JP2005238187A - Water purification cartridge, method for manufacturing the same, and water purifier comprising water purification cartridge - Google Patents

Water purification cartridge, method for manufacturing the same, and water purifier comprising water purification cartridge Download PDF

Info

Publication number
JP2005238187A
JP2005238187A JP2004055063A JP2004055063A JP2005238187A JP 2005238187 A JP2005238187 A JP 2005238187A JP 2004055063 A JP2004055063 A JP 2004055063A JP 2004055063 A JP2004055063 A JP 2004055063A JP 2005238187 A JP2005238187 A JP 2005238187A
Authority
JP
Japan
Prior art keywords
filter medium
water
purification cartridge
water purification
fibrous filter
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.)
Granted
Application number
JP2004055063A
Other languages
Japanese (ja)
Other versions
JP4255070B2 (en
Inventor
Masanori Ito
正則 伊藤
Masahiko Taneike
昌彦 種池
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 Rayon Co Ltd
Original Assignee
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 Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP2004055063A priority Critical patent/JP4255070B2/en
Publication of JP2005238187A publication Critical patent/JP2005238187A/en
Application granted granted Critical
Publication of JP4255070B2 publication Critical patent/JP4255070B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Water Treatment By Sorption (AREA)
  • Filtering Materials (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a water purification cartridge, which has a high level of water filtration performance and, at the same time, has low resistance to water permeation, and is less likely to cause clogging, and to provide a method for manufacturing the water purification cartridge and a water purifier comprising the water purification cartridge. <P>SOLUTION: In this water purification cartridge, a fibrous filter medium comprising fibers arranged in a central axis direction of a cylindrical vessel and having a fibrous filter medium thickness in the central axis direction of not less than 3 mm and less than 10 mm is disposed within a cylindrical vessel. This water purification cartridge has excellent performance, that is, has a high level of filtration performance and is less likely to cause clogging. The water purification cartridge having the above excellent performance can be manufactured by packing the fibrous filter medium in the cylindrical vessel in such a manner that the fibrous filter medium is compressed in a compression ratio of 0.1 to 5% in the radial direction of the cylindrical vessel. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、浄水性能に優れた浄水カートリッジとその製造方法、及びこれを備えた浄水器に関する。   The present invention relates to a water purification cartridge excellent in water purification performance, a method for producing the same, and a water purifier equipped with the same.

水道水中の塩素やカビ臭等、水の味を損なう物質や、鉛等の重金属や、トリハロメタン、農薬等の有害物質を除去するための浄水器が知られている。これらの物質を除去するための濾材としては、従来より活性炭等の吸着剤が広く用いられている。   Water purifiers are known for removing substances that impair the taste of water such as chlorine and musty odors in tap water, heavy metals such as lead, and harmful substances such as trihalomethanes and agricultural chemicals. Conventionally, adsorbents such as activated carbon have been widely used as filter media for removing these substances.

吸着剤は、粒状のものが用いられる場合が多いが、吸着剤の性能はその比表面積が大きいほど優れているため、その形状を繊維状とした濾材を用いた浄水器が知られている(例えば特許文献1参照)。   Adsorbents are often used in the form of granules, but the performance of the adsorbent is better as the specific surface area is larger, so a water purifier using a filter medium whose shape is fibrous is known ( For example, see Patent Document 1).

しかしながら繊維状濾材はかさ密度が大きいため、圧縮して使用しないと容積効率が悪くなる一方で、圧縮して使用すると水の通過に対する抵抗が大きくなり、かつ繊維が絡み合った部位に懸濁物が捕捉され、目詰まりし易くなりがちであった。
特開2002−177951号公報
However, since the fibrous filter medium has a high bulk density, the volumetric efficiency becomes poor if it is not used after being compressed. On the other hand, if it is used after being compressed, the resistance to the passage of water is increased, and the suspension is formed at the site where the fibers are entangled. It was likely to be trapped and easily clogged.
JP 2002-177951 A

本発明は、高い濾過性能を有すると共に、水の通過に対する抵抗が小さく、かつ目詰まりし難い浄水カートリッジとその製造方法、並びにこの浄水カートリッジを備えた浄水器を提供することを目的とする。   An object of the present invention is to provide a water purification cartridge having high filtration performance, low resistance to passage of water, and hardly clogging, a method for producing the same, and a water purifier provided with the water purification cartridge.

