JPH0133191Y2 - - Google Patents
Info
- Publication number
- JPH0133191Y2 JPH0133191Y2 JP14352183U JP14352183U JPH0133191Y2 JP H0133191 Y2 JPH0133191 Y2 JP H0133191Y2 JP 14352183 U JP14352183 U JP 14352183U JP 14352183 U JP14352183 U JP 14352183U JP H0133191 Y2 JPH0133191 Y2 JP H0133191Y2
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- purifier
- container
- water
- membrane
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 84
- 239000012528 membrane Substances 0.000 claims description 68
- 239000012510 hollow fiber Substances 0.000 claims description 67
- 230000002209 hydrophobic effect Effects 0.000 claims description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 28
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 13
- 239000003456 ion exchange resin Substances 0.000 claims description 13
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 4
- 238000004382 potting Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 2
- 239000008213 purified water Substances 0.000 description 12
- 241000894006 Bacteria Species 0.000 description 11
- 239000007788 liquid Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 11
- 238000001914 filtration Methods 0.000 description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 239000008399 tap water Substances 0.000 description 5
- 235000020679 tap water Nutrition 0.000 description 5
- 239000012535 impurity Substances 0.000 description 4
- 235000019645 odor Nutrition 0.000 description 4
- 230000000844 anti-bacterial effect Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 235000020188 drinking water Nutrition 0.000 description 3
- 239000003651 drinking water Substances 0.000 description 3
- 229920000098 polyolefin Polymers 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 235000019640 taste Nutrition 0.000 description 3
- 239000000084 colloidal system Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000003780 insertion Methods 0.000 description 2
- 230000037431 insertion Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical class OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 238000011045 prefiltration Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002510 pyrogen Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 208000035473 Communicable disease Diseases 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 241000293871 Salmonella enterica subsp. enterica serovar Typhi Species 0.000 description 1
- 241000607768 Shigella Species 0.000 description 1
- 229910021607 Silver chloride Inorganic materials 0.000 description 1
- 241000607626 Vibrio cholerae Species 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 230000036772 blood pressure Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000000741 diarrhetic effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000013013 elastic material Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 239000008233 hard water Substances 0.000 description 1
- 229920001477 hydrophilic polymer Polymers 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 229940118696 vibrio cholerae Drugs 0.000 description 1
- 235000015041 whisky Nutrition 0.000 description 1
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Description
【考案の詳細な説明】
本考案は細菌等の混入している虞のある水、コ
ロイド等汚濁物を含有する水もしくは永水を簡便
に精密濾過できる高性能、小型で携帯にも便利な
簡易型浄水器に関する。[Detailed description of the invention] This invention is a high-performance, compact, and easy-to-carry device that can easily perform precision filtration of water that may be contaminated with bacteria, water that contains pollutants such as colloids, or permanent water. Regarding type water purifiers.
従来から水道水の水質低下が指摘されており、
とくに海外旅行先や被災地での飲料水の確保は深
刻な課題である。海外旅行の経験者であれば飲料
水により誰でも一度ならず下痢症状に悩まされて
いるが、その原因の多くは細菌その他の微生物因
と水の硬度等不純物因とに大別される。とくに前
者の場合は病原性大腸菌のみならず赤痢菌、コレ
ラ菌、チフス菌といつた伝染病にも感染する危険
性があり、それも容器や取扱い上での汚染のため
煮沸水でも安心できないし、さらに氷にいたつて
は細菌汚染の確率が極めて高い。 It has long been pointed out that the quality of tap water has deteriorated.
Securing drinking water is a particularly serious issue in overseas travel destinations and disaster-stricken areas. Anyone who has traveled overseas has suffered from diarrheal symptoms more than once due to drinking water, and the causes can be broadly divided into bacteria and other microbial causes, and impurities such as water hardness. In the case of the former in particular, there is a risk of infection not only by pathogenic Escherichia coli but also by infectious diseases such as Shigella, Vibrio cholerae, and Salmonella typhi, and boiled water is not safe because of contamination in the container or handling. Moreover, when it comes to ice, there is an extremely high probability of bacterial contamination.
さらに近年水道水等にフタル酸エステル等の有
機物が含まれていたり、Ca,Mg等各種イオンが
含まれていたりしている。 Furthermore, in recent years, tap water has been found to contain organic substances such as phthalate esters and various ions such as Ca and Mg.
したがつて飲料水からの菌の除去、さらに好ま
しくは溶解不純物の除去に関する要請は国内にお
いても高く、まして海外旅行者、海外出張者等に
おいては海外における健康維持のため特に要請さ
れているものである。 Therefore, there is a high demand for the removal of bacteria from drinking water, and more preferably for the removal of dissolved impurities, even in Japan, and there is a particular need for overseas travelers and business travelers to maintain their health overseas. be.
従来より浄水器として活性炭を用いた装置を水
道蛇口に直結して水道水中の不純物、不快臭原因
物質等を吸着除去するもの、イオン交換樹脂充填
塔を用いて硬水を軟水化する水浄化装置、あるい
は逆浸透法等で水を浄化する純水製造装置等が知
られているが、活性炭を用いたものは水道水中の
殺菌成分である塩素を吸着して殺菌効果を失ない
浄化器中でむしろ細菌等が増殖し、その菌が浄化
された筈の水に混入するという欠点を有してい
る。 Conventional water purifiers that use activated carbon are connected directly to a tap to adsorb and remove impurities and substances that cause unpleasant odors in tap water; water purifiers that soften hard water using ion-exchange resin-packed towers; Alternatively, there are known pure water production devices that purify water using reverse osmosis, etc., but those that use activated carbon absorb chlorine, a bactericidal component in tap water, and are used in purifiers that do not lose their bactericidal effect. This method has the disadvantage that bacteria and the like proliferate and contaminate the water that is supposed to be purified.
