JPH0899080A - Packing material for filtering - Google Patents
Packing material for filteringInfo
- Publication number
- JPH0899080A JPH0899080A JP23636394A JP23636394A JPH0899080A JP H0899080 A JPH0899080 A JP H0899080A JP 23636394 A JP23636394 A JP 23636394A JP 23636394 A JP23636394 A JP 23636394A JP H0899080 A JPH0899080 A JP H0899080A
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- nonwoven fabric
- fabric layer
- density nonwoven
- filtration
- 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
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、浄水器などに組み込ま
れて原水中の遊離塩素及び有機物を除去する濾過用充填
材で、具体的には、微粒状活性炭や粒状活性炭、成型繊
維活性炭などからなる活性炭層を有するものに関する。BACKGROUND OF THE INVENTION The present invention relates to a filler for filtration which is incorporated into a water purifier or the like to remove free chlorine and organic matter in raw water, and specifically, fine granular activated carbon, granular activated carbon, molded fiber activated carbon, etc. And an activated carbon layer consisting of
【0002】[0002]
【従来の技術】近年の浄水器技術では、浄水能力とし
て、遊離塩素及び有機物を除去する遊離塩素・有機物除
去能力に加えて、濁質を除去できる除濁能力も要求され
るようになってきた。そのような要求を充足する濾過用
充填材として従来では、活性炭層と中空糸膜とを組み合
わせたものが知られている。2. Description of the Related Art In recent years, in water purifier technology, in addition to the free chlorine / organic matter removing ability for removing free chlorine and organic matter, a turbidity removing ability for removing suspended matter has been required. . Conventionally, a combination of an activated carbon layer and a hollow fiber membrane is known as a filler for filtration that satisfies such requirements.
【0003】[0003]
【発明が解決しようとする課題】しかし、上記従来の技
術によるときは、除濁能力を有するものの、中空糸膜を
用いることが原因で次のような不都合があった。However, the above-mentioned conventional technique has the following disadvantages due to the use of the hollow fiber membrane although it has the turbidity removing ability.
【0004】中空糸膜が精密濾過領域の濾過膜であるた
め、僅かな水質変化により中空糸膜の目詰まりが急速に
起こり、加えて、その中空糸膜では濁質だけでなく原水
中に含まれる有機物やその有機物に起因して異常増殖し
た菌が目詰まりの原因となり、その結果、短期間に濾過
流量が低下していた。そして、中空糸膜では一旦目詰ま
りが発生すると、洗浄などを行っても、目詰まり解消に
よる濾過流量の回復を望めず、濾過流量を確保するには
濾過流量が低下する毎に交換が必要となって、維持管理
費が嵩んでいた。Since the hollow fiber membrane is a filtration membrane in the microfiltration region, a slight change in water quality causes rapid clogging of the hollow fiber membrane. In addition, the hollow fiber membrane contains not only suspended solids but also raw water. The organic matter that is generated and the bacteria that have abnormally grown due to the organic matter cause clogging, and as a result, the filtration flow rate is reduced in a short period of time. Once the hollow fiber membrane is clogged, even if it is washed, it is not possible to recover the filtration flow rate by eliminating the clogging, and in order to secure the filtration flow rate, replacement is required every time the filtration flow rate decreases. As a result, maintenance costs were high.
【0005】しかも、中空糸膜では単位時間当たりの濾
過流量を大きく取れないから、浄水器などが必要とする
濾過流量を確保するには、膜面積を大きくする必要があ
り、その結果、高価な中空糸膜を多量に必要としてイニ
シャルコストが高く付くことはもちろん、中空糸膜の設
置に大きなスペースを必要として浄水器を小型化する場
合には実施不可能な事態を招来することもあった。Further, since the hollow fiber membrane cannot provide a large filtration flow rate per unit time, it is necessary to increase the membrane area in order to secure the filtration flow rate required by the water purifier or the like, and as a result, it is expensive. In addition to requiring a large amount of hollow fiber membranes, the initial cost is high, and a large space is required for installing the hollow fiber membranes, which may cause an impractical situation when the water purifier is downsized.
【0006】また、中空糸膜により原水中の生菌を濾過
捕捉して無菌浄水を得ることができるものの、捕捉した
生菌の副生物としての異味異臭などによる水質低下が避
けられなかった。[0006] Further, although the hollow fiber membrane makes it possible to filter and capture live bacteria in raw water to obtain aseptic purified water, it is unavoidable that water quality is deteriorated due to off-flavor and off-odor as a by-product of the captured live bacteria.
【0007】本発明の第1の目的は、優れた除濁能力を
発揮できながらも、長期間に亘って安定した濾過流量を
確保することができる濾過用充填材を提供する点にあ
り、第2の目的は、水質低下を招来することなく浄水の
無菌化も図ることができる濾過用充填材を提供する点に
ある。A first object of the present invention is to provide a filtration filler capable of ensuring a stable filtration flow rate for a long period of time while exhibiting an excellent turbidity removing ability. The purpose of No. 2 is to provide a filler for filtration which can sterilize purified water without causing deterioration of water quality.
