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JP3293705B2 - Water purifier - Google Patents

Water purifier

Info

Publication number
JP3293705B2
JP3293705B2 JP32885393A JP32885393A JP3293705B2 JP 3293705 B2 JP3293705 B2 JP 3293705B2 JP 32885393 A JP32885393 A JP 32885393A JP 32885393 A JP32885393 A JP 32885393A JP 3293705 B2 JP3293705 B2 JP 3293705B2
Authority
JP
Japan
Prior art keywords
water
activated carbon
exchange resin
hollow fiber
water purifier
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP32885393A
Other languages
Japanese (ja)
Other versions
JPH07178390A (en
Inventor
謙治 亘
正直 小泓
幸男 小林
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
Mitsubishi Rayon Co 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 Mitsubishi Chemical Corp, Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Chemical Corp
Priority to JP32885393A priority Critical patent/JP3293705B2/en
Publication of JPH07178390A publication Critical patent/JPH07178390A/en
Application granted granted Critical
Publication of JP3293705B2 publication Critical patent/JP3293705B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)
  • Water Treatment By Sorption (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は安全でおいしい水を得る
ための浄水器に関し、特に、吸着剤を限定することによ
り、安全性やおいしさを損なう原因となる化合物を除去
できる浄水器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purifier for obtaining safe and tasty water, and more particularly to a water purifier capable of removing a compound which impairs safety and taste by limiting an adsorbent.

【0002】[0002]

【従来の技術】水道水中に含まれる残留塩素を除くこと
を主目的とした活性炭浄水器が数年前に発売され使用さ
れて来たが、厚生省の調査により、長時間使用しなかっ
た場合に活性炭に雑菌が発生し、好ましくないことが明
かとなった。
2. Description of the Related Art Activated carbon water purifiers mainly intended to remove residual chlorine contained in tap water have been launched and used several years ago. Bacteria appeared on the activated carbon, which proved undesirable.

【0003】この雑菌の流出を抑えるために多孔質中空
糸膜等の膜濾過を利用した浄水器が発売され、最近では
このタイプが主流となっている。最近、活性炭収納ユニ
ット、分離濾過膜収納ユニットに更にイオン交換樹脂収
納ユニットを組み合わせたカセット式浄水器が提案され
ている(実開平3−7989号公報)。まだ数量的に多
くはないが、逆浸透膜を用いた浄水器や天然石、セラミ
ックス等を濾材として使用した浄水器も上市されてい
る。
[0003] Water purifiers using membrane filtration such as a porous hollow fiber membrane have been put on the market to suppress the outflow of the germs, and this type has recently become the mainstream. Recently, a cassette type water purifier in which an activated carbon storage unit, a separation filtration membrane storage unit, and an ion exchange resin storage unit are further combined has been proposed (Japanese Utility Model Laid-Open No. 3-7989). Although not quantitatively large, water purifiers using reverse osmosis membranes and water purifiers using natural stones, ceramics, etc. as filter media are also on the market.

【0004】[0004]

【発明が解決しようとする課題】上記のような浄水器に
おいて、多孔質中空糸膜等の膜濾過を行っていないもの
は、長時間使用しないと雑菌が繁殖し水道水の初流に流
出してしまうという問題点があった。このような問題点
を解決すべく、多孔質中空糸膜や平膜による精密濾過を
行う浄水器や活性炭に銀を添着する等の方法により抗菌
性を持たせた浄水器が開発され、上市されるようになっ
てきた。
In the above-mentioned water purifiers, those which have not been subjected to membrane filtration, such as porous hollow fiber membranes, are liable to grow germs and flow out to the initial flow of tap water unless used for a long time. There was a problem that would. In order to solve such problems, a water purifier that performs microfiltration using a porous hollow fiber membrane or a flat membrane or a water purifier that has antibacterial properties by, for example, impregnating activated carbon with silver has been developed and put on the market. It has become.