イオン交換樹脂は水中のイオンを除去するのみ
で菌や非イオン性不純物は除去できず、上記と同
様浄化装置内での菌等が増殖する虞もある。 Ion exchange resins only remove ions from water, but cannot remove bacteria and nonionic impurities, and as mentioned above, there is a risk that bacteria and the like will proliferate within the purification device.
さらに活性炭浄化器、イオン交換樹脂充填塔で
水を浄化するには水道水圧又はポンプ等を必要と
し、どこでも浄化された水を得ることができるも
のでもない。まして逆侵透法は大型の装置や高圧
発生手段を要し簡便に浄化水を得られるものでは
ない。 Furthermore, purifying water with an activated carbon purifier or an ion exchange resin packed tower requires tap water pressure or a pump, and purified water cannot be obtained anywhere. Furthermore, the reverse osmosis method requires large equipment and high pressure generating means, and purified water cannot be easily obtained.
この様な状況から本考案者等はさきに簡易型浄
水器として蛇腹構造を有する押圧容器とその出口
に連結された精密濾過機の組合せを提案した(実
願昭58−113582号)。しかしこれは一度にコツプ
一、二杯程度の浄化水を得るには適しているが、
一度にこれより多くの水を得られる様容量を大き
くしようとすると、例えばプラスチツク製等の通
常の蛇腹式押圧器を用いて該押圧器に水を入れる
とその水圧で押圧器が変形して、好ましい容量の
場合は充分に機能し得ないことが見出された。 Under these circumstances, the inventors of the present invention previously proposed a combination of a pressurized container having a bellows structure and a precision filter connected to its outlet as a simple water purifier (Utility Application No. 113582/1982). However, although this is suitable for obtaining one or two cups of purified water at a time,
If you try to increase the capacity so that you can obtain more water at once, for example, if you use a normal bellows-type presser made of plastic or the like and fill the presser with water, the presser will deform due to the water pressure. It has been found that the preferred capacity does not work satisfactorily.
さらに従来から提案されている種々の簡易型浄
水器は、地震その他災害等の非常時に細菌等の繁
殖している湖、沼、池や河川の水を浄化する等の
目的を有する装置であるにもかかわらず、容器に
水を入れる際に容器の口から河川水がこぼれて清
浄であるべき浄化水取出口を汚染する危険が何ら
考慮されていないのが現状である。 Furthermore, the various simple water purifiers that have been proposed in the past are devices that have the purpose of purifying water in lakes, swamps, ponds, and rivers where bacteria are breeding during emergencies such as earthquakes and other disasters. However, the current situation is that no consideration is given to the risk of river water spilling from the mouth of the container and contaminating the purified water outlet, which should be clean, when filling the container with water.
さらに多孔質中空糸膜を用いた従来の浄水器モ
ジユールは親水性の膜のみで形成されており、気
体が混入すると通常の圧力例えば1Kg/cm2程度の
圧力では混入した気体は容易には通過せず、膜面
に気体がたまり、たまつた気体により、水の透過
が邪魔され、膜の全体としての濾過効率が低下し
てしまうという欠点があつた。 Furthermore, conventional water purifier modules using porous hollow fiber membranes are formed only from hydrophilic membranes, and if gas gets mixed in, the mixed gas will not easily pass through at normal pressures such as 1 kg/ cm2 . Instead, gas accumulates on the membrane surface, which impedes water permeation and reduces the overall filtration efficiency of the membrane.
部分濾過型膜モジユールでは混入した気体は未
濾過液と共に系外に出るる場合もあるが、全量濾
過型の膜モジユールではモジユールに混入した気
体は系外に出ることはできず、大量の気体が混入
した場合はほとんど水を濾過できないような状態
におちいることがあり、その対策に苦慮していた
ものである。 In partial filtration type membrane modules, mixed gas may exit the system along with the unfiltered liquid, but in total filtration type membrane modules, gas mixed in the module cannot exit the system, and a large amount of gas If this happens, the water can become almost impossible to filter, and it has been difficult to find countermeasures.
この対策として液体中に気体が混入しない様
にあらかじめ脱気する。濾過器内の液体の流れ
を上から下へと流れる様にして、混入した気体が
上部にたまつて液体の濾過を妨げない様にする。
上方入口側に気体だめと気体抜きのコツク等を
設けて混入した気体を系外に除去する等の手段が
考えられるが、液体中の気体をあらかじめ脱気し
ておく方法は大がかりなタンク、真空ポンプ等を
必要とし、又混入気体を上方にためる方法は大量
の気体が混入したときはやはり濾過効率の低下を
招くという欠点を有している。気体だめと気体抜
きコツクを設ける方法は気体だめを大きくとると
処理液体量に比べてモジユールの容量が大きくな
り、かつデツドスペースが大きくなるし、気体だ
めを小さくすると頻繁にコツクを操作して気体を
抜かなければならないという頻雑な手間が必要に
なるという様に簡易型浄水器には適用しがたいも
のであつた。 As a countermeasure to this, deaerate the liquid in advance to prevent gas from entering the liquid. The liquid in the filter is made to flow from top to bottom so that mixed gas does not accumulate at the top and interfere with the filtration of the liquid.
It is possible to remove the mixed gas from the system by installing a gas reservoir and a gas removal pot on the upper inlet side, but the method of degassing the gas in the liquid in advance requires a large tank or a vacuum. The method that requires a pump or the like and stores the mixed gas upward has the disadvantage that the filtration efficiency decreases when a large amount of gas is mixed. The method of installing a gas reservoir and a gas removal pot is that if the gas reservoir is made large, the capacity of the module will be large compared to the amount of liquid to be processed, and the dead space will also become large. It is difficult to apply it to a simple water purifier because it requires the frequent labor of having to remove the water.
そこで本考案者等は上記の欠点を解消した簡易
型浄水器を提供することを目的として検討に努め
本考案に到達した。 Therefore, the inventors of the present invention have conducted studies with the aim of providing a simple water purifier that eliminates the above-mentioned drawbacks, and have arrived at the present invention.