【0008】[0008]
【課題を解決するための手段】請求項1記載の本発明の
第1発明による濾過用充填材の特徴は、活性炭層に高密
度不織布層を濾過方向で積層配置してある点にある。A feature of the filtration filler according to the first aspect of the present invention is that the high-density nonwoven fabric layer is laminated on the activated carbon layer in the filtration direction.
【0009】請求項2記載の本発明の第2発明による濾
過用充填材の特徴は、上記第1発明において、前記活性
炭層及び高密度不織布層のそれぞれに、合成無機不溶体
に銀イオンを結合させた抗菌材又は合成無機不溶体に銀
化合物を添着させた抗菌材を、活性炭層及び高密度不織
布層の銀含有率を0.05〜1.0%とさせる量をもっ
て均一分散させてある点にある。According to a second aspect of the present invention, the filler for filtration according to the second aspect of the present invention is characterized in that, in the first aspect of the present invention, a silver ion is bonded to a synthetic inorganic insoluble material in each of the activated carbon layer and the high density nonwoven fabric layer. The antibacterial material or the antibacterial material obtained by impregnating a synthetic inorganic insoluble material with a silver compound is uniformly dispersed in an amount such that the silver content in the activated carbon layer and the high density nonwoven fabric layer is 0.05 to 1.0%. It is in.
【0010】請求項3記載の本発明の第3発明による濾
過用充填材の特徴は、上記第1発明において、合成無機
不溶体に銀イオンを結合させた抗菌材又は合成無機不溶
体に銀化合物を添着させた抗菌材を、活性炭層の銀含有
率を0.05〜1.0%とさせる量をもって前記活性炭
層に均一分散させ、合成無機不溶体に銀イオンを結合さ
せた抗菌材又は合成無機不溶体に銀化合物を添着させた
抗菌材を、高密度不織布層の構成繊維の銀含有率を0.
05〜1.0%とさせる量をもって高密度不織布層の構
成繊維中に含有させてある点にある。According to a third aspect of the present invention, the filtering filler according to the third aspect is characterized in that, in the first aspect, the antibacterial material obtained by binding silver ions to the synthetic inorganic insoluble material or the silver compound to the synthetic inorganic insoluble material. The antibacterial material impregnated with is dispersed evenly in the activated carbon layer in an amount that makes the silver content of the activated carbon layer 0.05 to 1.0%, and an antibacterial material or a synthetic inorganic insoluble material bound with silver ions An antibacterial material obtained by impregnating an inorganic insoluble material with a silver compound was used to reduce the silver content of the constituent fibers of the high density nonwoven fabric layer to 0.
It is contained in the constituent fibers of the high-density nonwoven fabric layer in an amount of 05 to 1.0%.
【0011】[0011]
【作用】本発明者らは、実験及び研究を重ねた結果次の
事実を見出した。すなわち、成型繊維活性炭などからな
る活性炭層と密度が0.3g/cc以上の高密度不織布
層とを積層配置した構造の濾過用充填材では、活性炭層
及び高密度不織布層を単位時間当たりの濾過流量を大き
くした場合であっても、活性炭層での濾過抵抗と高密度
不織布層での濾過抵抗との僅かな差により、それら活性
炭層と高密度不織布層との界面で濁質を多量に捕捉でき
て、中空糸膜と同等の除濁能力を発揮でき、しかも、活
性炭層及び高密度不織布層では、水道水程度の水質変化
であれば、その水質変化が目詰まりの進行具合に全く影
響せずに常に安定した濾過流量を確保できる。The present inventors have found the following facts as a result of repeated experiments and studies. That is, in a filtration filler having a structure in which an activated carbon layer made of molded fiber activated carbon or the like and a high density nonwoven fabric layer having a density of 0.3 g / cc or more are laminated and arranged, the activated carbon layer and the high density nonwoven fabric layer are filtered per unit time. Even if the flow rate is increased, a small difference between the filtration resistance in the activated carbon layer and the filtration resistance in the high-density nonwoven fabric layer captures a large amount of suspended matter at the interface between the activated carbon layer and the high-density nonwoven fabric layer. In addition, it can exhibit the same turbidity removal performance as a hollow fiber membrane, and in the activated carbon layer and the high-density nonwoven fabric layer, if the water quality changes to the extent of tap water, the change in water quality has no effect on the progress of clogging. It is possible to always secure a stable filtration flow rate.