すなわち本発明の第一の要旨は、筒状容器の中心軸方向に繊維が配向し、かつその方向の厚みが3mm以上10mm未満である繊維状濾材が筒状容器の内部に配された浄水カートリッジである。   That is, the first gist of the present invention is a water purification cartridge in which fibers are oriented in the central axis direction of a cylindrical container, and a fibrous filter medium having a thickness in the direction of 3 mm or more and less than 10 mm is arranged inside the cylindrical container. It is.

本発明の第二の要旨は、筒状容器の中心軸方向に繊維を配向させ、かつその方向の厚みを3mm以上10mm未満とした繊維状濾材を、該筒状容器の径方向に0.1〜5%の圧縮率で圧縮して、該筒状容器の内部に充填する浄水カートリッジの製造方法である。   The second gist of the present invention is that a fibrous filter medium in which fibers are oriented in the central axis direction of the cylindrical container and the thickness in the direction is 3 mm or more and less than 10 mm is 0.1 in the radial direction of the cylindrical container. A method for producing a water purification cartridge that compresses at a compression rate of ˜5% and fills the inside of the cylindrical container.

本発明の第三の要旨は、上記浄水カートリッジが着脱可能に接続された浄水器である。   The third gist of the present invention is a water purifier to which the water purification cartridge is detachably connected.

本発明の浄水カートリッジ及びこれを備えた浄水器によれば、筒状容器の中心軸方向に繊維が配向し、かつその方向の厚みが3mm以上10mm未満である繊維状濾材を用いているので、除去したい物質の除去能力を向上させることができることに加えて、繊維状濾材の部位の水通過に対する抵抗を小さくし、かつ目詰まりすることを防止することができる。   According to the water purification cartridge of the present invention and the water purifier provided with the same, since the fibers are oriented in the central axis direction of the cylindrical container and the thickness of the direction is 3 mm or more and less than 10 mm, the fibrous filter medium is used. In addition to improving the ability to remove a substance to be removed, the resistance of the fibrous filter medium to water passage can be reduced, and clogging can be prevented.

本発明の浄水カートリッジの製造方法によれば、筒状容器の中心軸方向に繊維を配向させ、かつその方向の厚みを3mm以上10mm未満とした繊維状濾材を、筒状容器の径方向に0.1〜5%の圧縮率で圧縮して、筒状容器の内部に充填するので、繊維状濾材の水通過に対する抵抗を過度に増加させること無く、かつ目詰まりしにくい状態とすることができる。   According to the method for producing a water purification cartridge of the present invention, a fibrous filter medium in which fibers are oriented in the central axis direction of the cylindrical container and the thickness in the direction is 3 mm or more and less than 10 mm is reduced to 0 in the radial direction of the cylindrical container. Compressed at a compression ratio of 1 to 5% and filled into the cylindrical container, so that the resistance to water passage of the fibrous filter medium is not excessively increased and it is difficult to clog. .

以下、本発明の実施の形態を説明する。
図1は本発明の浄水カートリッジの一例を表す模式図である。
Embodiments of the present invention will be described below.
FIG. 1 is a schematic view showing an example of the water purification cartridge of the present invention.

浄水カートリッジ1は、筒状容器2の内部に、繊維状濾材3が充填されて構成される。本発明においては、繊維状濾材3は、筒状容器の中心軸方向に繊維を配向させ、かつその方向の厚みを3mm以上10mm未満としている。浄水カートリッジ1において、水は筒状容器の中心軸方向に流れる。   The water purification cartridge 1 is configured by filling a fibrous filter medium 3 inside a cylindrical container 2. In the present invention, the fibrous filter medium 3 has fibers oriented in the central axis direction of the cylindrical container, and the thickness in that direction is 3 mm or more and less than 10 mm. In the water purification cartridge 1, water flows in the direction of the central axis of the cylindrical container.