即ち本考案は上部に開口部を有する容器1と、
容器の該開口部を密封可能な蓋3と、該容器内部
と脱着可能に接続されている浄化器2とからな
り、蓋3には圧力抜き機構9を有する逆止弁付き
加圧装置4が容器内部と連通可能にとりつけられ
ており、浄化器2は内部に膜面の少なくとも一部
に疎水性部分12を有する多孔質中空糸膜と、親
水性多孔質中空糸膜11とからなる、開口端を開
口状態に保つたまま端部をポツテイング材で集束
固定されたU字型あるいは他端を封じた多孔質中
空糸束を有する筒とからなつており、浄化器2が
容器1からとりはずし可能である簡易型浄水器に
ある。 That is, the present invention includes a container 1 having an opening at the top,
It consists of a lid 3 that can seal the opening of the container, and a purifier 2 that is removably connected to the inside of the container. The purifier 2 is attached to the inside of the container so as to be able to communicate with the inside, and the purifier 2 has an opening formed inside the porous hollow fiber membrane having a hydrophobic portion 12 on at least a part of the membrane surface and a hydrophilic porous hollow fiber membrane 11. It consists of a U-shaped tube with one end kept open and fixed with a potting material, or a tube with a bundle of porous hollow fibers sealed at the other end, so that the purifier 2 can be removed from the container 1. This is a simple water purifier.
本考案の簡易型浄水器は、容器として300ml〜
5程度の容量のものが好ましく用いられる。容
器ハウジングは内部が若干加圧になるため剛性の
あるものがよく、また、耐蝕性であることが好ま
しい。ポリカーボネート、ポリスチレン、AS樹
脂、ABS樹脂、MMA樹脂等のプラスチツクあ
るいは耐蝕性金属製のものが好ましく用いられ
る。 The simple water purifier of this invention has a container size of 300ml or more.
A capacitor having a capacity of about 5 is preferably used. The container housing is preferably rigid since the inside thereof is slightly pressurized, and is preferably corrosion resistant. Plastics such as polycarbonate, polystyrene, AS resin, ABS resin, MMA resin, or materials made of corrosion-resistant metal are preferably used.
本考案に用いられる膜面の少なくとも一部に疎
水性部分を有する多孔質中空糸膜としてはポリオ
レフイン系、フルオロカーボン系、ポリエステル
系、EVA系、ポリアミド系等を用いることがで
きる。親水性多孔質中空糸膜としてはセルロース
系、PVA系あるいは上記に記載した疎水性多孔
質中空糸膜をアルコール類、界面活性剤等により
一時的に親水化したもの、表面に親水性モノマー
をグラフトしたり親水性ポリマーをコートしたり
して恒久又は半恒久的に親水化したもの等種々の
親水性多孔質中空糸膜を用いることができる。さ
らに該多孔質中空糸膜としてはパイロジエンも阻
止できるものであることが好ましい。ポリオレフ
イン系の多孔質中空糸膜を用いるとフタル酸エス
テル等の有機物を除去することができる。膜面の
少なくとも一部に疎水性部分を有する多孔質中空
糸膜と親水性多孔質中空糸膜とからなる多孔質中
空糸束を形成する方法としては上記の様な疎水性
多孔質中空糸膜と親水性多孔質中空糸膜とを一つ
に束ねてもよく、あらかじめ全体を親水化してお
いた疎水性多孔質中空糸膜を束ねて例えばハウジ
ング内部に収納してモジユールとした後、その中
空糸束の一部を疎水性に戻してもよい。多孔質中
空糸束内での疎水性部分の分布状態は均一であつ
てもよく、疎水性部分が島状又は縞状になつてい
てもよいが、疎水性部分を中空糸束の外周部の少
なくとも一部に配したものがより好ましい。これ
は、通常、中空糸モジユールでは中空糸束がその
外周部より中心部の方が密度が高く、気体は中空
糸束外周と外筒の間にたまり易いため、疎水性部
分は中空糸束外周部にある方が気体が抜け易いと
いう理由による。また、疎水性部分の位置は上下
どちらにあつてもよいが、気体は液体より比重が
軽いためモジユールに組んだとき上部に疎水性部
分があることが好ましい。従つて疎水性中空糸膜
を親水化した後部分的に疎水性に戻す方法をとる
場合は集束固定部分及び該集束固定部分近傍のみ
を疎水化することが好ましい。 As the porous hollow fiber membrane having a hydrophobic portion on at least a portion of the membrane surface used in the present invention, polyolefin-based, fluorocarbon-based, polyester-based, EVA-based, polyamide-based, etc. can be used. Hydrophilic porous hollow fiber membranes include cellulose-based, PVA-based, or hydrophobic porous hollow fiber membranes described above that have been temporarily made hydrophilic with alcohols, surfactants, etc., or those that have hydrophilic monomers grafted onto the surface. Various hydrophilic porous hollow fiber membranes can be used, such as those made permanently or semi-permanently hydrophilic by coating with a hydrophilic polymer. Furthermore, it is preferable that the porous hollow fiber membrane can also block pyrogen. When a polyolefin-based porous hollow fiber membrane is used, organic substances such as phthalate esters can be removed. As a method for forming a porous hollow fiber bundle consisting of a porous hollow fiber membrane having a hydrophobic portion on at least a part of the membrane surface and a hydrophilic porous hollow fiber membrane, the above-mentioned hydrophobic porous hollow fiber membrane can be used. and a hydrophilic porous hollow fiber membrane may be bundled together. For example, after the hydrophobic porous hollow fiber membranes, which have been made entirely hydrophilic in advance, are bundled and housed inside a housing to form a module, the hollow A portion of the yarn bundle may be made hydrophobic again. The distribution state of the hydrophobic parts within the porous hollow fiber bundle may be uniform, or the hydrophobic parts may be island-like or striped. It is more preferable that it is arranged at least in part. This is because in a hollow fiber module, the density of the hollow fiber bundle is normally higher at the center than at the outer periphery, and gas tends to accumulate between the outer periphery of the hollow fiber bundle and the outer cylinder, so the hydrophobic portion is located around the outer periphery of the hollow fiber bundle. This is because it is easier for gas to escape if it is located in the lower part. Further, the hydrophobic portion may be located either above or below, but since gas has a lower specific gravity than liquid, it is preferable that the hydrophobic portion be located at the top when assembled into a module. Therefore, when a method is adopted in which a hydrophobic hollow fiber membrane is made hydrophilic and then partially restored to hydrophobicity, it is preferable to hydrophobize only the focusing and fixing portion and the vicinity of the focusing and fixing portion.