【0005】活性炭に銀を添着したものは、溶出する銀
の量によって抗菌性が異なり、また銀が多量に流出して
も良くないので、性能的に若干不安定である。膜濾過に
よる方法は膜の使用法、固定法等に間違いがなければ雑
菌等を除去するのは充分な性能を有している。活性炭を
使用していれば、その使用量、性能にもよるがトリハロ
メタン、農薬等の微量溶解している危険性のある有機物
を除去することは可能である。
[0005] Activated carbon impregnated with silver is slightly unstable in performance because its antibacterial properties vary depending on the amount of silver eluted and a large amount of silver may not flow out. The method using membrane filtration has sufficient performance to remove various germs and the like if there is no mistake in the method of using and fixing the membrane. If activated carbon is used, it is possible to remove trace amounts of potentially hazardous dissolved organic substances such as trihalomethane and pesticides, depending on the amount and performance of the activated carbon.

【0006】然乍、配管材料などから溶出する鉛等の重
金属の陽イオンや硝酸性窒素及び亜硝酸性窒素等の陰イ
オンで溶解性のものは活性炭、膜濾過によって取り除く
ことは難しく、ほとんど除去できていないのが現状であ
った。これらのイオンを取り除くために、逆浸透膜を用
いた浄水器も開発されているが、飲用水のおいしさとい
う点でミネラル分全てを取り除いてしまうので、水が不
味くなり、安全でおいしい水という面では難点があっ
た。
However, cations of heavy metals such as lead and anions such as nitrate nitrogen and nitrite nitrogen, which are soluble in piping materials and the like, and which are soluble, are difficult to remove by activated carbon and membrane filtration, and are almost removed. It was not possible at present. In order to remove these ions, a water purifier using a reverse osmosis membrane has been developed.However, it removes all minerals in terms of the taste of drinking water, so the water becomes unpalatable and is called safe and delicious water. In terms of face, there were difficulties.

【0007】そこで、上記のような溶解性のイオン等を
選択的に除去するという目的で、活性炭、多孔質中空糸
膜に加えて、イオン交換樹脂が浄水槽に組み込まれた浄
水器が提案されている。この浄水器は、原水中に溶解し
ているイオン性物質を取り除くことにおいて優れてい
る。然乍、イオン交換樹脂それ自体は不溶解性であって
も、その製造過程においての不純物や未反応物が樹脂表
面に残っている場合があり、それらが溶出した場合には
精密濾過膜では除去できず濾過水に混入してしまう恐れ
がある。
Therefore, for the purpose of selectively removing the soluble ions and the like as described above, a water purifier has been proposed in which an ion exchange resin is incorporated in a water purification tank in addition to activated carbon and a porous hollow fiber membrane. ing. This water purifier is excellent in removing ionic substances dissolved in raw water. However, even if the ion exchange resin itself is insoluble, impurities and unreacted substances in the production process may remain on the resin surface, and when they elute, they are removed by the microfiltration membrane. It may not be possible to mix in filtered water.

【0008】本発明は、この様な状況を鑑み、安全でお
いしい水を得るために残留塩素、雑菌だけでなく、溶解
している重金属イオン等をも除去できる浄水器を提供す
ることを目的とする。
The present invention has been made in view of the above circumstances, and has as its object to provide a water purifier capable of removing not only residual chlorine and various bacteria but also dissolved heavy metal ions in order to obtain safe and delicious water. I do.

【0009】[0009]

【課題を解決するための手段】本発明の要旨は、浄化槽
がヒドロキシアパタイト、陰イオン交換樹脂、活性炭及
び多孔質中空糸膜で構成されることを特徴とする浄水器
にある。
SUMMARY OF THE INVENTION The gist of the present invention is to provide a septic tank.
Is hydroxyapatite, anion exchange resin, activated carbon
Water purifier characterized by comprising a porous hollow fiber membrane
It is in.

【0010】前記陰イオン交換樹脂が強塩基型陰イオン
交換樹脂であると好ましい。また、前記陰イオン交換樹
脂の前後に活性炭を配設することが好ましい。
The anion exchange resin is a strong base type anion.
It is preferably an exchange resin. In addition, the anion exchange tree
It is preferable to arrange activated carbon before and after the fat.