【0012】従って、第1発明によれば、中空糸膜と同
等の除濁性能を発揮でき、しかも、それでいて、長期間
に亘って安定した濾過流量を確保でき、その上、単位時
間当たりの濾過流量が大きいことで必要な濾過流量を得
るにあたって必要となる濾過面積を小さくできる。Therefore, according to the first aspect of the present invention, the same turbidity removal performance as that of the hollow fiber membrane can be exhibited, and yet a stable filtration flow rate can be secured for a long period of time, and moreover, filtration per unit time is achieved. Since the flow rate is large, the filtration area required to obtain the required filtration flow rate can be reduced.
【0013】また、ゼオライトなどの合成無機不溶体に
銀イオンを結合させた抗菌材や、合成無機不溶体に銀化
合物を添着させた抗菌材では、銀の生菌との接触で生菌
を死滅させる抗菌能を発現することが知られている。In addition, in an antibacterial material in which a silver ion is bound to a synthetic inorganic insoluble material such as zeolite or an antibacterial material in which a silver compound is attached to a synthetic inorganic insoluble material, the live bacteria are killed by contact with live silver bacteria. It is known to develop antibacterial activity.
【0014】従って、活性炭層及び高密度不織布層にそ
のような抗菌材を均一分散させてある第2発明や、或い
は、活性炭層に抗菌材を均一分散させ、高密度不織布層
の構成繊維に抗菌材を混入させてある第3発明によると
きは、それら活性炭層及び高密度不織布層の銀の含有率
を適宜選択することにより、活性炭層及び高密度不織布
層内での生菌の繁殖を阻止して、それらを無菌状態に維
持することができる。このように生菌の繁殖を阻止でき
るから、自ずと、水質低下原因となる異味異臭などの生
菌副生物の発生もない。Therefore, the second invention in which such an antibacterial material is uniformly dispersed in the activated carbon layer and the high-density nonwoven fabric layer, or the antibacterial material is uniformly dispersed in the activated carbon layer, and the constituent fibers of the high-density nonwoven fabric layer are antibacterial. In the case of the third invention in which the material is mixed, the growth of viable bacteria in the activated carbon layer and the high-density nonwoven fabric layer is prevented by appropriately selecting the content ratio of silver in the activated carbon layer and the high-density nonwoven fabric layer. And keep them sterile. In this way, since it is possible to prevent the growth of live bacteria, naturally, there is no generation of live bacteria by-products such as off-flavors and off-flavors that cause water quality deterioration.
【0015】そして、本発明者らは、実験及び研究の結
果、活性炭層及び高密度不織布層への抗菌材の添加量
は、活性炭層及び高密度不織布層の銀含有率を0.05
〜1.0%とさせる量が抗菌面及び経済面から見て最適
であることを見出した。つまり、0.05%よりも少な
いと、活性炭層及び高密度不織布層の抗菌化を確実に達
成できず、また、1.0%よりも多くしても、抗菌能の
改善が見られず、また、銀イオンの溶出量増大を招く。As a result of experiments and studies, the present inventors have found that the amount of antibacterial material added to the activated carbon layer and the high-density nonwoven fabric layer is such that the silver content of the activated carbon layer and the high-density nonwoven fabric layer is 0.05.
It was found that an amount of ˜1.0% is optimum from the viewpoint of antibacterial and economic aspects. That is, if it is less than 0.05%, antibacterialization of the activated carbon layer and the high-density nonwoven fabric layer cannot be reliably achieved, and if it is more than 1.0%, no improvement in antibacterial activity is observed. In addition, the elution amount of silver ions is increased.
【0016】従って第2発明によるときは、確実な抗菌
を経済的に行うことができる。Therefore, according to the second invention, reliable antibacterial can be economically performed.
【0017】また、本発明者らは、実験及び研究の結
果、高密度不織布層の構成繊維中の抗菌材の混合量は、
構成繊維の銀含有率を0.05〜1.0%とさせる量が
抗菌能の面及び経済面からみて最適であることを見出し
た。上記と同様に、0.05%よりも少ないと、活性炭
層及び高密度不織布層の抗菌化を確実に達成できず、ま
た、1.0%よりも多くしても、抗菌能の改善が見られ
ない。Further, as a result of experiments and research, the present inventors have found that the amount of the antibacterial material mixed in the constituent fibers of the high-density nonwoven fabric layer is
It has been found that the amount of the constituent fiber which makes the silver content 0.05 to 1.0% is optimum from the viewpoint of antibacterial activity and economical aspect. Similar to the above, if it is less than 0.05%, the antibacterial property of the activated carbon layer and the high-density nonwoven fabric layer cannot be reliably achieved, and if it is more than 1.0%, the antibacterial activity is improved. I can't.
【0018】従って第3発明によるときは、確実な抗菌
を経済的に行うことができる。Therefore, according to the third invention, reliable antibacterial can be economically performed.