この様な部分的に疎水化する方法としては例え
ば疎水性中空糸膜を親水化した多孔質中空糸膜を
用いたモジユールを集束固定部分が上になるよう
に置いて、重力によりモジユール内から水を自然
落下させる程度の方法で水抜きし、次に集束固定
部分が上になるようにモジユールを置いて例えば
アルコールを多孔質中空糸膜全体が充分濡れる程
度に添加し、次いで上側か1Kg/cm2程度の圧力で
圧縮空気を吹き込む方法をとることができる。そ
うするとアルコールは多孔質中空糸膜内に入り、
膜内の水と混合し、多孔質中空糸膜内を通つて系
外へ出て行き代つて膜内に空気が入り、膜のその
部分が乾燥、疎水化される。アルコールは中空糸
膜を通る最も抵抗の少ない箇所即ち集束固定部分
近傍から疎水化され、同時に集束固定部分も疎水
化される。空気を加圧、透過させる時間等で疎水
性部分の全膜面積に対する比率を調節することが
できる。 For example, a method for partially hydrophobicizing a hydrophobic hollow fiber membrane is to place a module using a porous hollow fiber membrane with the focused and fixed part facing upward, and then use gravity to release water from inside the module. Drain the water by allowing it to fall naturally, then place the module so that the focusing and fixing part faces up, add alcohol, for example, to the extent that the entire porous hollow fiber membrane is sufficiently wet, and then add 1 kg/cm of alcohol to the upper side. You can use a method of blowing compressed air at a pressure of about 2 . The alcohol then enters the porous hollow fiber membrane,
It mixes with the water in the membrane and exits the system through the porous hollow fiber membrane, causing air to enter the membrane and dry and hydrophobize that part of the membrane. The alcohol is made hydrophobic through the hollow fiber membrane from the point of least resistance, that is, near the focusing and fixing part, and at the same time, the focusing and fixing part is also made hydrophobic. The ratio of the hydrophobic portion to the total membrane area can be adjusted by pressurizing air, time for permeation, etc.
さらに、膜面の少なくとも一部に疎水性部分1
2を有する多孔質中空糸膜を中空糸束の外周部の
少なくとも一部にのみ配する方法としては親水性
中空糸束の周囲に疎水性多孔質中空糸膜を配して
もよく、上記の部分疎水化時に中空糸束を比較的
に密にしておいて周辺部のみを疎水化する様にし
てもよい。中空糸膜全体に対する疎水性部分の比
率は処理すべき水性液体の粘度、液体中に存在す
る気体の量に依存するが、0.2乃至10%であるこ
とが好ましい。10%以上あつても気体抜き効果は
それほど増大せず、むしろ水性液体を濾過する親
水性膜部分がその分少なくなるため好ましくな
い。0.2%以下では気体抜き効果が充分でないた
め好ましくない。 Furthermore, a hydrophobic portion 1 is provided on at least a portion of the membrane surface.
As a method of disposing a porous hollow fiber membrane having 2 only on at least a part of the outer periphery of the hollow fiber bundle, a hydrophobic porous hollow fiber membrane may be disposed around a hydrophilic hollow fiber bundle, and At the time of partial hydrophobization, the hollow fiber bundle may be made relatively dense and only the peripheral portion may be hydrophobized. The ratio of the hydrophobic portion to the entire hollow fiber membrane depends on the viscosity of the aqueous liquid to be treated and the amount of gas present in the liquid, but is preferably 0.2 to 10%. Even if it is 10% or more, the gas removal effect will not increase much, and in fact, the hydrophilic membrane portion that filters the aqueous liquid will decrease accordingly, which is not preferable. If it is less than 0.2%, it is not preferable because the gas removal effect is not sufficient.
多孔質中空糸の膜としての面積は0.1〜1m2程
度あることが好ましい。 The area of the porous hollow fibers as a membrane is preferably about 0.1 to 1 m 2 .
加圧装置としては手動で容器内を容易に加圧で
きるものであれば、どのようなものも用い得るが
血圧測定器に用いられる。いわゆるゴム球が逆止
弁、圧力抜き機構を有し、加圧、圧力抜きが容易
であること、容易に大量に入手し得ることから好
ましく用いられる。圧力抜き機構とは圧力が必要
な時に操作すれば容器内の圧力を抜いて外気圧と
同じに戻すことができる機構である。 Any pressurizing device can be used as long as it can easily manually pressurize the inside of the container, but it is used in blood pressure measuring devices. So-called rubber balls are preferably used because they have a check valve and a pressure release mechanism, are easy to pressurize and release, and are easily available in large quantities. The pressure relief mechanism is a mechanism that can be operated when pressure is needed to relieve the pressure inside the container and return it to the same pressure as the outside pressure.
以下に添付図面に基づき本考案をさらに詳しく
説明する。 The present invention will be described in more detail below with reference to the accompanying drawings.
第1図は本考案の簡易型浄水器の1実施例であ
り、第2図は他の実施例である。 FIG. 1 shows one embodiment of the simple water purifier of the present invention, and FIG. 2 shows another embodiment.