【0011】本発明は浄化槽がヒドロキシアパタイト
陰イオン交換樹脂、活性炭及び多孔質中空糸膜から構成
される。
According to the present invention, the septic tank is hydroxyapatite ,
Consists of anion exchange resin, activated carbon and porous hollow fiber membrane
Is done.

【0012】ヒドロキシアパタイトや活性炭のみでは、
雑菌の発生があった場合に浄水器からの初流に雑菌が流
出してしまい安全面からみて好ましくない。また、活性
炭と中空糸膜のみでは、鉛等の重金属の陽イオンや硝酸
性窒素及び亜硝酸性窒素等の陰イオンで溶解性のものは
取り除くことが難しいという問題点がある。
With hydroxyapatite or activated carbon alone,
When various bacteria are generated, the bacteria may flow out into the initial flow from the water purifier, which is not preferable from the viewpoint of safety. In addition, there is a problem that it is difficult to remove soluble cations of heavy metals such as lead and anions such as nitrate nitrogen and nitrite nitrogen only with activated carbon and hollow fiber membranes.

【0013】本発明の浄水器においてヒドロキシアパタ
イト、陰イオン交換樹脂、活性炭、多孔質中空糸膜のう
ち、多孔質中空糸膜は浄水槽の最終段に存在しているこ
とが望ましい。ヒドロキシアパタイト、陰イオン交換樹
脂、活性炭については、どのような順序になっても、或
は、三者の混合、いずれか二者の混合をして用いても差
し支えない。
In the water purifier of the present invention, among hydroxyapatite, anion exchange resin, activated carbon and porous hollow fiber membrane, the porous hollow fiber membrane is desirably present in the last stage of the water purification tank. The hydroxyapatite, anion exchange resin, and activated carbon may be used in any order, or a mixture of three or a mixture of any two may be used.

【0014】然乍、陰イオン交換樹脂を用いると、残留
塩素として存在する次亜塩素酸イオンが吸着され、陰イ
オン交換樹脂の交換容量を減少する恐れがあるので、
イオン交換樹脂の前に活性炭を配設し、陰イオン交換樹
脂の後に、樹脂からの溶出物を吸着除去する目的で再び
活性炭を配設する方法が好ましい。
[0014] Shika乍, the use of anion exchange resins, hypochlorite ions present as residual chlorine is adsorbed, there is a possibility to reduce the exchange capacity of the anion exchange resin, anion
Activated carbon is installed in front of the ion exchange resin,
After the fat, again to adsorb and remove the eluate from the resin
A method of disposing activated carbon is preferred.

【0015】本発明で用いるイオン交換樹脂は、除去し
たい物質に対応するものであれば、弱塩基性イオン交換
樹脂、強塩基性イオン交換樹脂のいずれも用いることが
できる。
As the ion exchange resin used in the present invention, any of a weakly basic ion exchange resin and a strongly basic ion exchange resin can be used as long as they correspond to the substance to be removed.

【0016】配水管に用いられている鉛管から溶出し、
有害物質として含まれる可能性が高い鉛等の重金属を除
去する目的で、陽イオン交換樹脂、特に強酸性陽イオン
交換樹脂を用いた浄水器には、次のような理由からカル
シウム塩型の強酸性陽イオン交換樹脂が用いられてい
る。
Elution from a lead pipe used for a water distribution pipe,
For the purpose of removing heavy metals such as lead, which are highly likely to be contained as harmful substances, cation exchange resins, especially water purifiers using strongly acidic cation exchange resins, are used for the following reasons. A cationic cation exchange resin is used.

【0017】強酸性陽イオン交換樹脂は一般にナトリウ
ム塩として販売されているが、イオン交換によりナトリ
ウムが流出し、飲用に供すると血圧の上昇等の問題が発
生することがあるのであまり好ましくない。
[0017] Strongly acidic cation exchange resins are generally sold as sodium salts, but are not preferred because sodium exchange is caused by ion exchange, and when used for drinking, problems such as an increase in blood pressure may occur.

