIG. Inlet 2 for tap water intake on the back of the main body 1, and a water purification cartridge 7,
A drainage port 3 for discharging the drainage discharged from the electrolyzer 8 is provided. Inside the main body 1, a water purification cartridge 7, an electrolyzer 8, a pipe system including an electric controller 9 located above the main body 1 and solenoid valves 13, 14, 15 and a check valve 16 are housed. The water purification cartridge 7 is a cylindrical body installed in the vertical direction, and has an inflow port in the lower part and an outflow port in the upper part. Then, the water purification cartridge 7 is filled with the porous adsorption resin 10-A. Electrolyzer 8
Is installed in the vertical direction, and the inside is an electrolytic diaphragm 11
Is divided into two rooms by the electrodes 12-a,
12-b is provided. The electrolytic diaphragm 11 has a gap below and the water entering from the lower inlet is communicated to the two chambers. At a certain height of the electrolytic diaphragm 11, the ions move to the other chambers through the electrolytic diaphragm 11, but the water is It is structured so that it does not move. An outlet is provided above each room. Electrodes 12-a, 12-b
Is connected to an electric controller 9 and each electrode can be switched to a cathode or an anode. Water purification cartridge 7 and electrolyzer 8 are water supply switch 5, solenoid valve 1
Pipes are provided as shown in FIG. 2 through 3, 14, 15 and the check valve 16. In addition, FIG. 2 shows the configuration of a water purifier according to a second embodiment of the present invention. The structure is almost the same as that of the water purifier of the first embodiment, and the inside of the water purification cartridge 7 is vertically partitioned by a porous plate, and the porous adsorption resin 10 is provided below.
-A, activated carbon 10-B is filled above. In the second embodiment, the purifying effect of activated carbon 10-B can be expected.

【0015】次に、動作について説明する。まず上水を
浄化する場合では、電磁弁13、14は実線矢印で示す
方向に切り替えられ、電磁弁15は閉じられている。そ
して、水道水は浄水カートリッジ7下部の流入口より供
給され多孔性吸着樹脂10−Aで浄化された後、上部の
流出口から吐出口4へ給水される。
Next, the operation will be described. First, in the case of purifying clean water, the solenoid valves 13 and 14 are switched in the directions indicated by solid arrows, and the solenoid valve 15 is closed. Then, the tap water is supplied from the inlet at the bottom of the water purification cartridge 7 and purified by the porous adsorption resin 10-A, and then is supplied to the outlet 4 from the outlet at the upper part.

【0016】一方、多孔性吸着樹脂10−Aの再生時の
場合、電磁弁13、14、は点線矢印で示す方向に切り
替えられ、電磁弁15は開けられている。再生の第1段
階、即ち多孔性吸着樹脂10−Aの再生段階では、水道
水はまず電気分解装置8へ供給され、一部は陰極になる
よう操作された電極12−aの部屋に送られアルカリ性
の水となり、浄水カートリッジ7へ送られ多孔性吸着樹
脂10−Aに吸着していた有機物成分を脱離させる。浄
水カートリッジ7通過後の排水は、電気分解装置8で同
時に陽極の電極12−bの部屋でできる酸性の水と混合
して中和した後排水口3より排出される。次に、第2段
階ではアルカリ性になった浄水カートリッジ7を中和す
る操作を行う。ここでは電極を第1段階とは逆に、即ち
電極12−aを陽極に、12−bを陰極にする。そうす
ることにより電気分解装置8の電極12−aの部屋で酸
性の水が得られるので、それを浄水カートリッジ7へ送
り中和する。浄水カートリッジ7通過後の排水は先ほど
と同様に電気分解装置8で同時に陰極の電極12−bの
部屋でできるアルカリ性の水と混合して中和した後、排
水口3より排出される。
On the other hand, when the porous adsorbent resin 10-A is regenerated, the solenoid valves 13 and 14 are switched to the direction shown by the dotted arrow and the solenoid valve 15 is opened. In the first stage of regeneration, ie the stage of regeneration of the porous adsorbent resin 10-A, tap water is first supplied to the electrolyzer 8 and partly sent to the chamber of the electrode 12-a which is operated to be the cathode. It becomes alkaline water and is sent to the water purification cartridge 7 to desorb the organic component adsorbed on the porous adsorption resin 10-A. The wastewater after passing through the water purification cartridge 7 is simultaneously mixed in the electrolyzer 8 with acidic water produced in the room of the anode electrode 12-b, and then neutralized, and then discharged from the drainage port 3. Next, in the second step, an operation of neutralizing the water purification cartridge 7 that has become alkaline is performed. Here, the electrodes are opposite to those in the first stage, that is, the electrodes 12-a are the anodes and 12-b are the cathodes. By doing so, acidic water is obtained in the room of the electrode 12-a of the electrolyzer 8, and is sent to the water purification cartridge 7 for neutralization. The drainage after passing through the water purification cartridge 7 is similarly mixed with alkaline water formed in the room of the cathode electrode 12-b in the electrolyzer 8 at the same time to be neutralized, and then discharged from the drainage port 3.

【0017】また、浄水器が長時間使用されない場合、
先ほどの多孔性吸着樹脂10−Aの再生後の中和操作と
同様にして、電気分解装置8により製造される酸性の水
を浄水カートリッジ7へ送ることにより静菌を行う。
When the water purifier is not used for a long time,
Similarly to the neutralization operation after the regeneration of the porous adsorption resin 10-A, the acidic water produced by the electrolyzer 8 is sent to the water purification cartridge 7 to perform bacteriostatic treatment.