【0019】[0019]
【発明の効果】以上の結果、請求項1記載の第1発明に
よるときは、中空糸膜と同等の除濁性能を発揮できなが
らも、長期間に亘って安定した濾過流量を確保できるこ
とにより交換サイクルが長くて維持管理が低コストにな
り、しかも、単位時間当たりの濾過流量が大きいことで
必要な濾過流量を得るにあたって必要となる濾過面積が
小さいことにより、設置スペースが少なくて済んで小型
の浄水器への組み込み実施も容易に行うことができる濾
過用充填材を提供できるようになった。As a result of the above, according to the first aspect of the present invention, the replacement can be performed by ensuring a stable filtration flow rate for a long period of time while exhibiting the same turbidity performance as the hollow fiber membrane. A long cycle reduces maintenance costs, and a large filtration flow rate per unit time reduces the filtration area required to obtain the required filtration flow rate. It has become possible to provide a packing material for filtration that can be easily incorporated into a water purifier.
【0020】特に、請求項2記載の第2発明や請求項3
記載の第3発明によるときは、加えて、水質低下を招来
することなく、無菌浄水を経済的に得ることもできる濾
過用充填材を提供できるようになった。Particularly, the second invention according to claim 2 and claim 3
According to the third aspect of the invention described above, in addition, it is possible to provide a filler for filtration that can economically obtain sterile purified water without causing deterioration of water quality.
【0021】[0021]
【実施例】浄水器等に組み込まれる濾過用充填材は、図
1に示すように、筒状の活性炭層1の外周に、高密度不
織布層2を積層密着配置して構成されている。EXAMPLE As shown in FIG. 1, a filtering filler incorporated in a water purifier or the like comprises a cylindrical activated carbon layer 1 and a high-density nonwoven fabric layer 2 laminated and closely arranged on the outer periphery thereof.
【0022】前記活性炭層1は、成型繊維活性炭から構
成されており、それの密度は0.2g/cc未満であ
る。つまり、密度が0.2g/cc以上であると、中空
糸膜と同様に僅かな水質変化により目詰まりが急速に起
こって短期間で濾過流量低下を招来するからである。成
型繊維活性炭は、約1000〜2000m2 /gの比表
面積を有する繊維活性炭にバインダーを加えて成型する
ことで製造されたものである。The activated carbon layer 1 is made of molded fiber activated carbon and has a density of less than 0.2 g / cc. That is, if the density is 0.2 g / cc or more, similar to the hollow fiber membrane, a slight change in water quality causes rapid clogging, resulting in a reduction in filtration flow rate in a short period of time. Molded fiber activated carbon is produced by adding a binder to fiber activated carbon having a specific surface area of about 1000 to 2000 m 2 / g and molding.
【0023】前記高密度不織布層2は、ナイロン繊維や
ポリエステル繊維、ポリプロピレン繊維などの合成繊維
を原材料(構成繊維)として製造された不織布を密度が
0.3g/cc以上となるように圧縮加工した不織布か
らなる。The high-density non-woven fabric layer 2 is a non-woven fabric produced by using synthetic fibers such as nylon fibers, polyester fibers and polypropylene fibers as a raw material (constituent fiber) and compression-processed to have a density of 0.3 g / cc or more. Made of non-woven fabric.
【0024】そして、前記活性炭層1及び高密度不織布
層2は、抗菌材の添加により抗菌化されている。The activated carbon layer 1 and the high-density nonwoven fabric layer 2 are made antibacterial by adding an antibacterial material.
【0025】前記抗菌材としては、合成無機不溶体に銀
イオンを結合させた抗菌材や、合成無機不溶体に銀化合
物を添着した抗菌材を挙げることができ、これらは、銀
の生菌への接触によりその生菌を死滅させるものであ
る。抗菌材の具体例としては、合成又は天然のゼオライ
トに銀イオンをイオン交換反応により結合させたもの
(以下銀ゼオライトと称する。)や、リン酸ジルコニウ
ムに銀イオンを担持結合させたものを挙げることができ
る。Examples of the antibacterial material include an antibacterial material in which a silver ion is bound to a synthetic inorganic insoluble material and an antibacterial material in which a silver compound is attached to a synthetic inorganic insoluble material. The contact between the two kills the viable bacteria. Specific examples of the antibacterial material include those in which silver ions are bound to synthetic or natural zeolite by an ion exchange reaction (hereinafter referred to as silver zeolite) and those in which silver ions are supported and bound to zirconium phosphate. You can
【0026】そして、前記活性炭層1を抗菌化する手段
は、活性炭層1内に抗菌材を均一分散させる手段であっ
て、抗菌化に必要な抗菌材の添加量は、活性炭層1の銀
含有量を0.05〜1.0%とさせる量である。また、
活性炭層1内に抗菌材を均一分散させる具体的手段とし
ては、成型繊維活性炭を製造する際、原料である繊維活
性炭に銀ゼオライトなどの抗菌材を均一分散混合させ、
この混合物を成型する手段を挙げることができる。The means for antibacterializing the activated carbon layer 1 is a means for uniformly dispersing the antibacterial material in the activated carbon layer 1, and the addition amount of the antibacterial material necessary for the antibacterial conversion is the silver content of the activated carbon layer 1. The amount is set to 0.05 to 1.0%. Also,
As a specific means for uniformly dispersing the antibacterial material in the activated carbon layer 1, when the molded fiber activated carbon is manufactured, the antibacterial material such as silver zeolite is uniformly dispersed and mixed in the fiber activated carbon as a raw material,
Means for molding this mixture may be mentioned.
