JPH11207391A - Water purifying and treatment device - Google Patents
Water purifying and treatment deviceInfo
- Publication number
- JPH11207391A JPH11207391A JP10016059A JP1605998A JPH11207391A JP H11207391 A JPH11207391 A JP H11207391A JP 10016059 A JP10016059 A JP 10016059A JP 1605998 A JP1605998 A JP 1605998A JP H11207391 A JPH11207391 A JP H11207391A
- Authority
- JP
- Japan
- Prior art keywords
- water
- filter
- magnetic
- secondary side
- reverse osmosis
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
- C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
Landscapes
- Health & Medical Sciences (AREA)
- Clinical Laboratory Science (AREA)
- 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)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、河川水、湖沼水、
海水、灌水等の原水から直接医療用として用いることの
できる浄化水を直接得ることのできる水の浄化処理装置
に関する。特に、本件に係る水の浄化処理装置で得られ
る浄化水は、人工透析用水の調整に用いることのできる
レベルの清浄度を有するものとなる。TECHNICAL FIELD The present invention relates to river water, lake water,
The present invention relates to a water purification treatment apparatus capable of directly obtaining purified water that can be used for medical use directly from raw water such as seawater or irrigation water. In particular, purified water obtained by the water purification treatment device according to the present invention has a level of cleanliness that can be used for adjustment of artificial dialysis water.
【0002】[0002]
【従来の技術】清浄な水を確保すると言うことは、人間
のライフラインの確保を意味し、市民の円滑な日常生活
の維持を可能とし、産業活動の停滞を防止するものであ
る。清浄度の高い水を要求する分野としては、電子産業
分野、薬品化学分野等種々の分野が考えられる。中で
も、医療に使用する水は、人間の生命に関わるものとし
て水の清浄度の低下は許容できるものではない。2. Description of the Related Art Securing clean water means securing a human lifeline, making it possible for citizens to maintain a smooth daily life, and preventing stagnation in industrial activities. Various fields, such as a field of the electronics industry and a field of chemical chemistry, can be considered as fields that require highly clean water. Above all, water used for medical treatment is not tolerable to decrease the cleanliness of water as it relates to human life.
【0003】一般に、医療用に用いられる水を得る原水
は、水道水、井戸水の如き比較的清浄な水が使用されて
いるのが通常である。例えば、人工透析用に用いる浄化
水は、パイロジェンフリーの用水、即ち微生物汚染であ
るエンドトキシンやグルカン等の微生物に由来する生理
活性物質を完全に除去したものであり、この浄化水を用
いて、市販の電解質濃縮液である原液を希釈混合して人
工透析用水として調整するものであり、この浄化水を汚
染の心配なく処理精製するためには大規模な浄化処理装
置が用いられている。In general, relatively clean water such as tap water and well water is used as raw water for obtaining water used for medical purposes. For example, purified water used for artificial dialysis is pyrogen-free water, i.e., completely removed biologically active substances derived from microorganisms such as endotoxin and glucan, which are microbial contaminants. The stock solution as an electrolyte concentrate is diluted and mixed to prepare water for artificial dialysis. A large-scale purification treatment apparatus is used to treat and purify the purified water without fear of contamination.
【0004】ところが、地震や大規模な火災等の災害発
生時に、被災地では水道配管の破裂による断水の発生、
水の浄化処理施設の損壊により医療用に用いることので
きるレベルの水を得るための水道水や井戸水等の比較的
汚染度の低い原水の確保が困難になり浄化水を安定して
得ることができなくなる場合が想定できる。However, in the event of a disaster such as an earthquake or a large-scale fire, in the stricken area, the water supply is cut off due to the rupture of water pipes.
Damage to the water purification facility makes it difficult to obtain tap water and well water with relatively low pollution such as tap water and well water to obtain water of a level that can be used for medical treatment, and it is possible to obtain purified water stably. It can be assumed that it will not be possible.
【0005】また、医療用に用いることのできるレベル
の水を得るための浄化処理装置は一般に大型のものが多
くトラック等の移動体に積載することは不可能である。
一方、小型で実験室レベルで使用できるようなものは、
水の浄化処理能力が劣り、被災時に大量の医療用水が必
要になる場合には対応できないという不合理が生じてい
た。[0005] Further, many purification treatment apparatuses for obtaining water at a level that can be used for medical purposes are generally large and cannot be loaded on a moving body such as a truck.
On the other hand, those that are small and can be used at the laboratory level are:
Water purification treatment capacity is poor, and it is unreasonable that a large amount of medical water is needed in the event of a disaster.
【0006】[0006]
【発明が解決しようとする課題】そこで、本発明は、汚
染度が高く、一般に医療用水の原水として用いることの
ない河川水、湖沼水、海水、灌水等を原水として利用し
た場合でも、このような原水から直接的に目的とする医
療用水として用いることのできる程度の清浄度を有する
浄化水を得ることの可能な水の浄化処理装置を提供せん
とするものである。Therefore, the present invention is applicable to a case where river water, lake water, seawater, irrigation water, etc., which are highly contaminated and are not generally used as raw water for medical treatment, are used as raw water. It is an object of the present invention to provide a water purification treatment apparatus capable of obtaining purified water having a degree of cleanliness that can be directly used as target medical water from natural raw water.