【0018】また、ナトリウムを流出させないために酸
型の強酸性陽イオン交換樹脂を用いると流出液のpHが
4以下になってしまうので、水道水質基準から外れ、刺
激も強くなるのであまり好ましくない。更に、溶出イオ
ンが水のおいさしを向上し、健康面でも不足しがちであ
るということよりカルシウム塩型とすることが好まし
い。
Further, if an acid-type strongly acidic cation exchange resin is used to prevent sodium from flowing out, the pH of the effluent becomes 4 or less, which deviates from the tap water quality standard and increases irritation. . Furthermore, it is preferable to use a calcium salt type because eluting ions improve the taste of water and tend to be insufficient in health.

【0019】一方、ヒドロキシアパタイトはカルシウム
のリン酸塩であり、アパタイト構造を有する。鉛等2価
の重金属を選択的にイオン交換でき、その時、交換イオ
ンとして結晶中の格子イオンであるカルシウムイオンが
放出される。従って、カルシウム塩型の強酸性陽イオン
交換樹脂と同様のイオン交換を行う。
On the other hand, hydroxyapatite is a phosphate of calcium and has an apatite structure. Divalent heavy metals such as lead can be selectively ion-exchanged, at which time calcium ions, which are lattice ions in the crystal, are released as exchange ions. Therefore, ion exchange similar to that of the calcium salt type strongly acidic cation exchange resin is performed.

【0020】ヒドロキシアパタイトの場合は、2価の重
金属特に鉛に対して選択性に優れ、交換効率並びに交換
容量共に市販の強酸性陽イオン交換樹脂よりも優れてい
る。また、陰イオンの交換もヒドロキシアパタイトは行
うが、硝酸イオン等の場合はイオン交換によってアパタ
イト構造が破壊されるので、濃度が高い場合別の除去剤
例えば陰イオン交換樹脂等による除去が好ましい。
In the case of hydroxyapatite, it has excellent selectivity for divalent heavy metals, especially lead, and is superior in both exchange efficiency and exchange capacity to commercially available strong acidic cation exchange resins. In addition, hydroxyapatite is also used for anion exchange. However, in the case of nitrate ion or the like, the apatite structure is destroyed by ion exchange. Therefore, when the concentration is high, removal with another removing agent such as an anion exchange resin is preferable.

【0021】また、実際の水道水中の硝酸イオンの濃度
は、ヒドロキシアパタイトの陽イオン交換特性を阻害す
るほどのことはないので、この点に付いては問題がな
い。また、溶出という問題に対しても、ヒドロキシアパ
タイトはクロマトグラフィーの充填剤として用いられて
いるように、水への溶解度は極めて小さく、また、溶出
があるとしても微量のカルシウム塩であり、安全面では
問題がない。更に、有機物に対する吸着特性も良好であ
り、活性炭の役割を補う、或はその代わりを果たすこと
も可能である。
Further, since the actual concentration of nitrate ions in tap water is not so large as to impair the cation exchange properties of hydroxyapatite, there is no problem in this respect. To solve the problem of elution, hydroxyapatite, as used as a packing material for chromatography, has extremely low solubility in water. There is no problem. Furthermore, it has good adsorption characteristics for organic substances, and can supplement or substitute for the role of activated carbon.

【0022】水質基準を超える水道水の例は、平成2年
度水道統計によると全データの最高値を見ても4820
浄水場中7浄水場と数少ないが、硝酸性窒素及び亜硝酸
性窒素を含んでいることがある。また、井戸水において
は更に多くの井戸に硝酸性窒素及び亜硝酸性窒素が含ま
れている場合があり、これを除くことも重要な課題とな
る。
In the case of tap water exceeding the water quality standard, the highest value of all data is 4820 according to the 1990 statistics.
There are only a few of the seven water treatment plants, but may contain nitrate nitrogen and nitrite nitrogen. In addition, in well water, nitrate nitrogen and nitrite nitrogen may be contained in more wells in some cases, and removal of such nitrate nitrogen is also an important issue.