【0027】他方、前記高密度不織布層2を抗菌化する
手段としては、〈1〉高密度不織布層2内に抗菌材を均
一分散させる手段と、〈2〉高密度不織布の原材料であ
る合成繊維(構成繊維)自体を抗菌材含有の抗菌繊維と
して製造する手段とを挙げることができる。On the other hand, as means for making the high density nonwoven fabric layer 2 antibacterial, <1> means for uniformly dispersing the antibacterial material in the high density nonwoven fabric layer 2 and <2> synthetic fiber as a raw material for the high density nonwoven fabric layer Means for producing (constituent fiber) itself as an antibacterial fiber containing an antibacterial material.
【0028】前者〈1〉の手段による抗菌化に必要な抗
菌材の添加量は、高密度不織布層2の銀含有量を0.0
5〜1.0%とさせる量であり、高密度不織布層2内に
抗菌材を均一分散させる具体的手段としては、高密度不
織布を製造する際、原材料である合成繊維(構成繊維)
に銀ゼオライトなどの抗菌材を均一分散混合させ、その
混合物から不織布を製造する手段を挙げることができ
る。The amount of the antibacterial material necessary for antibacterialization by the former <1> means that the silver content of the high density nonwoven fabric layer 2 is 0.0
The amount is 5 to 1.0%, and as a specific means for uniformly dispersing the antibacterial material in the high-density nonwoven fabric layer 2, synthetic fiber (constituent fiber) which is a raw material when manufacturing the high-density nonwoven fabric is used.
An example is a means for uniformly dispersing and mixing an antibacterial material such as silver zeolite, and producing a nonwoven fabric from the mixture.
【0029】また、後者〈2〉の手段による抗菌化に必
要な抗菌材の添加量は、構成繊維の銀含有率を0.05
〜1.0%とさせる量である。The amount of the antibacterial material required for antibacterial conversion by the latter <2> means that the silver content of the constituent fibers is 0.05.
The amount is about 1.0%.
【0030】なお、前者〈1〉の手段で抗菌化された高
密度不織布層2を抗菌材分散型のものと称し、後者
〈2〉の手段で抗菌化された高密度不織布層2を抗菌材
含有型のものと称する。The high-density non-woven fabric layer 2 antibacterialized by the former <1> is referred to as an antibacterial-material-dispersed type, and the high-density non-woven fabric layer 2 antibacterialized by the latter <2> is used. It is referred to as containing type.
【0031】上記のように構成された濾過用充填材は、
高密度不織布層2・活性炭層1とその記載順に原水を透
過させることにより、原水を濾過処理するものであり、
図2に示すように、カートリッジ容器3に内装された形
態で使用される。つまり、浄水器などに着脱自在に装填
される浄水カートリッジ4が濾過用充填材とカートリッ
ジ容器3とから構成されている。The filtration filler having the above-mentioned structure is
The high-density non-woven fabric layer 2 and the activated carbon layer 1 and the raw water permeate the raw water in the stated order to filter the raw water.
As shown in FIG. 2, the cartridge container 3 is used in the form of being installed therein. That is, the water purification cartridge 4 that is detachably loaded into the water purifier and the like is composed of the filtering filler and the cartridge container 3.
【0032】前記カートリッジ容器3について説明する
と、カートリッジ容器3は、円筒部とその円筒部の両端
を閉塞する端板部とを有する構造に構成されており、高
密度不織布層2の外周面と円筒部の内周面との間に原水
分散ゾーン5を形成するように濾過用充填材を同芯状に
位置させて内装するものであり、端板部のそれぞれに
は、内装した濾過用充填材の活性炭層1の端面に食い込
むことにより、活性炭層1の端面と端板部との隙間を通
しての濾過水集水路6を構成する濾過用充填材内空洞部
と前記原水分散ゾーン5との間での通水を遮断するリン
グ状のシール部7が形成されている。そして、円筒部に
は、原水分散ゾーン5に原水を供給する原水入口8が形
成され、一方の端板部には、濾過水集水路6から濾過水
を取り出す濾過水出口9が形成されている。これら原水
入口8及び濾過水出口9は、浄水器などの本体への浄水
カートリッジ4の装填に伴って本体に形成の原水供給路
及び濾過水取出し路に自動的に接続するものである。Explaining the cartridge container 3, the cartridge container 3 has a structure having a cylindrical portion and end plate portions for closing both ends of the cylindrical portion, and the outer peripheral surface of the high density nonwoven fabric layer 2 and the cylindrical portion. The filler for filtration is placed concentrically so as to form the raw water dispersion zone 5 between the inner peripheral surface and the inner peripheral surface of the inner portion, and each end plate portion is provided with the filler for filtration installed therein. By digging into the end surface of the activated carbon layer 1, the space between the raw material dispersion zone 5 and the hollow portion in the filler for filtration forming the filtered water collecting channel 6 passing through the gap between the end surface of the activated carbon layer 1 and the end plate portion. A ring-shaped seal portion 7 is formed to block the passage of water. A raw water inlet 8 for supplying raw water to the raw water dispersion zone 5 is formed in the cylindrical portion, and a filtered water outlet 9 for taking out filtered water from the filtered water collecting passage 6 is formed in one end plate portion. . The raw water inlet 8 and the filtered water outlet 9 are automatically connected to the raw water supply passage and the filtered water take-out passage formed in the main body as the main body such as the water purifier is loaded with the water purification cartridge 4.