【0007】また、本発明に係る水の浄化処理装置は、
トラック等の移動体に搭載可能な程度までの小型化が可
能な水の浄化処理装置を提供せんとしている。[0007] Further, the water purification treatment apparatus according to the present invention comprises:
The aim is to provide a water purification treatment device that can be made small enough to be mounted on a moving body such as a truck.
【0008】[0008]
【課題を解決するための手段】本発明に係る水の浄化装
置は、原水から医療用水として用いることのできる浄化
水を直接得ることのできる水の浄化処理装置であって、
複数の濾過手段である粗濾過器、精密濾過器、逆浸透膜
濾過器、活性炭濾過器、限外濾過器と各種ポンプとを連
結配管してなるものであり、原水の取水口から浄化水の
取り出し口に到るまでの全浄化経路の内、取水口から逆
浸透膜濾過器に到るまでの配管経路に1以上の磁気処理
手段を備え、その磁気処理手段により逆浸透膜濾過器に
流入する前の通過水に予め磁界をかけ磁気処理すること
をことを特徴とするものである。A water purifying apparatus according to the present invention is a water purifying apparatus capable of directly obtaining purified water that can be used as medical water from raw water,
It consists of a plurality of filtration means, a coarse filter, a microfilter, a reverse osmosis membrane filter, an activated carbon filter, an ultrafilter, and various pumps connected to each other. One or more magnetic processing means are provided in the piping route from the water intake to the reverse osmosis membrane filter out of the entire purification path to the discharge port, and the magnetic processing means flows into the reverse osmosis membrane filter. The method is characterized in that a magnetic field is applied in advance to the passing water before the magnetic treatment.
【0009】濾過手段の内、粗濾過器は、取水口より取
水ポンプにて汲み上げられた原水を最初に濾過し、原水
中に含まれた比較的大きな異物の除去を目的として用い
るものである。粗濾過器としては、いわゆる急速濾過器
又は高速濾過器が用いられる。ここで言う急速濾過器と
は、濾材にアンスラサイト及び砂を用いるが如き濾過器
をいい、高速濾過器とは、塩化ビニリデン等でできた特
殊繊維濾材を用いるが如き濾過器のことである。現実の
使用に際しては、急速濾過器又は高速濾過器のいずれか
一種が選択的に用いられる。急速濾過器と高速濾過器と
を併用して用いることも考えられるが、それぞれを単独
使用した場合とこの2つの濾過器を併用した場合を比べ
ても濾過効果に大きな差は生じない。Among the filtration means, the coarse filter is used for the purpose of first filtering raw water pumped from a water intake port by a water intake pump and removing relatively large foreign substances contained in the raw water. As the coarse filter, a so-called rapid filter or high-speed filter is used. As used herein, the term "rapid filter" refers to a filter using anthracite and sand as a filter medium, and the term "high-speed filter" refers to a filter using a special fiber filter made of vinylidene chloride or the like. In actual use, either a quick filter or a high-speed filter is selectively used. It is conceivable to use a combination of a rapid filter and a high-speed filter. However, there is no large difference in filtration effect between the case where each is used alone and the case where these two filters are used together.
【0010】精密濾過器は、少なくとも径5μmより大
きな異物の除去が可能な濾布からなる側壁を持つ中空の
円筒形濾過部材の複数本を金属製又は透明プラスチック
製等のケーシングの内部に備えたものであり、その円筒
形濾過部材の外部から通過水を流し円筒形濾過部材の側
壁を通じて濾材の中空内部に向かって濾過するものであ
る濾過器に代表されるものであるが、濾過部材の形状に
制約はない。この精密濾過器を用いて、少なくとも径5
μmより大きな異物を除去することで、精密濾過器の二
次側に配置されるポンプや逆浸透膜濾過器の逆浸透膜の
損傷を防ぎ、保護するものとなる。また、透明プラスチ
ック製ケーシングを用いると外部から溶液の流れを目視
確認しやすく、フィルター交換のタイミングも図りやす
くなる。The microfiltration device is provided with a plurality of hollow cylindrical filter members having side walls made of a filter cloth capable of removing foreign matters having a diameter of at least 5 μm inside a casing made of metal or transparent plastic. The filter is a typical example of a filter in which the passing water flows from the outside of the cylindrical filter member and is filtered toward the hollow inside of the filter medium through the side wall of the cylindrical filter member. There are no restrictions. Using this microfilter, at least 5
By removing foreign substances larger than μm, damage to a pump disposed on the secondary side of the microfilter and a reverse osmosis membrane of a reverse osmosis membrane filter can be prevented and protected. When a transparent plastic casing is used, the flow of the solution can be easily visually checked from the outside, and the timing for replacing the filter can be easily determined.