第3図は本考案の簡易型浄水器の蓋、加圧装
置、浄化水出口の1実施形態を示す図である。 FIG. 3 is a diagram showing one embodiment of the lid, pressurizing device, and purified water outlet of the simple water purifier of the present invention.
第4図及び第5図は本考案の実施例のモジユー
ルであり、第4図はU字型多孔質中空糸束を、第
5図は他端を閉塞した多孔質中空糸束を収納した
モジユールである。図中A及びCは平面図であ
り、B及びDは一部欠載縦断面図である。 Figures 4 and 5 show modules according to embodiments of the present invention; Figure 4 shows a U-shaped porous hollow fiber bundle, and Figure 5 shows a module housing a porous hollow fiber bundle with the other end closed. It is. In the figures, A and C are plan views, and B and D are longitudinal cross-sectional views, with some parts missing.
図において1は容器、2は浄化器、3は容器1
の開口部の蓋、4は加圧装置、5は多孔質中空糸
膜、6は活性炭及び/又はイオン交換樹脂、7は
多孔質中空糸支持固定部、8は浄化水導出管、9
は圧力抜き機構、10は逆止弁、11は親水性多
孔質中空糸膜、12は多孔質中空糸膜の疎水性部
分を示す。第4図、第5図において疎水性部分1
2は黒く塗りつぶされているが、これは閉塞ある
いは着色されていることを示すものではなく、単
に親水性膜部分と区別するためのものである。 In the figure, 1 is a container, 2 is a purifier, and 3 is a container 1
, 4 is a pressurizing device, 5 is a porous hollow fiber membrane, 6 is activated carbon and/or ion exchange resin, 7 is a porous hollow fiber support and fixing part, 8 is a purified water outlet pipe, 9
10 is a pressure relief mechanism, 10 is a check valve, 11 is a hydrophilic porous hollow fiber membrane, and 12 is a hydrophobic portion of the porous hollow fiber membrane. In Figures 4 and 5, hydrophobic portion 1
2 is painted black, but this does not indicate that it is blocked or colored, but is simply to distinguish it from the hydrophilic membrane portion.
第1図は浄化器2が容器1が外側に出ている例
であり、この場合は容器1の下部側面に側管14
があり、その端部は浄化器2の下部入口と脱着可
能に接続している。 Figure 1 shows an example in which the purifier 2 has a container 1 protruding outside, and in this case, a side pipe 14 is attached to the lower side of the container 1.
The end thereof is removably connected to the lower inlet of the purifier 2.
側管14には開閉コツクあるいは、浄化器2を
取付けた場合にのみ開く弁を有して、取はずし状
態で容器内の水が洩れないようになつていること
が好ましい。 It is preferable that the side pipe 14 has an opening/closing mechanism or a valve that opens only when the purifier 2 is installed, so that the water in the container does not leak when the purifier 2 is removed.
容器1の上部に設けた開口部は非常時に河川や
池、湖沼から適当な容器で汲んで入れたり、ある
いは水割りウイスキー等を作るための冷却水作成
用に永等を投入できる様広口であることが好まし
い。 The opening provided at the top of the container 1 should be wide-mouthed so that in case of an emergency, water can be pumped from rivers, ponds, lakes and marshes into a suitable container, or a container can be poured in to create cooling water for making water-split whiskey, etc. is preferred.
蓋3はこの開口部を密封可能なものであり、蓋
3には孔があいていてこの孔に気密に加圧装置4
が取りつけられている。 The lid 3 is capable of sealing this opening, and the lid 3 has a hole, and a pressurizing device 4 is inserted into the hole airtight.
is attached.
第2図は浄化器2が容器1内に収納されている
例である。 FIG. 2 shows an example in which the purifier 2 is housed within the container 1.
第1図における側管14の位置、及び第2図の
おける浄化器下部入口の位置は浄化される水がき
れいな時は容器内の水を有効利用するために容器
の底に近いことが好ましい。 The position of the side pipe 14 in FIG. 1 and the position of the lower inlet of the purifier in FIG. 2 are preferably close to the bottom of the container in order to make effective use of the water in the container when the water to be purified is clean.
しかし、池や川の水等よごれや沈降性浮遊物を
含む水の場合は、容器底部にこれらが堆積して側
管あるいは浄化器下部入口がつまる恐れがあるた
め容器底から5mm〜2cm離れていることが好まし
い。 However, if the water contains dirt or sedimentary suspended matter, such as water from a pond or river, there is a risk that these will accumulate at the bottom of the container and clog the side pipe or lower inlet of the purifier, so keep the water 5 mm to 2 cm away from the bottom of the container. Preferably.
各々の用途むけに容器1の底からの高さをかえ
たタイプを用意することも可能であるが、1つの
浄水器で底からの高さを水質にあわせて変更でき
る様にすることが好ましい。例えば第1図のもの
では底からの高さの異なる側管を複数個設け、水
質にあわせて浄化器2を適切な高さの側管に接続
する方法をとることができる。第2図の例では例
えば浄化器を挿入、支持する蓋3の挿入孔の周辺
部をゴム等の弾性体にしてゴムと浄化器2の筒と
の間の摩擦抵抗で浄化器2を任意の位置に固定
し、かつ水浄化時の加圧でも気密を保持できるよ
うにすることもでき、また浄化器筒外側の所定部
分にネジ山を設け蓋3の浄化器挿入孔にもこれに
あつたネジを切つてネジ込みの程度で底からの位
置を任意に設定できる様にしてもよい。 Although it is possible to prepare types with different heights from the bottom of the container 1 for each purpose, it is preferable to use one water purifier so that the height from the bottom can be changed according to the water quality. . For example, in the case of FIG. 1, a method can be adopted in which a plurality of side pipes having different heights from the bottom are provided and the purifier 2 is connected to the side pipes at an appropriate height depending on the water quality. In the example shown in FIG. 2, for example, the periphery of the insertion hole of the lid 3 for inserting and supporting the purifier is made of an elastic material such as rubber, and the frictional resistance between the rubber and the tube of the purifier 2 allows the purifier 2 to be moved freely. It can be fixed in position and maintain airtightness even when pressurized during water purification.Furthermore, a screw thread is provided at a predetermined part on the outside of the purifier cylinder to fit the purifier insertion hole in the lid 3. The position from the bottom may be set arbitrarily by cutting the screw and adjusting the screw-in level.