【0033】活性炭層1及び高密度不織布層2の銀の含
有率は同じであっても良いが、相違していても良い。そ
して、活性炭層1においては、活性炭による有機物の吸
着により活性炭表面に有機物が付着堆積してその活性炭
表面が生菌の繁殖に最適な環境となり易いことから、活
性炭層1の銀の含有率を大きくすることが好ましい。The silver contents of the activated carbon layer 1 and the high density nonwoven fabric layer 2 may be the same or different. Then, in the activated carbon layer 1, the adsorption of the organic matter by the activated carbon causes the organic matter to adhere to and deposit on the surface of the activated carbon, and the activated carbon surface is likely to be the optimum environment for the growth of live bacteria. Therefore, the silver content of the activated carbon layer 1 is increased. Preferably.
【0034】次に本発明者らが行った浄水実験を示す。 〈濾過テスト〉試験体の仕様を表1に示す。Next, a water purification experiment conducted by the present inventors will be shown. <Filtration Test> Table 1 shows the specifications of the test body.
【表1】 [Table 1]
【0035】試験体における活性炭層1及び高密度不織
布層2の組成などは実施例で説明したものである。な
お、高密度不織布層2は、抗菌材分散型のものである。
そして、上述の実施例で説明した浄水カートリッジ4の
形態としてテストを行った。テストは、濾過圧力を1.
0kg/m2 として行った。原水の濁度を2°とした場
合と、10°とした場合とについてテストした。そし
て、濾過に伴う濾過用充填材の濾過流量(リットル/
分)の変化、つまり、総濾過流量(リットル)と濾過流
量(リットル/分)との関係及び、総濾過流量(リット
ル)と濁質の除去率(%)との関係を調査した。原水濁
度2°の場合の調査結果を図3及び図4に示し、原水濁
度10°の場合の調査結果を図5及び図6に示す。特
に、原水濁度2°の場合における図4の濁度除去率の向
上は濁質による充填材の目詰まりによるもので、圧力損
失の上昇を招く。従って、対比して示す図3から分かる
ごとく濾過流量の低下を来す。その結果、実用上の濾過
流量は初期流量の50%程度となる。図5、図6(原水
濁度10°の場合)についても同様である。なお、高密
度不織布層2を抗菌材分散型とする場合の濾過性能と抗
菌材含有型とする場合の濾過性能とは同じと考えられる
から、つまり、抗菌材の添加の仕方による濾過性能の差
異がないと考えられるから、高密度不織布層2として抗
菌材含有型のものを用いた場合であっても、仕様が同じ
なら同様な結果を得られると推定できる。The composition and the like of the activated carbon layer 1 and the high density nonwoven fabric layer 2 in the test body are as described in the examples. The high-density nonwoven fabric layer 2 is of an antibacterial material dispersed type.
Then, a test was conducted as the form of the water purification cartridge 4 described in the above-mentioned embodiment. The test was conducted at a filtration pressure of 1.
It was performed at 0 kg / m 2 . Tests were carried out when the turbidity of raw water was 2 ° and 10 °. Then, the filtration flow rate of the filtration filler accompanying the filtration (liter /
Min), that is, the relationship between the total filtration flow rate (liter) and the filtration flow rate (liter / minute), and the relationship between the total filtration flow rate (liter) and the turbidity removal rate (%) were investigated. 3 and 4 show the investigation results when the raw water turbidity was 2 °, and FIGS. 5 and 6 show the investigation results when the raw water turbidity was 10 °. Particularly, when the raw water turbidity is 2 °, the improvement of the turbidity removal rate in FIG. 4 is due to the clogging of the filler due to the turbidity, which causes an increase in pressure loss. Therefore, as can be seen from FIG. 3 shown in contrast, the filtration flow rate is reduced. As a result, the practical filtration flow rate is about 50% of the initial flow rate. The same applies to FIGS. 5 and 6 (when the raw water turbidity is 10 °). The filtration performance when the high-density nonwoven fabric layer 2 is of the antibacterial material dispersed type is considered to be the same as that of the antibacterial material-containing type, that is, the difference in the filtration performance depending on the method of adding the antibacterial material. Therefore, it can be presumed that similar results can be obtained if the specifications are the same even when an antibacterial material-containing type is used as the high-density nonwoven fabric layer 2.