筒状容器の中心軸方向に繊維状濾材3の繊維を配向させるとは、繊維状濾材3を構成する繊維の繊維軸方向を、概ね筒状容器の中心軸方向となるように配することをいう。このとき、全ての繊維の繊維軸が、完全に筒状容器の中心軸方向を向くように配される必要は必ずしも無く、一部の繊維の繊維軸が筒状容器の中心軸方向に交差するように配されていてもよい。   To orient the fibers of the fibrous filter medium 3 in the direction of the central axis of the cylindrical container means that the fiber axis direction of the fibers constituting the fibrous filter medium 3 is approximately aligned with the central axis direction of the cylindrical container. Say. At this time, it is not always necessary that the fiber axes of all the fibers are completely oriented in the central axis direction of the cylindrical container, and the fiber axes of some of the fibers intersect the central axis direction of the cylindrical container. It may be arranged as follows.

繊維状濾材において、繊維同士が三次元的にランダムに絡み合っている場合、水通過方向の特定の面において、繊維同士が交差する点が多数存在するため、この面において水中の件濁物質が捕捉され易くなり、懸濁物質の堆積による目詰まりが起こりやすい。   In a fibrous filter medium, when fibers are randomly entangled three-dimensionally, there are many points where the fibers cross each other on a specific surface in the direction of water passage. And clogging due to the accumulation of suspended matter is likely to occur.

一方、本発明のように筒状容器の中心軸方向に繊維を配向させると、水通過方向の特定の面において、繊維同士が交差する点が少ないため、懸濁物質が面で捕捉されることがなくなり、目詰まりが起こり難くなると共に、水通過に対する抵抗も減らすことができる。   On the other hand, when the fibers are oriented in the direction of the central axis of the cylindrical container as in the present invention, there are few points where the fibers cross each other on a specific surface in the water passage direction, so that suspended substances are captured by the surface The clogging is less likely to occur, and the resistance to water passage can be reduced.

筒状容器の中心軸方向における本発明の繊維状濾材3の厚みは、薄すぎると水と濾材との十分な接触時間を確保できないため、濾過性能が不十分となる場合がある。また、厚みが厚すぎると、水通過に対する抵抗が大きくなって、水道の圧力が低い場所では濾過流量を確保できなくなる場合がある。   If the thickness of the fibrous filter medium 3 of the present invention in the direction of the central axis of the cylindrical container is too thin, sufficient contact time between water and the filter medium cannot be secured, and thus the filtration performance may be insufficient. On the other hand, if the thickness is too thick, resistance to water passage increases, and the filtration flow rate may not be ensured in a place where the water pressure is low.

従って繊維状濾材3の厚みは、3mm以上10mm未満とする必要があり、5〜9.7mmとすることが好ましく、6〜9mmとすることがより好ましく、7〜8mmとすることが更に好ましい。   Therefore, the thickness of the fibrous filter medium 3 needs to be 3 mm or more and less than 10 mm, preferably 5 to 9.7 mm, more preferably 6 to 9 mm, and still more preferably 7 to 8 mm.

繊維状濾材3の種類は、除去したい物質の種類に応じて設定すればよく、例えば繊維状活性炭、イオン交換繊維、キレート繊維等を用いることができる。中でも、鉛等の重金属を除去対象とする場合、イオン交換繊維を用いると、一般的な粒径の粒状イオン交換樹脂を用いる場合と比較して、単位体積あたりの除去性能を向上させることができるため好ましい。   The type of the fibrous filter medium 3 may be set according to the type of substance to be removed. For example, fibrous activated carbon, ion exchange fiber, chelate fiber, or the like can be used. In particular, when heavy metals such as lead are to be removed, the use of ion exchange fibers can improve removal performance per unit volume compared to the case of using a granular ion exchange resin having a general particle size. Therefore, it is preferable.

繊維状濾材3は、複数の繊維状濾材を混合して使用しても構わない。例えば、イオン交換繊維と繊維状活性炭とを混合した繊維状濾材3を用いると、重金属の除去性能に優れ、かつトリハロメタンや農薬等の除去性能も向上させた浄水カートリッジとすることができる。混合比率はその除去対象や、それぞれの除去能力に応じて決めればよいが、イオン交換繊維:繊維状活性炭の質量比率として、30:50〜50:30とすると、それぞれの除去能力のバランスがよくなるため好ましい。   The fibrous filter medium 3 may be used by mixing a plurality of fibrous filter media. For example, when a fibrous filter medium 3 in which ion exchange fibers and fibrous activated carbon are mixed is used, a water purification cartridge having excellent heavy metal removal performance and improved removal performance of trihalomethane, agricultural chemicals and the like can be obtained. The mixing ratio may be determined according to the object to be removed and the respective removal capacities, but when the mass ratio of ion exchange fiber: fibrous activated carbon is 30:50 to 50:30, the balance of the respective removal capacities is improved. Therefore, it is preferable.