【0011】逆浸透膜濾過器は、その通過水中の不純物
及び汚染物を除去することを目的として使用される。こ
の逆浸透膜濾過器での濾過が、医療用水として用いるこ
とのできる清浄度を有する浄化水を直接得ることができ
るか否かを決定づけるものとなる。逆浸透膜濾過器とし
ては、一般に用いられるスパイラル型、中空糸型等のい
ずれのタイプの使用も可能である。[0011] Reverse osmosis membrane filters are used for the purpose of removing impurities and contaminants in the passing water. The filtration by the reverse osmosis membrane filter determines whether or not purified water having a cleanliness that can be used as medical water can be directly obtained. As the reverse osmosis membrane filter, any commonly used type such as a spiral type and a hollow fiber type can be used.
【0012】逆浸透膜濾過器の性能を最大限に引き出す
ためには、濾過が進むに従って発生する逆浸透膜から排
出される濃縮排水に含まれた不純物又は汚染物質の逆浸
透膜表面への付着を防止する必要がある。特に本発明の
ように、原水に河川水、湖沼水、海水、灌水等を用いる
ことまでをも考慮する場合は、全ての濾過器の汚染進行
が速く、特にコストの高い、逆浸透膜濾過器の逆浸透膜
寿命を延ばすことがランニングコストの低減に大きく寄
与することになる。[0012] In order to maximize the performance of the reverse osmosis membrane filter, impurities or contaminants contained in concentrated wastewater discharged from the reverse osmosis membrane generated as the filtration progresses adhere to the surface of the reverse osmosis membrane. Need to be prevented. In particular, as in the present invention, when considering the use of river water, lake water, seawater, irrigation, and the like as raw water, the progress of contamination of all filters is fast, and the cost of reverse osmosis membrane filters is particularly high. Extending the life of the reverse osmosis membrane greatly contributes to a reduction in running cost.
【0013】本発明者は、逆浸透膜寿命を延ばすため、
予め逆浸透膜濾過器に流入する通過水に磁界をかけ、磁
気処理することで、逆浸透膜表面に付着する不純物又は
汚染物質の付着を防止することを考えたのである。この
磁気処理手段に関しては、後に詳説することとする。The present inventor has proposed that to extend the life of a reverse osmosis membrane,
The inventor considered that a magnetic field was applied to the passing water flowing into the reverse osmosis membrane filter in advance to perform magnetic treatment, thereby preventing impurities or contaminants from adhering to the reverse osmosis membrane surface. The magnetic processing means will be described later in detail.
【0014】活性炭濾過器は、通過水の脱臭、脱色及び
汚染物質の吸着除去に用いるものであり、目的とする処
理能力に応じて、溶液に用いることのできる活性炭であ
れば、いずれの種類のものでも使用可能である。The activated carbon filter is used for deodorizing and decolorizing passing water and removing adsorbed contaminants, and any type of activated carbon that can be used in a solution according to the target processing capacity. Anything can be used.
【0015】このとき、イオン交換樹脂を充填した濾過
器であるイオン交換濾過器を活性炭の処理後に用いる
と、通過水中に残留した不純物イオンを効果的に除去す
ることが可能となる。At this time, if an ion exchange filter, which is a filter filled with an ion exchange resin, is used after the treatment of the activated carbon, it is possible to effectively remove the impurity ions remaining in the passing water.
【0016】本発明では、最終濾過として限外濾過器を
用いるのが好ましい。この限外濾過器は通過水中に混入
した微量な不純物、異物、細菌、有機汚染物等を最終的
に除去可能なものだからである。以上に述べた各種濾過
器により逐次処理され浄化水を得るのである。In the present invention, it is preferable to use an ultrafilter as the final filtration. This is because this ultrafilter can finally remove trace impurities, foreign substances, bacteria, organic contaminants and the like mixed in the passing water. Purified water is obtained by successively treating with the various filters described above.
【0017】そして、本発明に係る水の浄化処理装置に
磁気処理手段を備えることとしたのは、通過水を磁気処
理することで、原水に含まれた不純物及び汚染物質の浄
化処理装置の配管内部への付着軽減及び逆浸透膜濾過器
内で濾過が進むに従って発生する逆浸透膜から排出され
る濃縮排水に含まれた不純物及び汚染物質の逆浸透膜面
への付着を軽減することができるのである。The water purification apparatus according to the present invention is provided with the magnetic treatment means because the passing water is subjected to magnetic treatment to thereby remove impurities and pollutants contained in the raw water. It is possible to reduce the adhesion to the inside and the adhesion of impurities and contaminants contained in the concentrated wastewater discharged from the reverse osmosis membrane generated as the filtration proceeds in the reverse osmosis membrane filter to the reverse osmosis membrane surface. It is.
