JPH07204635A - Water purifier - Google Patents

Water purifier

Info

Publication number
JPH07204635A
JPH07204635A JP2193494A JP2193494A JPH07204635A JP H07204635 A JPH07204635 A JP H07204635A JP 2193494 A JP2193494 A JP 2193494A JP 2193494 A JP2193494 A JP 2193494A JP H07204635 A JPH07204635 A JP H07204635A
Authority
JP
Japan
Prior art keywords
ceramic
aqueous solution
activated
water purifier
water
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
JP2193494A
Other languages
Japanese (ja)
Inventor
Shinji Makino
伸治 牧野
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.)
I B II KK
Original Assignee
I B II KK
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 I B II KK filed Critical I B II KK
Priority to JP2193494A priority Critical patent/JPH07204635A/en
Publication of JPH07204635A publication Critical patent/JPH07204635A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To remove microbes by installing a ceramic filter and a bacteria- removing filter and further installing a check valve in the outlet side of the bacterial removing filter, wherein the ceramic filter consists of activated ceramic which is treated by bringing it into contact with air led through an aqueous solution. CONSTITUTION:Tap water whose quality is improved by a ceramic filter 8 consisting of activated ceramic is introduced into a bacteria removing filter 9, wherein the activated ceramic is treated by bringing it into contact with air led through an aqueous solution. The bacteria-removing filter 9 is composed by laminating hollow fiber membranes 9A and forming a leading inlet 9B in the lower part of the outer circumference of the bacteria removing filter 9, and moreover a check valve 12 and a magnet 13 are set in the outlet side of the bacteria removing filter 9, that is in the inside of a water suppling pipe 11. Consequently, even if tap water is polluted with microbes proparaged in the inside of a cartridge 4 due to no use for a long duration, the microbes are removed by fine filtration by the hollow fiber membranes 9A.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は水を濾過除菌する浄水器
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 for filtering and sterilizing water.

【0002】[0002]

【従来の技術】従来、浄水器としては活性炭層、コーラ
ルサンド層等で固形分の濾過、有機物や塩素等の吸着を
行なっていた。
2. Description of the Related Art Conventionally, as a water purifier, an active carbon layer, a coral sand layer, etc. have been used to filter solids and to adsorb organic substances and chlorine.

【0003】[0003]

【発明が解決しようとする課題】しかしながら上記従来
の浄水器では、該浄水器を長期間使用しないときには微
生物が内部で繁殖するという問題点があった。また従来
の浄水器は単に固形物、塩素、有機物等を除去するだけ
で、水自体を活性化したり改質したりすることができな
かった。
However, the above-mentioned conventional water purifier has a problem that microorganisms propagate therein when the water purifier is not used for a long period of time. Further, the conventional water purifier cannot remove the solid matter, chlorine, organic matter, etc., but cannot activate or modify the water itself.

【0004】[0004]

【課題を解決するための手段】本発明は上記従来の課題
を解決するための手段として、セラミック濾過層(8)と
除菌フィルター(9) とからなる浄水器(1) を提供するも
のである。該セラミック濾過層(8) としては塩化第二鉄
を大量のカセイソーダ水溶液に溶かした後塩酸で中和
し、濃縮して得られた結晶および/または硫酸第一鉄を
大量の塩酸水溶液に溶かした後濃縮して得られた結晶の
水溶液に浸漬処理および/または該水溶液に通した空気
に接触処理された活性化セラミックを使用することが望
ましく、更に該除菌フィルター(9) の出口側には逆止弁
(12)を取付けることが望ましい。
The present invention provides a water purifier (1) comprising a ceramic filter layer (8) and a sterilization filter (9) as a means for solving the above conventional problems. is there. As the ceramic filtration layer (8), ferric chloride was dissolved in a large amount of caustic soda aqueous solution, neutralized with hydrochloric acid, and concentrated to obtain crystals and / or ferrous sulfate dissolved in a large amount of hydrochloric acid aqueous solution. It is desirable to use an activated ceramic that has been subjected to immersion treatment in an aqueous solution of crystals obtained by post-concentration and / or contact treatment with air passing through the aqueous solution, and further to the outlet side of the sterilization filter (9). Check valve
It is desirable to install (12).