【0023】このような場合には、中性塩分解能力のあ
る強塩基性陰イオン交換樹脂を用いることが好ましい。
強塩基性陰イオン交換樹脂は一般に塩化物型が市販され
ており、これをそのまま用いれば硝酸性窒素及び亜硝酸
性窒素を除去できる。水酸化物型とした場合は、流出す
る水のpHが高くなりあまり好ましくない。
In such a case, it is preferable to use a strongly basic anion exchange resin having a neutral salt decomposing ability.
In general, a strong basic anion exchange resin is commercially available in a chloride form, and if used as it is, nitrate nitrogen and nitrite nitrogen can be removed. In the case of the hydroxide type, the pH of the water flowing out becomes high, which is not preferable.

【0024】本発明では多孔質中空糸膜を用いなければ
ならない。多孔質平膜を用いた場合は充分な濾過膜面積
を得られない場合があるので好ましくない。本発明の多
孔質中空糸膜は雑菌等の微小物質が除去できれば特に限
定されるものではなく、ポリエチレン、ポリプロピレン
等のポリオレフィン系、ポリスルフォン系等の多孔質中
空糸膜が用いられる。これらの多孔質中空糸膜は、通水
性能を向上するために親水化されていることが好まし
い。
In the present invention, a porous hollow fiber membrane must be used. Use of a porous flat membrane is not preferable because a sufficient filtration membrane area may not be obtained. The porous hollow fiber membrane of the present invention is not particularly limited as long as minute substances such as various bacteria can be removed, and a porous hollow fiber membrane of a polyolefin type such as polyethylene or polypropylene or a polysulfone type is used. It is preferable that these porous hollow fiber membranes are hydrophilized in order to improve water passage performance.

【0025】本発明で使用する活性炭は、残留塩素を還
元する能力、トリハロメタンや農薬等の有害物を吸着す
る能力を持っていれば特に限定されるものではなく、形
態的には粉末状、粒状、繊維状、成形炭等の活性炭が使
用できる。原料的にも特に限定されるものではなくヤシ
ガラ活性炭、骨炭、木炭系のもの等の天然物系活性炭、
ピッチ系、石油コークス系等の合成活性炭等が使用でき
る。賦活方法についても特に限定されず、水蒸気賦活、
化学的賦活等の賦活法が用いられる。
The activated carbon used in the present invention is not particularly limited as long as it has the ability to reduce residual chlorine and the ability to adsorb harmful substances such as trihalomethane and pesticides. Activated carbon, such as fibrous or molded charcoal, can be used. The raw material is not particularly limited, and natural activated carbon such as coconut shell activated carbon, bone charcoal, and charcoal-based,
Pitch-based, petroleum-coke-based synthetic activated carbon and the like can be used. There is no particular limitation on the activation method, and steam activation,
An activation method such as chemical activation is used.

【0026】浄水器として用いた場合に、通水する水の
活性炭内の通過速度が通常の活性炭の使用法に比べて非
常に大きいので嵩密度の大きいものが好ましく、水道水
圧との関連から圧力損失は小さいものが好ましい。吸着
物質は比較的分子量の小さいものが多く、コスト面を含
めると水蒸気賦活した粒状ヤシガラ活性炭が現状では最
も好ましい。
When used as a water purifier, it is preferable that the bulk water has a large bulk density since the passing speed of the water to be passed through the activated carbon is much higher than that of a normal method of using activated carbon. Preferably, the loss is small. Most of the adsorbed substances have relatively small molecular weights, and in view of cost, granular activated palm carbon activated with steam is currently most preferable.

【0027】本発明の活性炭は抗菌性を付与するために
銀等の重金属を添着したものでも構わないが、余り大量
の重金属が溶出するものは好ましくない。抗菌性を付与
したものは比較的好ましく用いられる。本発明のヒドロ
キシアパタイト、活性炭、陰イオン交換樹脂及び多孔質
中空糸膜は一つの容器内に収められていても、複数個の
容器に収められこれらを組み合わせた形のものでも構わ
ない。また、上記の組み合わせに更に一次フィルターや
セラミックス、天然石等を併用しても構わない。
The activated carbon of the present invention may be one to which a heavy metal such as silver is impregnated for imparting antibacterial properties, but it is not preferable that a large amount of heavy metal is eluted. Those provided with antibacterial properties are relatively preferably used. The hydroxyapatite, activated carbon, anion exchange resin and porous hollow fiber membrane of the present invention may be housed in one container or may be housed in a plurality of containers and combined. Further, a primary filter, ceramics, natural stone, or the like may be used in combination with the above combination.