【0018】本発明でいう磁気処理手段は、配管の周囲
にいわゆる磁石を配置する方法、配管内の通過水中に磁
石を配置する方法又は配管周囲を通電コイルで取り囲み
通電して磁界をかける方法等種々の方法を採用すること
が可能である。中でも、ランニングコストの低減を考え
れば、磁石を利用することが望ましい。このとき使用す
る磁石としては、通常のフェライト系、スピノーダル型
に代表されるような合金系、希土類系等あらゆる磁石の
使用が可能である。必要となる磁力は、目的とする浄化
能力、流量、配管断面積等によって異なるが、種々の研
究を経た結果、本発明の予定した水の浄化装置では60
00ガウス以上の磁力があれば十分な磁気処理効果を得
ることができた。The magnetic processing means according to the present invention includes a method of arranging a so-called magnet around a pipe, a method of arranging a magnet in passing water in a pipe, and a method of enclosing a pipe around an energized coil and applying a magnetic field by energizing the pipe. Various methods can be adopted. Above all, it is desirable to use a magnet in consideration of reduction of running cost. As the magnet used at this time, any magnet such as a normal ferrite, an alloy represented by a spinodal type, and a rare earth magnet can be used. The required magnetic force varies depending on the desired purification capacity, flow rate, pipe cross-sectional area, etc., and as a result of various studies, the proposed water purification apparatus of the present invention has a magnetic force of 60%.
A sufficient magnetic processing effect could be obtained if the magnetic force was at least 00 Gauss.
【0019】磁気処理して磁化した水は、磁界を通過し
た後も一定時間の間は磁化された効果が保たれる。この
磁化された効果は以下の通りである。原水中に存在する
不純物や汚染物質は、水中でイオン状、分子、懸濁状等
で存在している。これらの表面と水の界面は、イオン吸
着層とその外側を取り巻くイオン拡散層とからなる二重
のイオン層により構成されている。このイオン吸着層と
イオン拡散層との電位差をゼータ電位といい、磁器処理
されるとこのゼータ電位が低下する現象が発生する。The magnetized water retains its magnetized effect for a certain period of time after passing through the magnetic field. This magnetized effect is as follows. Impurities and contaminants present in raw water exist in water in ionic, molecular, suspended, and the like. The interface between these surfaces and water is constituted by a double ion layer composed of an ion adsorption layer and an ion diffusion layer surrounding the ion adsorption layer. The potential difference between the ion-adsorbing layer and the ion-diffusion layer is called zeta potential, and a phenomena occurs in which the zeta potential decreases when subjected to porcelain treatment.
【0020】ゼータ電位の低下が起こると、配管内壁お
よび逆浸透膜表面と水との電位差が小さくなり、配管内
壁および逆浸透膜表面への吸着より、より大きなトータ
ル表面積をもつ水中に存在する固体粒子、分子等への吸
着が促進され、水中で結晶化が進行し、徐々に粗大化
し、不純物及び汚染物の沈殿物が形成されるまでにな
る。これらの沈殿物が形成されると言うことは不純物及
び汚染物の濾過器による除去が容易になると言うことを
意味し、しかも配管内壁および逆浸透膜表面への不純物
及び汚染物質の付着を有効に防止軽減することができる
こととなるのである。When the zeta potential decreases, the potential difference between the inner wall of the pipe and the surface of the reverse osmosis membrane and the water decreases, and the solid existing in the water having a larger total surface area than the adsorption on the inner wall of the pipe and the surface of the reverse osmosis membrane. Adsorption to particles, molecules, and the like is promoted, crystallization proceeds in water, and gradually coarsens, until precipitates of impurities and contaminants are formed. The fact that these precipitates are formed means that impurities and contaminants can be easily removed by a filter, and that the adhesion of impurities and contaminants to the inner wall of the pipe and the surface of the reverse osmosis membrane can be effectively performed. It can be prevented and reduced.
【0021】以上のことをもとに、本発明に係る水の浄
化処理装置において、磁気処理手段である磁気処理装置
を取り付ける位置を考えると、次のように考えられる。
不純物及び汚染物のスケールの付着防止を考慮すれば、
より取水口に近い位置に取り付ける方が良い。これに対
し、逆浸透膜の不純物及び汚染物のスケールの付着防止
を考慮すれば逆浸透膜濾過器により近い位置に取り付け
ることが望ましい。従って、装置によっては、単一の磁
気処理装置にとどまらず、複数の磁気処理装置を備えた
構造とすることで、単一の磁気処理装置とした場合に比
べ、より長く浄化処理装置の配管内部及び逆浸透膜を清
浄に保つことが可能となるのである。Based on the above, in the water purification treatment apparatus according to the present invention, the position where the magnetic treatment device as the magnetic treatment means is attached is considered as follows.