【0005】[0005]

【作用】水はセラミック濾過槽(8) を通過する際に固形
物、有機物、塩素等を除去されるが、同時に該セラミッ
ク濾過層の遠赤外線作用によって水のクラスターが細分
化され改質される。そして長期間の不使用中にセラミッ
ク濾過槽(8) 内に微生物が繁殖し、該水が該微生物によ
って汚染された場合でも、該除菌フィルターにより該微
生物は除去される。
[Action] Water passes through the ceramic filter tank (8) to remove solids, organic substances, chlorine, etc., but at the same time, the far infrared ray action of the ceramic filter layer subdivides and modifies water clusters. . Even when microorganisms propagate in the ceramic filtration tank (8) during a long period of nonuse and the water is contaminated with the microorganisms, the microorganisms are removed by the sterilization filter.

【0006】塩化第二鉄を大量のカセイソーダ水溶液に
溶かすと、塩化第二鉄を構成する鉄が活性化するものと
思われる。このように活性化した鉄を含む水溶液を塩酸
で中和すると、活性化した鉄の塩化物が結晶として得ら
れる。また硫酸第一鉄を大量の塩酸水溶液に溶かすと、
硫酸第一鉄を構成する鉄が活性化するものと思われる。
このように活性化した鉄を含む水溶液を濃縮すると、活
性化した鉄の塩化物が結晶として得られる。上記両方法
で得られた該結晶は望ましくは更にイソプロパノール−
水混合液に溶解させ、濃縮再結晶することによって精製
される。そこでこのような活性化した鉄の塩化物の水溶
液にセラミックを浸漬したり、あるいは該水溶液を通し
た空気をセラミックに接触させたりすると、セラミック
の上記効果が増幅される。
It is considered that when ferric chloride is dissolved in a large amount of caustic soda aqueous solution, the iron constituting ferric chloride is activated. When the aqueous solution containing activated iron is neutralized with hydrochloric acid, activated iron chloride is obtained as crystals. Also, when ferrous sulfate is dissolved in a large amount of hydrochloric acid aqueous solution,
It seems that the iron that constitutes ferrous sulfate is activated.
When the aqueous solution containing activated iron is concentrated, activated iron chloride is obtained as crystals. The crystals obtained by both of the above methods are preferably further isopropanol-
It is purified by dissolving in a water mixture and concentrating and recrystallizing. Therefore, when the ceramic is immersed in such an activated iron chloride aqueous solution, or when the air passing through the aqueous solution is brought into contact with the ceramic, the above effect of the ceramic is amplified.

【0007】本発明に用いられるセラミックとしては、
例えば酸化ケイ素、酸化アルミニウム、酸化ジルコニウ
ム、酸化チタン、窒化ケイ素、窒化ホウ素、炭化ケイ素
等の周知のセラミックがあり、これらは二種以上混合さ
れても良い。更に該除菌フィルター(9) の上側に逆止弁
(12)を取付けると、長期間使用しない場合でも出口側か
ら雑菌が侵入して該除菌フィルター(9) 出口側で繁殖す
ることを有効に防除することができ、該浄水器(1) は衛
生的に保たれる。
Ceramics used in the present invention include:
For example, there are known ceramics such as silicon oxide, aluminum oxide, zirconium oxide, titanium oxide, silicon nitride, boron nitride, and silicon carbide, and these may be mixed in two or more kinds. Further, a check valve is provided above the sterilization filter (9).
By installing (12), even if not used for a long period of time, it is possible to effectively prevent invasion of germs from the outlet side and breed at the sterilization filter (9) outlet side, and the water purifier (1) It is kept hygienic.

【0008】[0008]