【0036】〈抗菌テスト〉試験体として、高密度不織
布層2が抗菌材分散型のものと抗菌材含有型のものとの
二種類を用意した。各試験体の仕様及びテスト結果を表
2に示す。各試験体は、銀の含有率が相違するだけで、
他の仕様は表1に示した試験体1と同じである。<Antibacterial Test> As the test body, two kinds of the high-density nonwoven fabric layer 2 of antibacterial material dispersion type and antibacterial material containing type were prepared. Table 2 shows the specifications and test results of each test body. Each specimen has a different silver content,
Other specifications are the same as those of the test body 1 shown in Table 1.
【表2】 [Table 2]
【0037】テストは浄水カートリッジ4の形態で行っ
た。そしてテストは、各積算流量において濾過水をサン
プリングし、サンプリング水を標準寒天培地を用いて3
6℃48時間培養後に培地に集落を形成した生菌の数を
計測した。NDは検出せずである。The test was carried out in the form of a water purification cartridge 4. The test was conducted by sampling the filtered water at each cumulative flow rate and using the standard agar medium as the sampling water.
After culturing at 6 ° C. for 48 hours, the number of viable bacteria forming colonies in the medium was counted. ND is not detected.
【0038】〔別実施例〕上記実施例では、濾過用充填
材として円筒形のものを示したが、濾過用充填材は、図
7に示すように、円柱体又は立方体或いは直方体状の活
性炭層1に板状の高密度不織布層2を濾過方向で積層配
置したものであっても良い。上記実施例では、活性炭層
1として成型繊維活性炭からなるものを示したが、活性
炭層1は、微粒状活性炭や粒状活性炭からなるものであ
っても良い。また、繊維活性炭と微粒状活性炭とを混在
させて成型したものや、繊維活性炭と粒状活性炭とを混
在させて成型したものであっても良い。[Other Embodiments] In the above-mentioned embodiment, a cylindrical packing material is shown, but as shown in FIG. 7, the filtering packing material is a columnar, cubic or rectangular parallelepiped activated carbon layer. Alternatively, the plate-shaped high-density nonwoven fabric layer 2 may be laminated on the sheet 1 in the filtration direction. In the above-mentioned examples, the activated carbon layer 1 is made of molded fiber activated carbon, but the activated carbon layer 1 may be made of fine granular activated carbon or granular activated carbon. Further, it may be molded by mixing fiber activated carbon and fine granular activated carbon, or molded by mixing fiber activated carbon and granular activated carbon.
【0039】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.
【図1】切り欠き斜視図FIG. 1 is a cutaway perspective view.
【図2】浄水カートリッジの縦断面図[Figure 2] Vertical sectional view of water purification cartridge
【図3】原水濁度2°の場合の濾過テスト結果である総
濾過流量と濾過流量との関係を示すグラフFIG. 3 is a graph showing the relationship between the total filtration flow rate and the filtration flow rate, which are the filtration test results when the raw water turbidity is 2 °.
【図4】原水濁度2°の場合の濾過テスト結果である総
濾過流量と濁質除去率との関係を示すグラフFIG. 4 is a graph showing the relationship between the total filtration flow rate, which is the filtration test result when the raw water turbidity is 2 °, and the turbidity removal rate.
【図5】原水濁度10°の場合の濾過テスト結果である
総濾過流量と濾過流量との関係を示すグラフFIG. 5 is a graph showing the relationship between the total filtration flow rate and the filtration flow rate, which are the filtration test results when the raw water turbidity is 10 °.
【図6】原水濁度10°の場合の濾過テスト結果である
総濾過流量と濁質除去率との関係を示すグラフFIG. 6 is a graph showing the relationship between the total filtration flow rate, which is the filtration test result when the turbidity of raw water is 10 °, and the turbidity removal rate.
【図7】別実施例を示す断面図FIG. 7 is a sectional view showing another embodiment.