繊維状濾材3の繊維軸の方向を配向させ、かつ前述の厚みとするには、繊維状濾材3を成型体としてから、これを筒状容器2に充填するようにすると、取扱い性が向上するため好ましい。成形方法は、例えば濾材の繊維に熱融着繊維をバインダーとして混合させて、その後加熱する方法によって、成型体を得ることができる。   In order to orient the direction of the fiber axis of the fibrous filter medium 3 and to have the above-described thickness, the handleability is improved when the fibrous filter medium 3 is formed into a molded body and then filled into the cylindrical container 2. Therefore, it is preferable. As the molding method, for example, a molded body can be obtained by a method in which a heat-sealing fiber is mixed as a binder with fibers of a filter medium and then heated.

成型体の形状は、筒状容器2の形状に合わせて円盤状とすることが好ましいが、その他ドーナツ状等の形状とすることもできる。   The shape of the molded body is preferably a disc shape in accordance with the shape of the cylindrical container 2, but may be other shapes such as a donut shape.

浄水カートリッジ1には、図1に示すように、繊維状濾材3の他に、粒状濾材4を充填することもできる。このように繊維状濾材3と粒状濾材4とを併用すると、除去したい物質に応じて様々な種類の濾材を充填することができるため好ましい。   As shown in FIG. 1, the water purification cartridge 1 can be filled with a granular filter medium 4 in addition to the fibrous filter medium 3. Thus, it is preferable to use the fibrous filter medium 3 and the granular filter medium 4 together because various types of filter medium can be filled in accordance with the substance to be removed.

粒状濾材4の種類は特に限定されず、粉末状活性炭、粒状活性炭、分子吸着樹脂、ゼオライト、モレキュラーシーブ、キレート樹脂、イオン交換樹脂、亜硫酸カルシウム、コーラルサンド、麦飯石、医王石、トルマリンなどを使用することができる。また、これらのうちの2種以上を用いることもできる。
粒状濾材4は、除去可能な物質が多いことから、粒状活性炭が好ましい。
The type of the particulate filter medium 4 is not particularly limited, and powdered activated carbon, granular activated carbon, molecular adsorption resin, zeolite, molecular sieve, chelate resin, ion exchange resin, calcium sulfite, coral sand, barleystone, Ioishi stone, tourmaline, etc. are used. can do. Two or more of these can also be used.
The granular filter medium 4 is preferably granular activated carbon because many substances can be removed.

繊維状濾材3と粒状濾材4とを併用する場合、それぞれの除去性能の観点だけから充填量を決定すると、圧力損失が増大して通水困難になる可能性があるため、通水抵抗を適宜調節することが好ましい。   When the fibrous filter medium 3 and the granular filter medium 4 are used in combination, if the filling amount is determined only from the viewpoint of the respective removal performances, there is a possibility that the pressure loss increases and water flow becomes difficult. It is preferable to adjust.

繊維状濾材3と粒状濾材4の通水抵抗としては、繊維状濾材3の通水抵抗を1としたとき、粒状濾材4の通水抵抗が5〜70となるように設定すると、各濾材の除去能力のバランスと全体の圧力損失が好ましい範囲となる。また、繊維状濾材3の通水抵抗を1としたとき、粒状濾材4の通水抵抗が10〜50となるように設定するとより好ましく、繊維状濾材3の通水抵抗を1としたとき、粒状濾材4の通水抵抗が20〜40となるように設定するとさらに好ましい。   As the water flow resistance of the fibrous filter medium 3 and the granular filter medium 4, when the water flow resistance of the fibrous filter medium 3 is set to 1, the flow resistance of the granular filter medium 4 is set to 5 to 70. The balance of removal capability and the overall pressure loss are in the preferred range. Moreover, when the water flow resistance of the fibrous filter medium 3 is 1, it is more preferable to set the water flow resistance of the granular filter medium 4 to be 10-50, and when the water resistance of the fibrous filter medium 3 is 1, More preferably, the water resistance of the granular filter medium 4 is set to 20 to 40.