Considering the prevention of scale adhesion of impurities and contaminants,
It is better to install it closer to the intake. On the other hand, in consideration of the prevention of adhesion of impurities and contaminants on the reverse osmosis membrane, it is desirable to mount the filter at a position closer to the reverse osmosis membrane filter. Therefore, depending on the device, not only a single magnetic processing device but also a structure having a plurality of magnetic processing devices can be used to make the inside of the pipe of the purification processing device longer than a single magnetic processing device. In addition, the reverse osmosis membrane can be kept clean.
【0022】[0022]
【発明の実施の形態】以下、その具体的な実施形態を説
明することで、本発明に係る水の浄化処理装置を詳細に
説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, a specific embodiment of the present invention will be described, and the water purification apparatus according to the present invention will be described in detail.
【0023】第1実施形態 図1は第1実施形態にかか
る水の浄化処理装置1による水の浄化処理のフローを示
したものである。原水2の浄化処理は、原水2を図1の
左から右方に流す経路3を通り、その経路内に配置した
各種の濾過器により原水2の浄化を行なうのである。従
って、以下の説明も、その浄化処理経路の順に行なうも
のとする。 First Embodiment FIG. 1 shows a flow of water purification processing by a water purification apparatus 1 according to a first embodiment. In the purification process of the raw water 2, the raw water 2 passes through a path 3 through which the raw water 2 flows from left to right in FIG. 1, and the raw water 2 is purified by various filters disposed in the path. Therefore, the following description will be made in the order of the purification process.
【0024】取水口4にはストレーナー5が取り付けて
あり、原水2中の粗大ごみを除去した液を経路3にて取
水ポンプ6が取り込み、最初の浄化装置としての磁気処
理装置7に送り込む。今回は、原水2に海水を用い、磁
気処理装置7では6500ガウスの磁力を持つ希土類系
磁石を配管周囲に配する形のものを用いた。A strainer 5 is attached to the water intake port 4, and a liquid from which bulky debris has been removed from the raw water 2 is taken in by a water intake pump 6 through a path 3 and sent to a magnetic processing device 7 as a first purification device. In this case, seawater was used as the raw water 2, and the magnetic treatment device 7 used was a type in which a rare earth magnet having a magnetic force of 6,500 gauss was arranged around the piping.
【0025】磁気処理装置7を経た液は圧送ポンプ8で
適度の圧がかけられ、次の濾過器である高速濾過器9に
供給される。この高速濾過器9内には樹脂製濾材10が
充填してあり、この樹脂製濾過材10は塩化ビニリデン
からなるものであり、25ミクロン以上の粒径を持つ微
粒子の捕捉が可能なものである。The liquid that has passed through the magnetic processing device 7 is applied with an appropriate pressure by a pressure pump 8 and supplied to a high-speed filter 9 which is the next filter. The high-speed filter 9 is filled with a resin filter medium 10, which is made of vinylidene chloride and capable of capturing fine particles having a particle diameter of 25 microns or more. .
【0026】高速濾過器9の次には精密濾過器11が設
けてあり、これは、先の高速濾過器9を経た液中の5ミ
クロン以上の粒径を有する微粒子を除去するために用い
るものである。この精密濾過器11は次の高圧ポンプ1
2と逆浸透膜濾過器13を保護する役目も果たすもので
ある。Next to the high-speed filter 9, there is provided a microfilter 11, which is used to remove fine particles having a particle size of 5 microns or more in the liquid having passed through the high-speed filter 9. It is. This microfilter 11 is the next high pressure pump 1
2 and also serves to protect the reverse osmosis membrane filter 13.
【0027】高圧ポンプ12は浸透圧を超える圧力を付
加するためのものであり、精密高速濾過器9を経た液は
逆浸透膜濾過器13にて逆浸透膜モジュールを介し液中
のコロイド物質、溶解イオン物質、微生物や大腸菌その他
の一般細菌類ないしこれらの死骸(デブリ)、更にはパ
イロジェンを含む有機系不純物を除去した。ここで用い
た逆浸透膜にはスパイラル型を用いた。The high-pressure pump 12 is for applying a pressure exceeding the osmotic pressure. Dissolved ionic substances, microorganisms, Escherichia coli and other general bacteria, their dead bodies (debris), and organic impurities including pyrogen were removed. The spiral osmosis membrane used here was a spiral type.
【0028】逆浸透膜濾過器13の二次側には活性炭濾
過器14を設けた。その間の経路3には導電率センサー
15や自動三方弁16が配置してある。そして逆浸透膜
濾過器13を経た液(透過水)は活性炭濾過器14に導
かれ、活性炭フィルター17により有機物やグルカンそ
の他の汚染物質の吸着を行わせた。An activated carbon filter 14 was provided on the secondary side of the reverse osmosis membrane filter 13. A conductivity sensor 15 and an automatic three-way valve 16 are arranged in the path 3 between them. The liquid (permeated water) passed through the reverse osmosis membrane filter 13 was guided to the activated carbon filter 14, and the activated carbon filter 17 was used to adsorb organic substances, glucan, and other contaminants.