【実施例】【Example】

[実施例1]図1に本実施例の浄水器(1) を示す。本実
施例の浄水器(1) は基台(2) と該基台(2) 上に取りはず
し可能に設置されている外容器(3) と、該外容器(3) 内
に収納される取外し可能な処理材のカートリッジ(4)
と、該基台(2) の下部には給水口(10)が開口し、該カー
トリッジ(4) 上面には導入口(4A)が設けられており、該
カートリッジ(4) の内部には通水パイプ(11)が貫通し、
該通水パイプ(11)の終端は外容器(3) の外部に差出され
ている。該外容器(3) の内周下部には螺溝(3A)が設けら
れ、該螺溝(3A)の上部にはパッキン(3B)が装着されてい
る。なお該基台(2) の外周上部には螺溝(2A)が設けられ
ており、該外容器(3) の螺溝(3A)を該基台(2) の螺溝(2
A)に螺合することによって、該外容器(3) は該基台(2)
上に取りはずし可能に設置され、また基台(2) から外容
器(3) を外した状態で該カートリッジ(4) の交換が行な
われる。
[Embodiment 1] FIG. 1 shows a water purifier (1) of this embodiment. The water purifier (1) of this embodiment comprises a base (2), an outer container (3) that is removably installed on the base (2), and a removable container that is stored in the outer container (3). Possible Processing Material Cartridge (4)
A water inlet (10) is opened at the bottom of the base (2), an inlet (4A) is provided on the upper surface of the cartridge (4), and the inside of the cartridge (4) is opened. The water pipe (11) penetrates,
The end of the water passage pipe (11) is extended to the outside of the outer container (3). The outer container (3) is provided with a screw groove (3A) at the lower inner periphery thereof, and a packing (3B) is attached to the upper part of the screw groove (3A). A screw groove (2A) is provided on the upper periphery of the base (2), and the screw groove (3A) of the outer container (3) is connected to the screw groove (2A) of the base (2).
The outer container (3) is screwed onto the base (2) by being screwed into (A).
The cartridge (4) is detachably installed on the upper side, and the cartridge (4) is exchanged with the outer container (3) removed from the base (2).

【0009】該処理材のカートリッジ(4) は上側から順
にヤシガラ活性炭を充填したヤシガラ活性炭層(5) 、コ
ーラルサンドを充填したコーラルサンド層(6) 、塩基性
三リン五カルシウムを充填した塩基性三リン五カルシウ
ム層(7) 、セラミック濾過層(8) 並びに通水パイプ(11)
に連絡する除菌フィルター(9) とからなる。該除菌フィ
ルター(9) 内は孔径0.4 μm の中空糸膜(9A)が積層さ
れ、該除菌フィルター(9) の外周下部には導入口(9B)が
設けられ、更に通水パイプ(11)内には逆止弁(12)および
磁石(13)が収納されている。
The treatment material cartridge (4) comprises a coconut husk activated carbon layer (5) filled with coconut husk activated carbon, a coral sand layer (6) filled with coral sand, and a basic triphosphorus pentacalcium filled basic Triphosphorus pentacalcium layer (7), ceramic filtration layer (8) and water pipe (11)
It consists of a sterilization filter (9) to be contacted. A hollow fiber membrane (9A) having a pore size of 0.4 μm is laminated inside the sterilization filter (9), an inlet (9B) is provided at the lower outer periphery of the sterilization filter (9), and a water pipe is further provided. A check valve (12) and a magnet (13) are housed in (11).

【0010】本実施例においては該セラミックとして酸
化アルミニウム・酸化ケイ素1:1重量比混合セラミッ
クとし以下のように活性化処理された。1gの塩化第二
鉄無水物を12Nカセイソーダー水溶液5ml中に入れて
攪拌溶解せしめ5時間以上室温に放置する。該水溶液を
12N塩酸水溶液によってpH約7に中和し、該中和液
を濾紙(No.5C)で濾過した後減圧濃縮すると結晶が
析出する。該結晶を採取してデシケーター中で減圧乾燥
した後、10mlのイソプロパノール−水の80:20重
量比の混合溶媒に溶解せしめ、濾紙(No.5C)によっ
て該溶液を濾過した後減圧濃縮して溶媒を除去し乾燥せ
しめる。上記抽出−濃縮−乾燥の操作は数回繰返され、
精製された活性化鉄塩化物の結晶が得られる。該結晶を
蒸留水に溶解し2ppm 水溶液とする。酸化ケイ素と酸化
アルミニウムの1:1重量比混合粉末にポリビニルアル
コールと水とを添加して混練し、該混練物を所望の形状
に成形した後、1000℃、3時間焼成してセラミック
を作製する。該セラミックを該水溶液に浸漬し2時間放
置した後回収して100℃2時間の乾燥を行ない、活性
化セラミックを得る。
In this example, the ceramic was aluminum oxide / silicon oxide mixed in a 1: 1 weight ratio and was activated as follows. 1 g of ferric chloride anhydrous was put into 5 ml of 12N caustic soda aqueous solution, dissolved by stirring, and left at room temperature for 5 hours or more. The aqueous solution is neutralized to a pH of about 7 with a 12N hydrochloric acid aqueous solution, the neutralized solution is filtered through filter paper (No. 5C) and then concentrated under reduced pressure to precipitate crystals. The crystals were collected, dried under reduced pressure in a desiccator, dissolved in 10 ml of a mixed solvent of 80:20 by weight of isopropanol-water, filtered through a filter paper (No. 5C), and concentrated under reduced pressure to remove the solvent. Remove and dry. The above-mentioned extraction-concentration-drying operation is repeated several times,
Purified activated iron chloride crystals are obtained. The crystals are dissolved in distilled water to make a 2 ppm aqueous solution. Polyvinyl alcohol and water are added to a 1: 1 weight ratio mixed powder of silicon oxide and aluminum oxide, and the mixture is kneaded, and the kneaded product is molded into a desired shape, followed by firing at 1000 ° C. for 3 hours to produce a ceramic. . The ceramic is immersed in the aqueous solution, left standing for 2 hours, then collected and dried at 100 ° C. for 2 hours to obtain an activated ceramic.