また、繊維状濾材3が占める体積あたりの質量は、0.1〜0.25g/cmとすると、除去能力と圧力損失のバランスが良くなるため好ましく、0.16〜0.22g/cmとすることがより好ましい。 The mass per volume occupied by the fibrous filter medium 3, when the 0.1~0.25g / cm 3, preferably the balance is improved removal capability and the pressure loss, 0.16~0.22g / cm 3 More preferably.

粒状濾材4が占める体積あたりの質量は、0.45〜0.65g/cmとすると、除去能力と圧力損失のバランスが良くなるため好ましく、0.50〜0.58g/cmとすることがより好ましい。
また、粒状濾材4の粒径は、120μm〜1300μmが好ましく、150μm〜450μmがより好ましい。
Mass per volume particulate filter medium 4 is occupied, when 0.45~0.65g / cm 3, preferably the balance is improved removal capability and the pressure loss, be 0.50~0.58g / cm 3 Is more preferable.
Moreover, the particle size of the granular filter medium 4 is preferably 120 μm to 1300 μm, and more preferably 150 μm to 450 μm.

筒状容器2へ繊維状濾材3を充填するにあたっては、筒状容器2の中心軸方向に繊維を配向させ、かつその方向の厚みを3mm以上10mm未満とした繊維状濾材3を、筒状容器2の径方向に0.1〜5%の圧縮率で圧縮してから、繊維状濾材3を筒状容器2の内部に挿入することによって充填を行う。   When the fibrous filter medium 3 is filled into the cylindrical container 2, the fibrous filter medium 3 in which the fibers are oriented in the central axis direction of the cylindrical container 2 and the thickness in the direction is 3 mm or more and less than 10 mm is used. After compressing in the radial direction of 2 at a compression rate of 0.1 to 5%, the fibrous filter medium 3 is filled into the cylindrical container 2 by filling.

なお、ここでいう圧縮率とは、繊維状濾材3を圧縮する前の自然な状態における筒状容器2の径方向の長さに対する、繊維状濾材3を圧縮することによって、筒状容器2の径方向に収縮した長さの割合をいう。   The compression rate referred to here is the compression of the fibrous filter medium 3 by compressing the fibrous filter medium 3 with respect to the radial length of the cylindrical container 2 in a natural state before the fibrous filter medium 3 is compressed. The ratio of the length contracted in the radial direction.

圧縮率を0.1〜5%とすることにより、繊維状濾材3の外周部と筒状容器2の内壁との間に隙間が発生することを防止し、かつ繊維状濾材3の水通過に対する抵抗の上昇を防止することができる。
圧縮率は1〜3%とするとより好ましい。
By setting the compression rate to 0.1 to 5%, it is possible to prevent a gap from being generated between the outer peripheral portion of the fibrous filter medium 3 and the inner wall of the cylindrical container 2, and to the water passage of the fibrous filter medium 3 An increase in resistance can be prevented.
The compression ratio is more preferably 1 to 3%.

粒状濾材4を併用する場合、まず粒状濾材4を筒状容器に充填し、その後で繊維状濾材3を充填し、さらに繊維状濾材3に対し、10〜300Nの力を筒状容器2の中心軸方向に印加すると、粒状濾材4の充填空間に隙間が発生し、この隙間によって水がショートパスして濾材性能が低下することを防止できるため好ましい。
繊維状濾材3に対し印加する力は、50〜200Nがより好ましく、75〜150Nが更に好ましい。
When the granular filter medium 4 is used in combination, first, the granular filter medium 4 is filled in the cylindrical container, and then the fibrous filter medium 3 is filled. Further, a force of 10 to 300 N is applied to the fibrous filter medium 3 in the center of the cylindrical container 2. When applied in the axial direction, it is preferable because a gap is generated in the filling space of the granular filter medium 4, and water can be prevented from short-passing through the gap to reduce the filter medium performance.
The force applied to the fibrous filter medium 3 is more preferably 50 to 200N, and even more preferably 75 to 150N.