1 活性炭層 2 高密度不織布層 1 Activated carbon layer 2 High density nonwoven fabric layer
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/50 540 F 560 Z B (72)発明者 國▲崎▼ 伸一 大阪府三島郡島本町大字山崎1023―1 サ ントリー株式会社技術開発センター微生物 センター内 (72)発明者 益田 光信 大阪府大阪市北区堂島浜1丁目3番23号 株式会社タクマ内 (72)発明者 川口 純 大阪府大阪市北区堂島浜一丁目3番23号 株式会社タクマ内 (72)発明者 森本 健 大阪府大阪市北区堂島浜一丁目3番23号 株式会社タクマ内─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 6 Identification number Internal reference number FI Technical display location C02F 1/50 540 F 560 Z B (72) Inventor Kunisaki Shinichi Shimamoto-cho, Mishima-gun, Osaka Prefecture 1023-1 Yamazaki, Sanritsu Co., Ltd. Technology Development Center, Microbial Center (72) Inventor Mitsunobu Masuda 1-32 Dojimahama, Kita-ku, Osaka City, Osaka Prefecture Takuma Co., Ltd. (72) Inventor, Jun Kawaguchi Osaka City, Osaka Prefecture 1-32 Dojimahama, Kita-ku, Takuma Co., Ltd. (72) Inventor Ken Morimoto 1-3-23, Dojimahama, Kita-ku, Osaka, Osaka
Claims (3)
あって、前記活性炭層(1)に高密度不織布層(2)を
濾過方向で積層配置してある濾過用充填材。1. A filtration filler having an activated carbon layer (1), wherein a high density nonwoven fabric layer (2) is laminated on the activated carbon layer (1) in the filtration direction.
(2)のそれぞれに、合成無機不溶体に銀イオンを結合
させた抗菌材又は合成無機不溶体に銀化合物を添着させ
た抗菌材を、活性炭層(1)及び高密度不織布層(2)
の銀含有率を0.05〜1.0%とさせる量をもって均
一分散させてある請求項1記載の濾過用充填材。2. An antibacterial material in which a silver ion is bound to a synthetic inorganic insoluble material or an antibacterial material in which a silver compound is attached to a synthetic inorganic insoluble material in each of the activated carbon layer (1) and the high density nonwoven fabric layer (2). Activated carbon layer (1) and high-density nonwoven fabric layer (2)
The filler for filtration according to claim 1, wherein the filler is uniformly dispersed in an amount such that the silver content is 0.05 to 1.0%.
抗菌材又は合成無機不溶体に銀化合物を添着させた抗菌
材を、活性炭層(1)の銀含有率を0.05〜1.0%
とさせる量をもって前記活性炭層(1)に均一分散さ
せ、合成無機不溶体に銀イオンを結合させた抗菌材又は
合成無機不溶体に銀化合物を添着させた抗菌材を、高密
度不織布層(2)の構成繊維の銀含有率を0.05〜
1.0%とさせる量をもって高密度不織布層(2)の構
成繊維中に含有させてある請求項1記載の濾過用充填
材。3. An antibacterial material obtained by binding a silver ion to a synthetic inorganic insoluble material or an antibacterial material obtained by impregnating a synthetic inorganic insoluble material with a silver compound, wherein the silver content of the activated carbon layer (1) is 0.05 to 1. 0%
An antibacterial material obtained by uniformly dispersing silver ions in a synthetic inorganic insoluble material or an antibacterial material obtained by impregnating a synthetic inorganic insoluble material with a silver compound in a high density nonwoven fabric layer (2). ) The silver content of the constituent fibers is 0.05 to
The filler for filtration according to claim 1, which is contained in the constituent fibers of the high-density nonwoven fabric layer (2) in an amount of 1.0%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23636394A JPH0899080A (en) | 1994-09-30 | 1994-09-30 | Packing material for filtering |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23636394A JPH0899080A (en) | 1994-09-30 | 1994-09-30 | Packing material for filtering |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0899080A true JPH0899080A (en) | 1996-04-16 |
Family
ID=16999693
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23636394A Pending JPH0899080A (en) | 1994-09-30 | 1994-09-30 | Packing material for filtering |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0899080A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007296484A (en) * | 2006-05-01 | 2007-11-15 | Unitika Ltd | Water treatment filter |
| JP2009095731A (en) * | 2007-10-15 | 2009-05-07 | Kuraray Chem Corp | Filter for water treatment |
| WO2012133664A1 (en) * | 2011-03-31 | 2012-10-04 | 栗田工業株式会社 | Ultrapure water producing system and ultrapure water producing method |
| CN103768841A (en) * | 2012-10-17 | 2014-05-07 | 单建民 | Manufacturing method of activated carbon filter |
| 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 |
-
1994
- 1994-09-30 JP JP23636394A patent/JPH0899080A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007296484A (en) * | 2006-05-01 | 2007-11-15 | Unitika Ltd | Water treatment filter |
| JP2009095731A (en) * | 2007-10-15 | 2009-05-07 | Kuraray Chem Corp | Filter for water treatment |
| WO2012133664A1 (en) * | 2011-03-31 | 2012-10-04 | 栗田工業株式会社 | Ultrapure water producing system and ultrapure water producing method |
| CN103768841A (en) * | 2012-10-17 | 2014-05-07 | 单建民 | Manufacturing method of activated carbon filter |
| CN103768841B (en) * | 2012-10-17 | 2015-11-25 | 南通美亚新型活性炭制品有限公司 | Manufacturing method of activated carbon filter |
| 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 |
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