浄化器2は内部に膜面の少なくとも一部に疎水
性部分12を有する多孔質中空糸膜と、親水性多
孔質中空糸膜11とからなる、開口端を開口状態
に保つたまま端部をウレタン等のポツテイング材
で集束固定されたU字型あるいは他端を封じた多
孔質中空糸束を有する筒とからなつている。 The purifier 2 consists of a porous hollow fiber membrane having a hydrophobic portion 12 on at least a part of the membrane surface inside, and a hydrophilic porous hollow fiber membrane 11. It consists of a U-shaped tube that is bundled and fixed with a potting material such as urethane, or a tube that has a porous hollow fiber bundle whose other end is sealed.
浄化器2内に水を下から上に流すと混入した気
体は間隙の小さい中空糸と中空糸の間よりも比較
的間隙の大きい中空糸束と外筒の間を通つて上方
に移動し、その間に疎水性部分12で膜を透過し
て浄化器2外に排出される。浄化器2内最上部に
達した気体もその周辺にある疎水性部分12で膜
を透過して浄化器2外に排出される。 When water flows into the purifier 2 from the bottom to the top, the mixed gas moves upward through the gap between the hollow fiber bundle and the outer cylinder, which has a relatively large gap, rather than between the hollow fibers, which have a small gap. During this time, the water passes through the membrane through the hydrophobic portion 12 and is discharged to the outside of the purifier 2. The gas that has reached the top of the purifier 2 also passes through the membrane at the hydrophobic portion 12 around it and is discharged to the outside of the purifier 2.
第1図における側管部入口、第2図における浄
化器下部入口にはプレフイルターを設けてごみ等
が浄化器内に入らない様にしてもよい。 A pre-filter may be provided at the side pipe inlet in FIG. 1 and at the lower inlet of the purifier in FIG. 2 to prevent dirt and the like from entering the purifier.
また、プレフイルターを第1図の例では、例え
ば容器蓋部で容器内部壁面に密着した容器内容積
とほぼ同一の大きさの袋としてもよく、第2図の
例では浄化器2の下部入口を含めて浄化器の少な
くとも一部を包む袋としてもよい。 Furthermore, in the example shown in FIG. 1, the prefilter may be a bag of approximately the same size as the internal volume of the container, which is in close contact with the inner wall surface of the container at the container lid, and in the example shown in FIG. It may also be a bag that encloses at least a portion of the purifier including the purifier.
親水性の多孔質中空糸膜は通常、一旦乾燥する
と孔形状が変わり透水性が低下することが多く、
またポリオレフイン等疎水性多孔質中空糸膜をア
ルコール等で親水化したものは乾燥により疎水性
に戻り、多少の圧力では水を透さなくなることが
ある。 Typically, once a hydrophilic porous hollow fiber membrane dries, the pore shape changes and water permeability often decreases.
Furthermore, hydrophobic porous hollow fiber membranes such as polyolefins made hydrophilic with alcohol or the like return to hydrophobicity upon drying, and may become impermeable to water under some pressure.
従つて浄化器2をとりはずした時に水が洩出し
て多孔質中空糸膜が乾燥するのを防止するために
浄化器の下部入口に逆止弁が設けてあることが好
ましい。 Therefore, in order to prevent water from leaking out and drying the porous hollow fiber membrane when the purifier 2 is removed, a check valve is preferably provided at the lower inlet of the purifier.
本考案の簡易型浄水器は浄化器2内に設けた多
孔質中空糸膜5の束を水が透過するだけで細菌等
を除去できるが、臭い、味等を改善するために活
性炭及び/又はイオン交換樹脂6を浄化器2内に
入れておいてもよい。活性炭やイオン交換樹脂は
浄化器2筒内の多孔質中空糸膜5のない部分にフ
イルター等で仕切を設け、そこに入れてもよい
が、活性炭やイオン交換樹脂を各々布製袋や浄化
器2の筒内径と同一あるいはこれより小さい外径
を有し上下面は自由に水を通し、活性炭やイオン
交換樹脂のほとんどを透さない沢山の微孔を有す
る筒内に入れてもよい。 The simple water purifier of the present invention can remove bacteria, etc. by simply allowing water to pass through a bundle of porous hollow fiber membranes 5 provided in the purifier 2, but in order to improve odor, taste, etc., activated carbon and/or The ion exchange resin 6 may be placed inside the purifier 2. Activated carbon and ion exchange resin may be put in a partition with a filter etc. in the part of the purifier 2 cylinders where there is no porous hollow fiber membrane 5, but activated carbon and ion exchange resin may be placed in cloth bags or in purifier 2 respectively. It may be placed in a cylinder that has an outer diameter that is the same as or smaller than the inner diameter of the cylinder, has upper and lower surfaces that freely allow water to pass through, and has many micropores that do not allow most of the activated carbon or ion exchange resin to pass through.
使用されるイオン交換樹脂としては金属イオン
を除去するため陽イオン交換樹脂を少なくとも用
いることが好ましい。また、活性炭としては例え
ば塩化銀等制菌性あるいは殺菌性物質を表面にコ
ートしたものが浄化器内の菌の繁殖をおさえる意
味で好ましく用いられる。活性炭、イオン交換樹
脂は粒状に限らず例えば繊維状のものであつても
よい。 As the ion exchange resin used, it is preferable to use at least a cation exchange resin in order to remove metal ions. Furthermore, activated carbon whose surface is coated with an antibacterial or bactericidal substance such as silver chloride is preferably used in order to suppress the proliferation of bacteria within the purifier. Activated carbon and ion exchange resin are not limited to granular forms, but may be, for example, fibrous forms.