【0011】上記構成の浄水器(1) において給水口(10)
より水道水を導入すると図1の矢印の方向に水道水は移
動しカートリッジ(4) の上面の導入口(4A)から該カート
リッジ(4) 内に導入されまずヤシガラ活性炭層(5) 内を
通過して、該水道水の固形物、悪臭、悪味、残留塩素、
有機物等が濾過吸着除去される。このようにして処理さ
れた水道水はコーラルサンド層(6) 内を通過して残存す
る有機物等を吸着除去されるとともに天然ミネラルを供
給されかつpHを調製される。ついで該水道水は塩基性
三リン五カルシウム層(7) 内を通過して更に残存した有
機物等を吸着除去され、またカルシウムイオンを供給さ
れて身体に良いアルカリ性の水に変化させられ、更に天
然ミネラルを供給される。該水道水は塩化第二鉄によっ
て活性化されたセラミック濾過層(8) に達し、該セラミ
ック濾過層(8) によって、更に不純物を濾過されるとと
もに、水のクラスターが細分化され改質される。該活性
化セラミック濾過層(8) によって改質された水道水は除
菌フィルター(9) 内に導入され、長期間の不使用によっ
てカートリッジ(4) 内部に繁殖した微生物によって該水
道水が汚染されている場合でも、該中空糸膜(9A)による
微細濾過によって該微生物が除去される。上記カートリ
ッジ(4) によって濾過除菌された水道水は通水パイプ(1
1)内に導入された磁石(13)によって磁化され、供給口(1
4)から排出される。上記浄水器(1) の不使用時におい
て、通水パイプ(11)から除菌フィルター(9)の出口側へ
微生物を含んだ水が逆流する場合には、該通水パイプ(1
1)内の逆止弁(12)によって該水が除菌フィルター(9) の
出口側まで達することを阻止される。
In the water purifier (1) having the above structure, the water supply port (10)
When more tap water is introduced, the tap water moves in the direction of the arrow in Fig. 1 and is introduced into the cartridge (4) from the inlet (4A) on the upper surface of the cartridge (4) and first passes through the coconut husk activated carbon layer (5). Then, the solid matter of the tap water, odor, bad taste, residual chlorine,
Organic substances and the like are removed by adsorption by filtration. The tap water treated in this way passes through the coral sand layer (6) to adsorb and remove the remaining organic substances and the like, and is supplied with natural minerals and adjusted in pH. Then, the tap water passes through the basic triphosphorus pentacalcium layer (7) to adsorb and remove the remaining organic substances, and is supplied with calcium ions to be changed into alkaline water that is good for the body, and further natural water. Supplied with minerals. The tap water reaches the ceramic filtration layer (8) activated by ferric chloride, and the ceramic filtration layer (8) further filters impurities and subdivides and reforms water clusters. . The tap water modified by the activated ceramic filtration layer (8) is introduced into the sterilization filter (9), and the tap water is contaminated by the microorganisms that have propagated inside the cartridge (4) due to long-term non-use. In this case, the microorganisms are removed by fine filtration through the hollow fiber membrane (9A). The tap water filtered and sterilized by the cartridge (4) is passed through the water pipe (1
It is magnetized by the magnet (13) introduced in (1) and
Emitted from 4). When water containing microorganisms flows backward from the water passage pipe (11) to the outlet side of the sterilization filter (9) when the water purifier (1) is not used, the water passage pipe (1)
The check valve (12) in 1) prevents the water from reaching the outlet side of the sterilization filter (9).