粒状濾材4の充填は、筒状容器2を振動させながら行うと、充填密度を上げることができるため好ましい。   It is preferable to fill the granular filter medium 4 while vibrating the cylindrical container 2 because the packing density can be increased.

粒状濾材4を用いる場合は、メッシュや焼結体等、粒状濾材4の通過を防止できる仕切り部材5を筒状容器2内に配し、粒状濾材4の漏れを防止することが好ましい。   When the granular filter medium 4 is used, it is preferable that a partition member 5 that can prevent passage of the granular filter medium 4 such as a mesh or a sintered body is disposed in the cylindrical container 2 to prevent leakage of the granular filter medium 4.

なお、粒状濾材4と繊維状濾材3との間に仕切り部材を配置することもできるが、繊維状濾材3が粒状濾材4の漏れを防止できるので、図1に示すように、粒状濾材4と繊維状濾材3との間に仕切り部材を配置しなくてもよい。   In addition, although a partition member can also be arrange | positioned between the granular filter medium 4 and the fibrous filter medium 3, since the fibrous filter medium 3 can prevent the granular filter medium 4 from leaking, as shown in FIG. It is not necessary to arrange a partition member between the fibrous filter medium 3.

図1に示すように、筒状容器2の水が流入する側の端部には、繊維状濾材3が配されているので、筒状容器2からそれぞれの濾材が漏れることはないが、筒状容器2の端部にさらに仕切り部材6を配置してもよい。この仕切り部材6は、あまり通水抵抗が大きいと好ましくないため、繊維状濾材3の通水抵抗を1としたとき、仕切り部材6の通水抵抗が0.2〜0.75となるように設定することが好ましい。   As shown in FIG. 1, since the fibrous filter medium 3 is arranged at the end of the cylindrical container 2 on the water inflow side, each filter medium does not leak from the cylindrical container 2. A partition member 6 may be further arranged at the end of the container 2. Since this partition member 6 is not preferable if the water flow resistance is too large, when the water flow resistance of the fibrous filter medium 3 is 1, the water flow resistance of the partition member 6 is 0.2 to 0.75. It is preferable to set.

また、図1に示すように、浄水カートリッジ1には、中空糸膜7を配すると、細菌等も除去できるため好ましい。中空糸膜7の素材としては特に制限はないが、セルロース系、ポリオレフィン(ポリエチレン、ポリプロピレン)系、ポリビニリデンフロライド(PVDF)、ポリビニルアルコール系、エチレン・ビニルアルコール共重合体、ポリエーテル系、ポリメタクリル酸メチル(PMMA)系、ポリスルフォン系、ポリアクリロニトリル系、ポリ四弗化エチレン(PTFE)系、ポリカーボネイト系、ポリエステル系、ポリアミド系、芳香族ポリアミド系等の各種材料が挙げられる。   Moreover, as shown in FIG. 1, it is preferable to arrange a hollow fiber membrane 7 in the water purification cartridge 1 because bacteria and the like can be removed. The material of the hollow fiber membrane 7 is not particularly limited, but is cellulose, polyolefin (polyethylene, polypropylene), polyvinylidene fluoride (PVDF), polyvinyl alcohol, ethylene / vinyl alcohol copolymer, polyether, poly Examples include various materials such as methyl methacrylate (PMMA), polysulfone, polyacrylonitrile, polytetrafluoroethylene (PTFE), polycarbonate, polyester, polyamide, and aromatic polyamide.