浄化器2の上部の浄化水導出管8は先端が横乃
至下をむいていることが好ましい。また、浄化水
導出管8の先及び加圧装置4は携帯時に便利な様
に取り外し可能であることが好ましい。 The purified water outlet pipe 8 at the upper part of the purifier 2 preferably has a tip facing sideways or downwards. Further, it is preferable that the end of the purified water outlet pipe 8 and the pressurizing device 4 are removable for convenience when carrying.
浄化器2の下部はとりはずし可能にして活性炭
及び/又ははイオン交換樹脂を使用した場合その
交換、中空糸膜の洗浄ができる様にすることもで
きる。 The lower part of the purifier 2 can be made removable so that activated carbon and/or ion exchange resin, if used, can be replaced and the hollow fiber membrane can be cleaned.
第3図の様に浄化水導出管8の先及び加圧装置
4を蓋3の横から出すこともできる。 As shown in FIG. 3, the end of the purified water outlet pipe 8 and the pressurizing device 4 can also be taken out from the side of the lid 3.
本考案の浄水器は、容器1の開口部より容器に
浄化すべき水を入れ、蓋3をしめて浄化器2をと
りつけ、加圧装置4をくりかえし圧縮して必要な
程度まで容器1内を加圧すると、水は好ましくは
プレフイルターで大きなごみ、砂等が除去され、
浄化器2の下部入口13を通り、好ましくは活性
炭、イオン交換樹脂で臭、味成分が吸着され、多
孔質中空糸で細菌、コロイド等汚濁物、さらに好
ましくはパイロジエンも除去された清浄な水が得
られ、飲用、調理用等に供せられる。 In the water purifier of the present invention, water to be purified is poured into the container from the opening of the container 1, the lid 3 is closed, the purifier 2 is attached, and the pressure device 4 is repeatedly compressed to heat the inside of the container 1 to the required degree. When pressed, the water is preferably prefiltered to remove large debris, sand, etc.
Clean water passes through the lower inlet 13 of the purifier 2, with odor and taste components preferably adsorbed by activated carbon or ion exchange resin, and from which contaminants such as bacteria and colloids, and more preferably pyrogene, are removed by porous hollow fibers. It can be used for drinking, cooking, etc.
本考案は、以上に述べた様に細菌、パイロジエ
ン等が除去され、不快臭味等のない浄化水が簡便
に得られ、海外旅行時、災害の際の避難時にも簡
便に携帯でき、河川、湖沼、池の水あるいは長期
間備蓄した後の水等飲用に不適な水を簡単に飲用
可能とすることができ、また浄化器内に空気が混
入した場合でも膜の疎水性部分を通して空気が浄
化器外に出るため、濾過効率の低下が生じず、操
作も簡便であり、実用上特に有効な浄水器であ
る。 As mentioned above, the present invention removes bacteria, pyrogen, etc., easily obtains purified water without unpleasant odors, tastes, etc., and can be easily carried when traveling overseas or evacuating in the event of a disaster. Water that is not suitable for drinking, such as lake water, pond water, or water that has been stored for a long time, can be easily made drinkable.Also, even if air gets into the purifier, the air can be purified through the hydrophobic part of the membrane. Because the water exits outside the vessel, there is no reduction in filtration efficiency, and the operation is simple, making it a particularly effective water purifier in practice.
第1図は本考案の簡易型浄水器の1実施例であ
り、第2図は他の実施例である。第3図は本考案
の簡易型浄化水器の蓋、加圧装置、浄化水出口の
1実施形態を示す図である。第4図及び第5図は
本考案に用いられる浄化器の例であり、第4図は
U字型中空糸束を、第5図は他端を閉塞した中空
糸束を収納したモジユールである。図中A及びC
は平面図であり、B及びDは一部欠載縦断面図で
ある。
1:容器、2:浄化器、3:容器1の開口部の
蓋、4:加圧装置、5:多孔質中空糸膜、6:活
性炭及び/又はイオン交換樹脂、7:多孔質中空
糸支持固定部、8:浄化水導出管、9:圧力抜き
機構、10:逆止弁、11:親水性多孔質中空糸
膜、12:多孔質中空糸膜の疎水性部分。
FIG. 1 shows one embodiment of the simple water purifier of the present invention, and FIG. 2 shows another embodiment. FIG. 3 is a view showing one embodiment of the lid, pressurizing device, and purified water outlet of the simple water purifier of the present invention. Figures 4 and 5 are examples of purifiers used in the present invention, with Figure 4 showing a U-shaped hollow fiber bundle, and Figure 5 showing a module housing a hollow fiber bundle with the other end closed. . A and C in the diagram
is a plan view, and B and D are longitudinal cross-sectional views with some parts missing. 1: Container, 2: Purifier, 3: Lid for opening of container 1, 4: Pressurizing device, 5: Porous hollow fiber membrane, 6: Activated carbon and/or ion exchange resin, 7: Porous hollow fiber support Fixed part, 8: Purified water outlet pipe, 9: Pressure release mechanism, 10: Check valve, 11: Hydrophilic porous hollow fiber membrane, 12: Hydrophobic portion of the porous hollow fiber membrane.