【0029】活性炭濾過器14の二次側には最後の浄化
装置として限外濾過器18が設けてある。ここでは最終
処理として、活性炭濾過器14を経た液中に残っている
可能性のある極微量な微粒子、コロイド物質、パイロジ
ェンその他の有機系不純物を除去するものである。On the secondary side of the activated carbon filter 14, an ultrafilter 18 is provided as a final purifier. Here, as a final treatment, a very small amount of fine particles, colloidal substances, pyrogens and other organic impurities which may remain in the liquid passed through the activated carbon filter 14 are removed.
【0030】限外濾過器18の二次側には、限外濾過器
18を経た浄化水を取り出すための取り出し口19、及
び洗浄排水経路20等を設けた。このようにして得られ
た、浄化水の性質は図4に示す通りである。また、磁気
処理装置7を備えていない場合は運転開始から約3月で
逆浸透膜の薬品洗浄が必要となるのに対し、本実施形態
では運転開始から約6月まで薬品洗浄を必要としなかっ
た。On the secondary side of the ultrafilter 18, a take-out port 19 for taking out purified water passed through the ultrafilter 18 and a washing / draining passage 20 are provided. The properties of the purified water thus obtained are as shown in FIG. When the magnetic treatment device 7 is not provided, chemical cleaning of the reverse osmosis membrane is required about three months from the start of operation, whereas in the present embodiment, chemical cleaning is not required until about six months from the start of operation. Was.
【0031】第2実施形態 次に図2を参照して第2実
施形態について説明する。この第2実施形態は先の第1
実施形態と重複するところがあるため、第1実施形態と
同様な部分については同一符号で示すことにより重複説
明を省略する。Second Embodiment Next, a second embodiment will be described with reference to FIG. This second embodiment is similar to the first embodiment.
Since there is some overlap with the first embodiment, the same parts as those in the first embodiment are denoted by the same reference numerals, and the duplicate description will be omitted.
【0032】第1実施形態と第2実施形態との違いは、
第1実施形態が単一の磁気処理装置を用いるのに対し、
第2実施形態では第1及び第2の2つの磁気処理装置
7,7’を用いる点にある。この第1磁気処理装置7
は、第1実施形態と同じ位置に配し、更に第2磁気処理
装置7’を保安フィルター濾過器11と高圧ポンプ12
の間に配した。このようにして、水の浄化を行うこと
で、逆浸透膜の薬品洗浄を必要とするまでの期間が約8
月程度に延びた。このようにして得られた、浄化水の性
質は図4に示す通りである。The difference between the first embodiment and the second embodiment is that
While the first embodiment uses a single magnetic processing device,
In the second embodiment, the first and second magnetic processing devices 7 and 7 'are used. This first magnetic processing device 7
Is disposed at the same position as the first embodiment, and furthermore, the second magnetic processing device 7 ′ is connected to the security filter 11 and the high-pressure pump 12.
Arranged between. By purifying the water in this way, the period before the chemical cleaning of the reverse osmosis membrane is required is about 8 hours.
It extended to about a month. The properties of the purified water thus obtained are as shown in FIG.
【0033】第3実施形態 更に図3を参照して第3実
施形態について説明する。この第3実施形態は先の第1
実施形態及び第2実施形態と重複するところがあるた
め、第1実施形態及び第2実施形態と同様な部分につい
ては同一符号で示すことにより重複説明を省略する。The third embodiment will be described with reference to the third embodiment further FIG. This third embodiment is similar to the first embodiment.
Since there are some overlaps with the embodiment and the second embodiment, the same parts as those in the first embodiment and the second embodiment are indicated by the same reference numerals, and the duplicate explanation is omitted.
【0034】この第3実施形態に係る水の浄化処理装置
は、第2実施形態に記載した水の浄化装置の構成に、イ
オン交換濾過器21を付加したものである。ここでは、
イオン交換濾過器21を、活性炭濾過器14と限外濾過
器18との間に配した。The water purification apparatus according to the third embodiment is obtained by adding an ion exchange filter 21 to the configuration of the water purification apparatus described in the second embodiment. here,
The ion exchange filter 21 was disposed between the activated carbon filter 14 and the ultrafilter 18.
【0035】このイオン交換濾過器21を用いること
で、通過水中に残留溶解している不純物イオンを、第1
実施形態及び第2実施形態で得られた浄化水に比べ、非
常に効率よく除去することができた。このようにして得
られた、浄化水の性質は図4に示す通りである。逆浸透
膜の薬品洗浄を必要とするまでの期間は第2実施形態と
同様約8月程度であった。By using the ion exchange filter 21, impurity ions remaining and dissolved in the passing water can be removed by the first method.
As compared with the purified water obtained in the embodiment and the second embodiment, the water could be removed very efficiently. The properties of the purified water thus obtained are as shown in FIG. The period until the chemical cleaning of the reverse osmosis membrane was required was about 8 months as in the second embodiment.