【0012】[実施例2]本実施例の浄水器(1) は実施
例1のセラミック濾過槽(8) に使用するセラミックとし
て下記の活性化セラミックを使用する以外は実施例1と
同様な構成とする。セラミックとして酸化アルミニウム
を処理容器内に収納して該処理容器に実施例1と同様に
調製した水溶液を通した空気を5l/分の流速で3時間
送通して活性化セラミックを得る。
[Embodiment 2] The water purifier (1) of this embodiment has the same structure as that of Embodiment 1 except that the following activated ceramic is used as the ceramic used in the ceramic filtration tank (8) of Embodiment 1. And Aluminum oxide is housed in a processing container as a ceramic, and the aqueous solution prepared in the same manner as in Example 1 is passed through the processing container at a flow rate of 5 l / min for 3 hours to obtain an activated ceramic.

【0013】[実施例3]本実施例の浄水器(1) は実施
例1のセラミック濾過槽(8) に使用するセラミックとし
て下記の活性化セラミックを使用する以外は実施例1と
同様な構成とする。本実施例においてはセラミックとし
てはシリカを使用し以下のように活性化処理をされた。
1gの硫酸第一鉄を12N塩酸水溶液5ml中に入れて攪
拌溶解せしめ、該溶液を濾紙(No.5C)で濾過した後
減圧濃縮すると結晶が析出する。該結晶を採取してデシ
ケーター中で減圧乾燥した後、10mlのイソプロパノー
ル−水の80:20重量比の混合溶媒に溶解せしめ、濾
紙(No.5C)によって該溶液を濾過した後減圧濃縮し
て溶媒を除去し乾燥せしめる。上記抽出−濃縮−乾燥の
操作は数回繰返され、精製された活性化鉄塩化物の結晶
が得られる。該結晶を蒸留水に溶解し2ppm 水溶液とす
る。セラミックを該水溶液に浸漬し2時間放置した後回
収して100℃2時間の乾燥を行ない、活性化セラミッ
クを得る。
[Embodiment 3] The water purifier (1) of this embodiment has the same construction as that of Embodiment 1 except that the following activated ceramic is used as the ceramic used in the ceramic filtration tank (8) of Embodiment 1. And In this example, silica was used as the ceramic and was activated as follows.
1 g of ferrous sulfate was put into 5 ml of 12N hydrochloric acid aqueous solution to dissolve with stirring, and the solution was filtered through filter paper (No. 5C) and then concentrated under reduced pressure to precipitate crystals. The crystals were collected, dried under reduced pressure in a desiccator, dissolved in 10 ml of a mixed solvent of 80:20 by weight of isopropanol-water, filtered through a filter paper (No. 5C), and concentrated under reduced pressure to remove the solvent. Remove and dry. The above extraction-concentration-drying operation is repeated several times to obtain purified activated iron chloride crystals. The crystals are dissolved in distilled water to make a 2 ppm aqueous solution. The ceramic is dipped in the aqueous solution, left standing for 2 hours, then recovered and dried at 100 ° C. for 2 hours to obtain an activated ceramic.

【0014】[実施例4]本実施例の浄水器(1) は実施
例1のセラミック濾過槽(8) に使用するセラミックとし
て下記の活性化セラミックを使用する以外は実施例1と
同様な構成とする。セラミックとして酸化ジリコニウム
を処理容器内に収納して該処理容器に実施例3と同様に
調製した水溶液を通した空気を5l/分の流速で3時間
送通して活性化セラミックを得る。
[Embodiment 4] The water purifier (1) of this embodiment has the same construction as that of Embodiment 1 except that the following activated ceramic is used as the ceramic used in the ceramic filtration tank (8) of Embodiment 1. And As a ceramic, zirconium oxide is housed in a processing container, and air containing an aqueous solution prepared in the same manner as in Example 3 is passed through the processing container at a flow rate of 5 l / min for 3 hours to obtain an activated ceramic.