【0028】[0028]

【発明の効果】本発明は上記のようにヒドロキシアパタAs described above, the present invention provides a hydroxyapat
イト、活性炭、陰イオン交換樹脂、多孔質中空糸膜といSite, activated carbon, anion exchange resin, porous hollow fiber membrane
う構成の新規な浄水器により、これまで除去の困難であNew water purifiers that have been difficult to remove.
った溶解イオン性有害物質をも除去できる画期的な浄水Innovative water purification that can remove even dissolved ionic harmful substances
器である。It is a vessel.

【0029】[0029]

【0030】[0030]

【0031】[0031]

【0032】[0032]

【0033】[0033]

【0034】[0034]

【0035】[0035]

【0036】[0036]

【0037】[0037]

【0038】[0038]

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平4−122493(JP,A) 特開 平6−114371(JP,A) 特開 平5−200282(JP,A) 実開 平6−77881(JP,U) 実開 平5−76593(JP,U) 実開 平5−80584(JP,U) (58)調査した分野(Int.Cl.7,DB名) C02F 1/28 C02F 1/42 C02F 1/44 B01D 35/04 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-4-122493 (JP, A) JP-A-6-114371 (JP, A) JP-A-5-200282 (JP, A) 77881 (JP, U) Japanese Utility Model Hei 5-76593 (JP, U) Japanese Utility Model Utility Model 5-80584 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) C02F 1/28 C02F 1 / 42 C02F 1/44 B01D 35/04

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 浄化槽がヒドロキシアパタイト、陰イオ
ン交換樹脂、活性炭及び多孔質中空糸膜で構成されるこ
とを特徴とする浄水器。
1. A septic tank comprising hydroxyapatite, an anion
Consisting of an exchange resin, activated carbon and a porous hollow fiber membrane.
And a water purifier characterized by the following.
【請求項2】 前記陰イオン交換樹脂が強塩基性陰イオ
ン交換樹脂であることを特徴とする請求項1記載の浄水
器。
2. The method according to claim 1, wherein said anion exchange resin is a strongly basic anion.
2. Water purification according to claim 1, wherein the water is an exchange resin.
vessel.
【請求項3】 前記陰イオン交換樹脂の前後に活性炭が
配設されてなることを特徴とする請求項2記載の浄水
器。
3. An activated carbon before and after the anion exchange resin.
3. Water purification according to claim 2, wherein the water purification is provided.
vessel.
JP32885393A 1993-12-24 1993-12-24 Water purifier Expired - Lifetime JP3293705B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32885393A JP3293705B2 (en) 1993-12-24 1993-12-24 Water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32885393A JP3293705B2 (en) 1993-12-24 1993-12-24 Water purifier

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2002015697A Division JP2002263639A (en) 2002-01-24 2002-01-24 Water purifier

Publications (2)

Publication Number Publication Date
JPH07178390A JPH07178390A (en) 1995-07-18
JP3293705B2 true JP3293705B2 (en) 2002-06-17

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP32885393A Expired - Lifetime JP3293705B2 (en) 1993-12-24 1993-12-24 Water purifier

Country Status (1)

Country Link
JP (1) JP3293705B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0720968A4 (en) * 1994-07-25 1997-10-01 Toto Ltd Water cleaner
JP4698792B2 (en) * 2000-03-17 2011-06-08 日本メナード化粧品株式会社 Method for removing heavy metals from mushroom extract
CN107324544B (en) * 2017-08-18 2020-08-18 浙江海盐力源环保科技股份有限公司 A filter equipment for handling industry heavy metal sewage

Also Published As

Publication number Publication date
JPH07178390A (en) 1995-07-18

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