【0036】[0036]
【発明の効果】上述の通り、本発明に係る水の浄化処理
装置を用いると、有機系不純物や無機系不純物を完全に
除去でき、原水として水道水や井戸水よりも汚染度の高
い河川、湖沼、海水その他を選択しても、直接これらの
原水から意図する純度の高い医療用水として使用するこ
とも可能な浄化水を生成することができる。As described above, the use of the water purification apparatus according to the present invention makes it possible to completely remove organic impurities and inorganic impurities, and to use rivers, lakes and marshes that are more polluted than tap water or well water as raw water. Even if water, seawater, or the like is selected, purified water that can be used as medical water with high purity as intended from these raw waters can be generated directly.
【0037】更に、本発明に係る水の浄化処理装置の構
成を採用すると、従来の医療用水を製造する装置に比
べ、極めてコンパクトにすることが可能となる。従っ
て、トラックその他の移動体に搭載でき、被災地へこの
水の浄化装置を運搬して現地で河川、湖沼、海水等から
医療用水を直接得ることが可能となり、医療活動を円滑
にするものとなる。Further, when the configuration of the water purification treatment apparatus according to the present invention is adopted, it becomes possible to make the apparatus extremely compact as compared with a conventional apparatus for producing medical water. Therefore, it can be mounted on trucks and other moving objects, and it is possible to transport this water purification device to the stricken area and directly obtain medical water from rivers, lakes, marshes, seawater, etc., and facilitate medical activities. Become.
【図1】水の浄化処理装置の浄化フローの概念図。FIG. 1 is a conceptual diagram of a purification flow of a water purification treatment device.
【図2】水の浄化処理装置の浄化フローの概念図。FIG. 2 is a conceptual diagram of a purification flow of a water purification treatment device.
【図3】水の浄化処理装置の浄化フローの概念図。FIG. 3 is a conceptual diagram of a purification flow of a water purification treatment device.
【図4】原水(海水)、浄化水、透析用水水質基準値と
の比較一覧表。FIG. 4 is a comparison list of raw water (seawater), purified water, and dialysis water quality standard values.
2原水 3経路 7磁気処理装置 9高速濾過器 13逆浸透膜濾過器 14活性炭濾過器 18限外濾過器 21イオン交換濾過器 2 Raw water 3 paths 7 Magnetic treatment device 9 High speed filter 13 Reverse osmosis membrane filter 14 Activated carbon filter 18 Ultrafilter 21 Ion exchange filter
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 9/00 502 C02F 9/00 502L 503 503B 504 504B B01D 61/04 B01D 61/04 61/16 61/16 65/08 65/08 C02F 1/00 C02F 1/00 U 1/48 1/48 A ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 9/00 502 C02F 9/00 502L 503 503B 504 504B B01D 61/04 B01D 61/04 61/16 61/16 65/08 65 / 08 C02F 1/00 C02F 1/00 U 1/48 1/48 A
Claims (4)
きる浄化水を直接得ることのできる水の浄化処理装置で
あって、複数の濾過手段である粗濾過器、精密濾過器、
逆浸透膜濾過器、活性炭濾過器、限外濾過器と各種ポン
プとを連結配管してなるものであり、原水の取水口から
浄化水の取り出し口に到るまでの全浄化経路の内、取水
口から逆浸透膜濾過器に到るまでの配管経路に1以上の
磁気処理手段を備え、その磁気処理手段により逆浸透膜
濾過器に流入する前の通過水に予め磁界をかけ磁気処理
することをことを特徴とする水の浄化処理装置。An apparatus for purifying water that can directly obtain purified water that can be used as medical water from raw water, comprising a plurality of filtration means, a coarse filter, a fine filter,
It consists of a reverse osmosis membrane filter, activated carbon filter, ultrafilter and various pumps connected and connected, and the water is taken out of the entire purification path from the raw water intake to the purified water intake. The pipe route from the mouth to the reverse osmosis membrane filter is provided with one or more magnetic processing means, and the magnetic processing means applies a magnetic field to the passing water before flowing into the reverse osmosis membrane filter to perform magnetic processing. A water purification treatment device characterized by the above-mentioned.
た原水を磁気処理するための磁気処理手段である磁気処
理装置と、その磁気処理装置の二次側に原水に含まれる
比較的大きな異物を除去するための粗濾過器を圧送ポン
プを介在させ設け、その粗濾過器の二次側に通過水中の
ミクロ粒子を除去するための精密濾過器を設け、その精
密濾過器の二次側に通過水中の不純物及び汚染物を除去
するための逆浸透膜濾過器を高圧ポンプを介在させ設
け、その逆浸透膜濾過器の二次側に通過水中の有機系不
純物及び有機系汚染物を吸着除去するための活性炭濾過
器を設け、その活性炭濾過器の二次側に最終濾過を行う
ものである限外濾過器を設け、そしてこの限外濾過器か
ら浄化水を取り出すための取り出し口とから成る請求項
1記載の水の浄化処理装置。2. A magnetic processing apparatus as a magnetic processing means for magnetically processing raw water collected by an intake pump from an intake port on a primary side, and a relatively large foreign substance contained in the raw water on a secondary side of the magnetic processing apparatus. A coarse filter for removing fine particles is provided with a pressure pump interposed, and a fine filter for removing microparticles in the passing water is provided on the secondary side of the coarse filter, and on the secondary side of the fine filter. A reverse osmosis membrane filter for removing impurities and contaminants in passing water is installed with a high-pressure pump interposed, and organic impurities and organic contaminants in the passing water are adsorbed and removed on the secondary side of the reverse osmosis membrane filter. And an ultrafiltration device for performing final filtration on the secondary side of the activated carbon filtration device, and an outlet for removing purified water from the ultrafiltration device. The water purification treatment according to claim 1. apparatus.