【0015】本実施例以外、本発明においては無処理の
活性化されていないセラミックをセラミック濾過層とし
て使用しても良い。また除菌フィルター(9) 内の中空糸
膜(9A)の代わりに微細連続気孔を有するプラスチック発
泡体、セラミック多孔体等が用いられても良い。また除
菌フィルター(9) の孔径は濾過、除菌されるべき目的物
の大きさに応じて選択されれば良いが、通常は0.45
μm 以下のものとする。
Other than this embodiment, untreated, non-activated ceramics may be used in the present invention as the ceramic filtration layer. Further, instead of the hollow fiber membrane (9A) in the sterilization filter (9), a plastic foam body having fine continuous pores, a porous ceramic body or the like may be used. The pore size of the sterilization filter (9) may be selected according to the size of the target substance to be filtered and sterilized, but is usually 0.45.
It should be less than μm.

【0016】[0016]

【発明の効果】したがって、本発明においては浄水器を
長期間使用しない場合に浄水器内で微生物が繁殖し、該
微生物によって被処理水が汚染された場合でも、該微生
物は除菌フィルターによって除去される衛生的な浄水器
を提供することができ、更にセラミックによって改質さ
れた水を供給することができる。
Therefore, in the present invention, even when the water purifier is not used for a long period of time, even if the microorganisms propagate in the water purifier and the water to be treated is contaminated by the microorganisms, the microorganisms are removed by the sterilization filter. It is possible to provide a sanitary water purifier, and further supply ceramic-modified water.

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

図1は本発明の実施例1に関するものである。 FIG. 1 relates to Example 1 of the present invention.

【図1】側断面図1] Side sectional view

【符号の説明】 1 浄水器 8 セラミック濾過層 9 除菌フィルター 12 逆止弁[Explanation of symbols] 1 Water purifier 8 Ceramic filtration layer 9 Sterilization filter 12 Check valve

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】セラミック濾過層と除菌フィルターとから
なることを特徴とする浄水器
1. A water purifier comprising a ceramic filter layer and a sterilizing filter.
【請求項2】該セラミック濾過層は塩化第二鉄を大量の
カセイソーダ水溶液に溶かした後塩酸で中和し、濃縮し
て得られた結晶の水溶液に浸漬処理された活性化セラミ
ックからなる請求項1に記載の浄水器
2. The ceramic filter layer is composed of activated ceramics obtained by immersing ferric chloride in a large amount of caustic soda solution, neutralizing with hydrochloric acid, and concentrating the solution to dip it in an aqueous solution of crystals. Water purifier according to 1.
【請求項3】該セラミック濾過層は塩化第二鉄を大量の
カセイソーダ水溶液に溶かした後塩酸で中和し、濃縮し
て得られた結晶の水溶液に通した空気を接触せしめた活
性化セラミックからなる請求項1に記載の浄水器
3. The ceramic filter layer is made from an activated ceramic obtained by dissolving ferric chloride in a large amount of caustic soda aqueous solution, neutralizing it with hydrochloric acid, and concentrating the solution to obtain an aqueous solution of crystals. The water purifier according to claim 1.
【請求項4】該セラミック濾過層は硫酸第一鉄を大量の
塩酸水溶液に溶かした後濃縮して得られた結晶の水溶液
に浸漬処理された活性化セラミックならなる請求項1に
記載の浄水器
4. The water purifier according to claim 1, wherein the ceramic filter layer is made of an activated ceramic that is immersed in an aqueous solution of crystals obtained by dissolving ferrous sulfate in a large amount of hydrochloric acid aqueous solution and then concentrating the solution.
【請求項5】該セラミック濾過層は硫酸第一鉄を大量の
塩酸水溶液に溶かした後濃縮して得られた結晶の水溶液
に通した空気を接触せしめた活性化セラミックからなる
請求項1に記載の浄水器
5. The ceramic filter layer comprises an activated ceramic obtained by contacting air passing through an aqueous solution of crystals obtained by dissolving ferrous sulfate in a large amount of hydrochloric acid aqueous solution and then concentrating the solution. Water purifier
【請求項6】該除菌フィルタ−の出口側には逆止弁が取
付けられている請求項1に記載の浄水器
6. The water purifier according to claim 1, wherein a check valve is attached to the outlet side of the sterilization filter.
JP2193494A 1994-01-21 1994-01-21 Water purifier Pending JPH07204635A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2193494A JPH07204635A (en) 1994-01-21 1994-01-21 Water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2193494A JPH07204635A (en) 1994-01-21 1994-01-21 Water purifier