Claims (1)
口部を密封可能な蓋3と、該容器内部と脱着可
能に接続されている浄化器2とからなり、蓋3
には圧力抜き機構を有する逆止弁付き加圧装置
4が容器内部と連通可能にとりつけられてお
り、浄化器2は内部に膜面の少なくとも一部に
疎水性部分12を有する多孔質中空糸膜と、親
水性多孔質中空糸膜11とからなる、開口端を
開口状態に保つたまま端部をポツテイング材で
集束固定されたU字型あるいは他端を封じた多
孔質中空糸束を有する筒とからなつており、浄
化器2が容器1からとりはずし可能である簡易
型浄水器。 2 膜面の少なくとも一部に疎水性部分12を有
する多孔質中空糸膜が中空糸束の外周部の少な
くとも一部に配され、中空糸束の中央部は実質
的に親水性多孔質中空糸膜のみからなることを
特徴とする実用新案登録請求の範囲第1項記載
の簡易型浄水器。 3 該疎水性部分12の膜面積が全体の膜面積の
0.2〜10%であることを特徴とする実用新案登
録請求の範囲第1項又は第2項記載の簡易型浄
水器。 4 該膜面の一部に疎水性部分12を有する多孔
質中空糸膜が集束固定部分及び該集束固定部分
近傍のみが疎水性であることを特徴とする実用
新案登録請求の範囲第1項、第2項又は第3項
記載の簡易型浄水器。 5 浄化器2内にさらに活性炭及び/又はイオン
交換樹脂を収納していることを特徴とする実用
新案登録請求の範囲第1項又は第2項記載の簡
易型浄水器。 6 浄化器2の下部入口に逆止弁が設けられてい
ることを特徴とする実用新案登録請求の範囲第
1項又は第2項又は第5項記載の簡易型浄水
器。[Claims for Utility Model Registration] 1. Consisting of a container 1 having an opening at the top, a lid 3 capable of sealing the opening of the container, and a purifier 2 detachably connected to the inside of the container, Lid 3
A pressurizing device 4 with a check valve and a pressure release mechanism is attached to the container so as to be able to communicate with the inside of the container, and the purifier 2 is equipped with a porous hollow fiber having a hydrophobic portion 12 on at least a part of the membrane surface inside. It has a U-shaped porous hollow fiber bundle consisting of a membrane and a hydrophilic porous hollow fiber membrane 11, the end of which is bundled and fixed with a potting material while keeping the open end open, or the other end is sealed. This simple water purifier consists of a cylinder and a purifier 2 is removable from a container 1. 2. A porous hollow fiber membrane having a hydrophobic portion 12 on at least a portion of the membrane surface is disposed on at least a portion of the outer periphery of the hollow fiber bundle, and the center portion of the hollow fiber bundle is substantially made of hydrophilic porous hollow fibers. A simple water purifier according to claim 1, characterized in that it consists of only a membrane. 3 The membrane area of the hydrophobic portion 12 is the total membrane area.
2. A simple water purifier according to claim 1 or 2, characterized in that the concentration is 0.2 to 10%. 4. Utility model registration claim 1, wherein the porous hollow fiber membrane having a hydrophobic portion 12 on a part of the membrane surface is hydrophobic only in the focusing fixing portion and the vicinity of the focusing fixing portion, The simple water purifier according to item 2 or 3. 5. The simple water purifier according to claim 1 or 2 of the utility model registration claim, characterized in that the purifier 2 further contains activated carbon and/or ion exchange resin. 6. The simple water purifier according to claim 1, 2, or 5, characterized in that a check valve is provided at the lower inlet of the purifier 2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14352183U JPS6049986U (en) | 1983-09-16 | 1983-09-16 | Simple water purifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14352183U JPS6049986U (en) | 1983-09-16 | 1983-09-16 | Simple water purifier |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6049986U JPS6049986U (en) | 1985-04-08 |
JPH0133191Y2 true JPH0133191Y2 (en) | 1989-10-09 |
Family
ID=30320340
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14352183U Granted JPS6049986U (en) | 1983-09-16 | 1983-09-16 | Simple water purifier |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6049986U (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62125804A (en) * | 1985-11-27 | 1987-06-08 | Toomee Sangyo Kk | Simple liquid purifier |
JP2717663B2 (en) * | 1987-10-12 | 1998-02-18 | テルモ株式会社 | Hollow fiber membrane dialysis machine |
JP2533718Y2 (en) * | 1989-07-28 | 1997-04-23 | 株式会社クラレ | Water purifier |
JPH0621541Y2 (en) * | 1991-11-07 | 1994-06-08 | トーメー産業株式会社 | Simple liquid purification device |
GB2443608B (en) * | 2006-09-25 | 2008-11-12 | Michael Pritchard | A water purifying device |
-
1983
- 1983-09-16 JP JP14352183U patent/JPS6049986U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6049986U (en) | 1985-04-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR880000292Y1 (en) | Hollow fiber filtering module | |
JP3224383B2 (en) | Water purification container and hydrant water purification method | |
US7507338B2 (en) | Universal water purifier unit assembly device | |
US3327859A (en) | Portable unit for potable water | |
US5536403A (en) | Liquid purification system with microfiltration means, disinfection means and adsorption means | |
US4976866A (en) | Concentric tubular membrane device and process useful in ion exchange or absorbent processes | |
JP2004230358A (en) | Desk top type water purifier | |
JPH0133191Y2 (en) | ||
CN206915909U (en) | central pure water system | |
CN112299587A (en) | Portable reverse osmosis purifier | |
RU68348U1 (en) | FILTER MATERIAL AND BACTERICIDAL DEVICE | |
US20030136724A1 (en) | Water filtering device | |
JPH0243518Y2 (en) | ||
RU2568730C1 (en) | Individual facility for liquid purification | |
KR880000940Y1 (en) | A clean water device using filter module | |
JPH01262983A (en) | Water purifying device | |
RU2432980C2 (en) | Filtration element and water cleaning filter | |
CN211733999U (en) | Emergency water storage tank structure of water dispenser with separation function | |
CN214571075U (en) | Portable reverse osmosis purifier | |
RU51522U1 (en) | WATER TREATMENT DEVICE | |
JP2559041Y2 (en) | Water purifier | |
JPS62132586A (en) | Water cleaning device | |
JP3563515B2 (en) | Water purifier | |
JPH055994Y2 (en) | ||
RU24650U1 (en) | WATER TREATMENT DEVICE |