た原水を磁気処理するための磁気処理手段である第一磁
気処理装置と、その第一磁気処理装置の二次側に原水に
含まれる比較的大きな異物を除去するための粗濾過器を
圧送ポンプを介在させ設け、その粗濾過器又は高速濾過
器の二次側に通過水中のミクロ粒子を除去するための精
密濾過器を設け、その精密濾過器の二次側に通過水を更
に磁気処理するための磁気処理手段である第二磁気処理
装置を設け、第二磁気処理装置の二次側に通過水中の不
純物及び汚染物を除去するための逆浸透膜濾過器を高圧
ポンプを介在させ設け、その逆浸透膜濾過器の二次側に
通過水中の有機系不純物及び有機系汚染物を吸着除去す
るための活性炭濾過器を設け、その活性炭濾過器の二次
側に最終濾過を行うものである限外濾過器と、そしてこ
の限外濾過器から浄化水を取り出すための取り出し口と
から成る請求項1に記載の水の浄化処理装置。3. A first magnetic treatment apparatus which is a magnetic treatment means for magnetically treating raw water collected by a water intake pump from an intake port on a primary side, and raw water is included on a secondary side of the first magnetic treatment apparatus. A coarse filter for removing relatively large foreign matter is provided with a pressure pump interposed, and a fine filter for removing microparticles in passing water is provided on the secondary side of the coarse filter or the high-speed filter. A second magnetic treatment device, which is a magnetic treatment means for further magnetically treating the passing water, is provided on the secondary side of the microfilter, and impurities and contaminants in the passing water are removed on the secondary side of the second magnetic treatment device. A reverse osmosis membrane filter is provided with a high-pressure pump interposed, and an activated carbon filter for adsorbing and removing organic impurities and organic contaminants in the passing water is provided on the secondary side of the reverse osmosis membrane filter. Perform the final filtration on the secondary side of the activated carbon filter The water purification treatment device according to claim 1, comprising an ultrafiltration device, and an outlet for removing purified water from the ultrafiltration device.
る限外濾過器との間の配管経路にイオン交換樹脂を充填
した濾過器であるイオン交換濾過器を配してなる請求項
2または請求項3に記載の水の浄化処理装置。4. An ion-exchange filter, which is a filter filled with an ion-exchange resin, is disposed in a piping path between the activated carbon filter and an ultrafilter that performs final filtration. The water purification treatment device according to claim 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10016059A JPH11207391A (en) | 1998-01-28 | 1998-01-28 | Water purifying and treatment device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10016059A JPH11207391A (en) | 1998-01-28 | 1998-01-28 | Water purifying and treatment device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11207391A true JPH11207391A (en) | 1999-08-03 |
Family
ID=11906011
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10016059A Pending JPH11207391A (en) | 1998-01-28 | 1998-01-28 | Water purifying and treatment device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11207391A (en) |
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JP2005095812A (en) * | 2003-09-26 | 2005-04-14 | Daicen Membrane Systems Ltd | Water purifying device and water purifying method |
EP1801078A1 (en) * | 2005-12-23 | 2007-06-27 | Enia S.P.A. | Apparatus for purification treatment of drinking water and process therefor |
WO2007072127A1 (en) * | 2005-12-23 | 2007-06-28 | Enia Spa | Apparatus for purification treatment of drinking water and process therefor |
CN104529041A (en) * | 2014-11-20 | 2015-04-22 | 成都市飞龙水处理技术研究所 | Ultrafiltration membrane water purifier with magnetizing mineralizing functions, and preparation method thereof |
CN104445692A (en) * | 2014-11-27 | 2015-03-25 | 新疆德蓝股份有限公司 | Method for purifying bitter salty water into micro salt-containing water |
JP2016155098A (en) * | 2015-02-25 | 2016-09-01 | 三菱化学株式会社 | Separation membrane module |
CN106186507A (en) * | 2016-08-27 | 2016-12-07 | 郑光茂 | Large purification machine |
CN111995091A (en) * | 2020-08-24 | 2020-11-27 | 泉州三江源饮品科技有限公司 | Production process system for barreled purified water |
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