図2は、本発明の浄水カートリッジ1が着脱可能に接続された浄水器の一例を示す模式的断面図である。
この浄水器は、水道の蛇口と接続する蛇口取付部10を有する流路切換部9と浄水カートリッジ1を収納するカートリッジ収納筒体部8とから構成されている。
水道水は、蛇口取付部10で水道の蛇口と連結されることにより原水受入口11から流路切換部9内部に導入される。導入された水道水は流路切換レバー13の操作により、水道水を浄化せずにそのまま吐出する原水吐出口(図示せず)と、カートリッジ収納筒体部8と接続してカートリッジ収納筒体部へ原水を送る原水送水部12とに、選択的に切り換えられ送水される。
原水送水部より送られた水道水は、収納筒体部8内部に導入され、仕切り部材6から浄水カートリッジ1内部に流入する。
浄水カートリッジ1内部に流入した水道水は、繊維状濾材3、粒状濾材4、中空糸膜7を順に通過し濾過され、浄水として浄水吐出口13より吐出される。
FIG. 2 is a schematic cross-sectional view showing an example of a water purifier to which the water purification cartridge 1 of the present invention is detachably connected.
This water purifier is composed of a flow path switching unit 9 having a faucet mounting portion 10 connected to a faucet of a water supply and a cartridge housing cylinder portion 8 for housing the water purification cartridge 1.
The tap water is introduced from the raw water receiving port 11 into the flow path switching unit 9 by being connected to the tap of the tap at the tap mounting portion 10. The introduced tap water is connected to a raw water discharge port (not shown) for discharging tap water as it is without purifying it by operating the flow path switching lever 13 and the cartridge storage cylinder portion 8 to connect the cartridge storage cylinder portion. The water is selectively switched to the raw water supply section 12 that sends the raw water to the water.
The tap water sent from the raw water feed section is introduced into the storage cylinder section 8 and flows into the clean water cartridge 1 from the partition member 6.
The tap water that has flowed into the water purification cartridge 1 passes through the fibrous filter medium 3, the granular filter medium 4, and the hollow fiber membrane 7 in order, is filtered, and is discharged from the purified water discharge port 13 as purified water.

本発明の実施例の一例として蛇口直結型浄水器の態様について説明したが、カートリッジ収納筒体部を流しの天板等に置く据置形浄水器や、浄水カートリッジを流し台下に配設するアンダーシンク型浄水器であってもよい。   The embodiment of the faucet direct connection type water purifier has been described as an example of the embodiment of the present invention. A type water purifier may be used.

本発明の浄水カートリッジの一例を示す模式的断面図である。It is typical sectional drawing which shows an example of the water purification cartridge of this invention. 本発明の浄水器の一例を示す模式図である。It is a schematic diagram which shows an example of the water purifier of this invention.

符号の説明Explanation of symbols

1 浄水カートリッジ
2 筒状容器
3 繊維状濾材
4 粒状濾材
5 仕切り部材
6 仕切り部材
7 中空糸膜
8 収納筒体部
9 流路切換部
10 蛇口取付部
11 原水受入口
12 原水送水部
13 浄水吐出口
DESCRIPTION OF SYMBOLS 1 Water purification cartridge 2 Cylindrical container 3 Fibrous filter medium 4 Granular filter medium 5 Partition member 6 Partition member 7 Hollow fiber membrane 8 Storage cylinder part 9 Flow path switching part 10 Faucet attachment part 11 Raw water inlet 12 Raw water supply part 13 Purified water discharge outlet

Claims (4)

筒状容器の中心軸方向に繊維が配向し、かつその方向の厚みが3mm以上10mm未満である繊維状濾材が筒状容器の内部に配された浄水カートリッジ。   A water purification cartridge in which fibers are oriented in a central axis direction of a cylindrical container, and a fibrous filter medium having a thickness in the direction of 3 mm or more and less than 10 mm is arranged inside the cylindrical container. 筒状容器の中心軸方向に繊維を配向させ、かつその方向の厚みを3mm以上10mm未満とした繊維状濾材を、該筒状容器の径方向に0.1〜5%の圧縮率で圧縮して、該筒状容器の内部に充填する浄水カートリッジの製造方法。   A fibrous filter medium in which the fibers are oriented in the central axis direction of the cylindrical container and the thickness in the direction is 3 mm or more and less than 10 mm is compressed at a compression rate of 0.1 to 5% in the radial direction of the cylindrical container. And the manufacturing method of the water purification cartridge with which the inside of this cylindrical container is filled. 粒状濾材を前記筒状容器の内部に充填した後、前記繊維状濾材を前記筒状容器の内部に充填し、さらに前記繊維状濾材に対し、10〜300Nの力を前記筒状容器の中心軸方向に印加する請求項2に記載の浄水カートリッジの製造方法。   After filling the inside of the cylindrical container with the granular filter medium, the fibrous filter medium is filled into the inside of the cylindrical container, and further, a force of 10 to 300 N is applied to the central axis of the cylindrical container against the fibrous filter medium. The manufacturing method of the water purification cartridge of Claim 2 applied to a direction. 請求項1に記載の浄水カートリッジが着脱可能に接続された浄水器。   A water purifier to which the water purification cartridge according to claim 1 is detachably connected.
JP2004055063A 2004-02-27 2004-02-27 Water purification cartridge, method for producing the same, and water purifier provided with the same Expired - Fee Related JP4255070B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004055063A JP4255070B2 (en) 2004-02-27 2004-02-27 Water purification cartridge, method for producing the same, and water purifier provided with the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004055063A JP4255070B2 (en) 2004-02-27 2004-02-27 Water purification cartridge, method for producing the same, and water purifier provided with the same