Publications (1)

Publication Number Publication Date
JPH07204635A true JPH07204635A (en) 1995-08-08

Family

ID=12068885

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2193494A Pending JPH07204635A (en) 1994-01-21 1994-01-21 Water purifier

Country Status (1)

Country Link
JP (1) JPH07204635A (en)

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EP1031539A1 (en) * 1999-02-24 2000-08-30 Kil Ho Kim Water purifier
JP2009504399A (en) * 2005-08-22 2009-02-05 シーメンス・ウォーター・テクノロジーズ・コーポレーション Assembly for water filtration using a tubular manifold to minimize backwash
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US9022224B2 (en) 2010-09-24 2015-05-05 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
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US9533261B2 (en) 2012-06-28 2017-01-03 Evoqua Water Technologies Llc Potting method
US9604166B2 (en) 2011-09-30 2017-03-28 Evoqua Water Technologies Llc Manifold arrangement
US9675938B2 (en) 2005-04-29 2017-06-13 Evoqua Water Technologies Llc Chemical clean for membrane filter
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US9764288B2 (en) 2007-04-04 2017-09-19 Evoqua Water Technologies Llc Membrane module protection
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Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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US9675938B2 (en) 2005-04-29 2017-06-13 Evoqua Water Technologies Llc Chemical clean for membrane filter
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
US8894858B1 (en) 2005-08-22 2014-11-25 Evoqua Water Technologies Llc Method and assembly for water filtration using a tube manifold to minimize backwash
JP2009504399A (en) * 2005-08-22 2009-02-05 シーメンス・ウォーター・テクノロジーズ・コーポレーション Assembly for water filtration using a tubular manifold to minimize backwash
US9764288B2 (en) 2007-04-04 2017-09-19 Evoqua Water Technologies Llc Membrane module protection
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
US9206057B2 (en) 2007-05-29 2015-12-08 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US10507431B2 (en) 2007-05-29 2019-12-17 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US9573824B2 (en) 2007-05-29 2017-02-21 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US10441920B2 (en) 2010-04-30 2019-10-15 Evoqua Water Technologies Llc Fluid flow distribution device
US9914097B2 (en) 2010-04-30 2018-03-13 Evoqua Water Technologies Llc Fluid flow distribution device
US9022224B2 (en) 2010-09-24 2015-05-05 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9630147B2 (en) 2010-09-24 2017-04-25 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9604166B2 (en) 2011-09-30 2017-03-28 Evoqua Water Technologies Llc Manifold arrangement
US9925499B2 (en) 2011-09-30 2018-03-27 Evoqua Water Technologies Llc Isolation valve with seal for end cap of a filtration system
US10391432B2 (en) 2011-09-30 2019-08-27 Evoqua Water Technologies Llc Manifold arrangement
US11065569B2 (en) 2011-09-30 2021-07-20 Rohm And Haas Electronic Materials Singapore Pte. Ltd. Manifold arrangement
US9533261B2 (en) 2012-06-28 2017-01-03 Evoqua Water Technologies Llc Potting method
US9764289B2 (en) 2012-09-26 2017-09-19 Evoqua Water Technologies Llc Membrane securement device
US9962865B2 (en) 2012-09-26 2018-05-08 Evoqua Water Technologies Llc Membrane potting methods
US9815027B2 (en) 2012-09-27 2017-11-14 Evoqua Water Technologies Llc Gas scouring apparatus for immersed membranes
US11173453B2 (en) 2013-10-02 2021-11-16 Rohm And Haas Electronic Materials Singapores Method and device for repairing a membrane filtration module
US10322375B2 (en) 2015-07-14 2019-06-18 Evoqua Water Technologies Llc Aeration device for filtration system
CN105565445A (en) * 2016-01-11 2016-05-11 孙茂友 Cell energy water manufacturing device

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