【0018】[0018]

【発明の効果】本発明は上記にように吸着剤として多孔
性吸着樹脂を用い、さらに電気分解装置により前記多孔
性吸着樹脂を再生することができ、また、静菌すること
ができるのでカートリッジ寿命の長い浄水器を提供する
ことができるという効果を有する。
INDUSTRIAL APPLICABILITY As described above, the present invention uses the porous adsorbent resin as the adsorbent, and the porous adsorbent resin can be regenerated by the electrolyzer, and the bacteriostatic can be performed, so that the cartridge life is shortened. It has the effect that a water purifier with a long length can be provided.

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

【図 1】本発明の第1の実施例の浄水器を示す断面図
である。
FIG. 1 is a sectional view showing a water purifier according to a first embodiment of the present invention.

【図 2】本発明の第2の実施例の浄水器を示す断面図
である。
FIG. 2 is a sectional view showing a water purifier according to a second embodiment of the present invention.

【図 3】本発明に使用する多孔性吸着樹脂の色素の除
去率のpH依存性を示す図である。
FIG. 3 is a diagram showing the pH dependence of the dye removal rate of the porous adsorption resin used in the present invention.

【符号の説明】[Explanation of symbols]

1 本体 2 流入口 3 排水口 4 吐出口 5 給水スイッチ 6 電源コード 7 浄水カートリッジ 8 電気分解装置 9 電気コントローラー 10−A 多孔性吸着樹脂 10−B 活性炭 11 電解隔膜 12−a 電極 12−b 電極 13 電磁弁 14 電磁弁 15 電磁弁 16 逆止弁 1 Main Body 2 Inlet 3 Drain 4 Outlet 5 Water Switch 6 Power Cord 7 Water Purification Cartridge 8 Electrolyzer 9 Electric Controller 10-A Porous Adsorption Resin 10-B Activated Carbon 11 Electrolytic Separator 12-a Electrode 12-b Electrode 13 Solenoid valve 14 Solenoid valve 15 Solenoid valve 16 Check valve

───────────────────────────────────────────────────── フロントページの続き (72)発明者 河村 典彦 大阪府門真市大字門真1048番地松下電工株 式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Norihiko Kawamura 1048 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Works Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 多孔性吸着樹脂10−Aを充填してなる
浄水カートリッジ7及び前記浄水カートリッジ7の再生
装置を有することを特徴とする浄水器。
1. A water purifier comprising a water purification cartridge 7 filled with a porous adsorption resin 10-A and a regeneration device for the water purification cartridge 7.
【請求項2】 多孔性吸着樹脂10−Aの下流側に活性
炭10−B層を設けたことを特徴とする請求項1記載の
浄水器。
2. The water purifier according to claim 1, wherein an activated carbon 10-B layer is provided on the downstream side of the porous adsorption resin 10-A.
【請求項3】 浄水カートリッジ7の再生装置が陽極と
陰極12−a、12−b、及び電解隔膜11により構成
される電気分解装置であることを特徴とする請求項1記
載の浄水器。
3. The water purifier according to claim 1, wherein the regenerator for the water purification cartridge 7 is an electrolyzer comprising an anode and a cathode 12-a, 12-b, and an electrolytic diaphragm 11.
JP4109493A 1992-04-28 1992-04-28 Water purifier Pending JPH05305281A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4109493A JPH05305281A (en) 1992-04-28 1992-04-28 Water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4109493A JPH05305281A (en) 1992-04-28 1992-04-28 Water purifier

Publications (1)

Publication Number Publication Date
JPH05305281A true JPH05305281A (en) 1993-11-19

Family

ID=14511651

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4109493A Pending JPH05305281A (en) 1992-04-28 1992-04-28 Water purifier

Country Status (1)

Country Link
JP (1) JPH05305281A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007125334A1 (en) * 2006-04-28 2007-11-08 Arvia Technology Limited Apparatus for the electrochemical regeneration of absorbents
JP2008272594A (en) * 2007-03-09 2008-11-13 Okayama Univ Electrolytic reduction dehalogenation method for activated carbon adsorbed organic halide
WO2010128298A1 (en) * 2009-05-06 2010-11-11 Arvia Technology Limited Treatment of contaminated liquids
WO2010149982A1 (en) * 2009-06-25 2010-12-29 Arvia Technology Limited Treatment of liquid with oily contaminants

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007125334A1 (en) * 2006-04-28 2007-11-08 Arvia Technology Limited Apparatus for the electrochemical regeneration of absorbents
GB2438850A (en) * 2006-04-28 2007-12-12 Univ Manchester Apparatus for treating liquid using regeneratable adsorbent material
GB2438850B (en) * 2006-04-28 2010-04-21 Univ Manchester Liquid treatment apparatus
US7790024B2 (en) 2006-04-28 2010-09-07 Arvia Technology Limited Apparatus for the electrochemical regeneration of absorbents
AU2007245405B2 (en) * 2006-04-28 2011-05-12 Arvia Technology Limited Apparatus for the electrochemical regeneration of absorbents
JP2008272594A (en) * 2007-03-09 2008-11-13 Okayama Univ Electrolytic reduction dehalogenation method for activated carbon adsorbed organic halide
WO2010128298A1 (en) * 2009-05-06 2010-11-11 Arvia Technology Limited Treatment of contaminated liquids
EP2427408A1 (en) * 2009-05-06 2012-03-14 Arvia Technology Limited Treatment of contaminated liquids
US8936726B2 (en) 2009-05-06 2015-01-20 Arvia Technology Limited Treatment of contaminated liquids
WO2010149982A1 (en) * 2009-06-25 2010-12-29 Arvia Technology Limited Treatment of liquid with oily contaminants
GB2486130A (en) * 2009-06-25 2012-06-06 Arvia Technology Ltd Treatment of liquid with oily contaminants
GB2486130B (en) * 2009-06-25 2013-04-17 Arvia Technology Ltd Treatment of liquid with oily contaminants

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