Publications (2)

Publication Number Publication Date
JP2005238187A true JP2005238187A (en) 2005-09-08
JP4255070B2 JP4255070B2 (en) 2009-04-15

Family

ID=35020483

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004055063A Expired - Fee Related JP4255070B2 (en) 2004-02-27 2004-02-27 Water purification cartridge, method for producing the same, and water purifier provided with the same

Country Status (1)

Country Link
JP (1) JP4255070B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008156168A1 (en) * 2007-06-20 2008-12-24 Mitsubishi Rayon Cleansui Company, Limited Water purifying cartridge, and water purifier
JP2009006239A (en) * 2007-06-27 2009-01-15 Mrc Home Products Kk Water purifying cartridge and water purifier
CN102616877A (en) * 2007-06-20 2012-08-01 三菱丽阳可菱水有限公司 Water purifying cartridge, and water purifier
JP2017192869A (en) * 2016-04-18 2017-10-26 三菱ケミカル・クリンスイ株式会社 Water purification cartridge and water purifier

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008156168A1 (en) * 2007-06-20 2008-12-24 Mitsubishi Rayon Cleansui Company, Limited Water purifying cartridge, and water purifier
CN102616877A (en) * 2007-06-20 2012-08-01 三菱丽阳可菱水有限公司 Water purifying cartridge, and water purifier
JP2009006239A (en) * 2007-06-27 2009-01-15 Mrc Home Products Kk Water purifying cartridge and water purifier
JP2017192869A (en) * 2016-04-18 2017-10-26 三菱ケミカル・クリンスイ株式会社 Water purification cartridge and water purifier

Also Published As

Publication number Publication date
JP4255070B2 (en) 2009-04-15

Similar Documents

Publication Publication Date Title
KR100905346B1 (en) Method for cleaning water purifier
JP5582194B2 (en) Water purification cartridge and water purifier
KR20090059162A (en) Filter with improved media utilization and methods of making and using same
JP6182819B2 (en) Water purification cartridge, water purifier
US7229552B1 (en) Water purification apparatus and system
JP4255070B2 (en) Water purification cartridge, method for producing the same, and water purifier provided with the same
JP4512455B2 (en) Self-weight filtration type water purifier and water purification cartridge
JP4131821B2 (en) Water purifier
EP1948346B1 (en) Filter cartridge for water purification
JP4299522B2 (en) Water purifier cartridge and water purifier
JP2005000768A (en) Water cleaning cartridge
JP2002355515A (en) Filter for water treatment
JP5081749B2 (en) Water purifier cartridge
JP2002263637A (en) Water purifying unit
JP4866512B2 (en) Water purification cartridge, water purifier and water purification shower using cylindrical filter media
JP5081750B2 (en) Water purifier cartridge
KR100401937B1 (en) deep bed filter cartridge
JP4646282B2 (en) Water purifier
TWI391176B (en) Water filter
JP3495062B2 (en) Water purifier
JP2003062561A (en) Cartridge for water purifier
EP2647414A1 (en) Assembly for forming a component of a device for treating a fluid
JP2002126724A (en) Water cleaner
KR200307488Y1 (en) deep bed filter cartridge
JP5099052B2 (en) cartridge

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20070215

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20080827

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080904

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20081030

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20081120

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20081218

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20090122

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20090123

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120206

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120206

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130206

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130206

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130206

Year of fee payment: 4

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130206

Year of fee payment: 4

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130206

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees