JPH0593593U - Membrane module - Google Patents
Membrane moduleInfo
- Publication number
- JPH0593593U JPH0593593U JP3852592U JP3852592U JPH0593593U JP H0593593 U JPH0593593 U JP H0593593U JP 3852592 U JP3852592 U JP 3852592U JP 3852592 U JP3852592 U JP 3852592U JP H0593593 U JPH0593593 U JP H0593593U
- Authority
- JP
- Japan
- Prior art keywords
- raw water
- activated carbon
- membrane
- membrane module
- sheet
- 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
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
(57)【要約】
【目的】水道水中の消毒剤を活性炭で吸着除去したうえ
で水道水の濾過を行う膜モジュ−ルにおいて、活性炭の
付設による原水圧力の低下並びにエアリ−クテスト時の
エア抵抗の増大をよく防止し、高い濾過流量を保障で
き、エアリ−クテストを容易に行い得、しかも通水停止
時の原水室内での雑菌繁殖をよく抑制できる膜モジュ−
ルを提供する。
【構成】一端に原水入口を、他端に濾過水出口をそれぞ
れ有するケ−ス内に濾過膜を設け、原水室側において濾
過膜をシ−ト状繊維活性炭で覆った。
(57) [Summary] [Purpose] In a membrane module for filtering tap water after adsorbing and removing the disinfectant in tap water with activated carbon, a drop in raw water pressure due to the addition of activated carbon and air resistance during air leak testing. Membrane module that can prevent the increase of water flow, ensure a high filtration flow rate, can easily perform air leak test, and can also suppress the growth of various bacteria in the raw water chamber when water flow is stopped.
To provide [Structure] A filter membrane was provided in a case having a raw water inlet at one end and a filtered water outlet at the other end, and the filter membrane was covered with sheet-like fiber activated carbon on the raw water chamber side.
Description
【0001】[0001]
本考案は膜モジュ−ルに関し、特に、飲料水の濾過に有用なものである。 The present invention relates to a membrane module, and is particularly useful for filtering drinking water.
【0002】[0002]
水道水を全量濾過方式の膜モジュ−ルで濾過する場合、水道水中の塩素系消毒 剤による膜劣化を防止し、膜寿命を長くするために、活性炭で塩素系消毒剤を吸 着除去したうえで、膜濾過を行うことが必要である。 このため、この種の従来の膜モジュ−ルには、膜を収容した原水室と原水入口 との間に、細かい目のスクリ−ンで仕切ったスペ−スを設け、このスペ−スに粒 状活性炭を充填したものが使用されている。 When tap water is filtered with a full-volume filtration membrane module, the chlorine-based disinfectant is adsorbed and removed with activated carbon in order to prevent membrane deterioration due to the chlorine-based disinfectant in tap water and prolong the life of the membrane. Therefore, it is necessary to perform membrane filtration. For this reason, in this type of conventional membrane module, a space separated by a fine-screen screen is provided between the raw water chamber containing the membrane and the raw water inlet, and the space is divided into particles. What is filled with activated carbon is used.
【0003】[0003]
ところで、上記膜モジュ−ルにおいて、膜の総面積をS1,膜単位面積あたり の濾過流量をa1,活性炭充填スペ−スの流路断面積をS2,活性炭充填スペ−ス の流路断面単位面積あたりの原水流量をa2とすれば、a2=a1S1/S2であり 、通常、活性炭充填スペ−スの流路断面積S2に較べ膜の総面積S1が著しく大で あるから、活性炭充填スペ−スの流路断面単位面積あたりの原水流量a2、即ち 原水流速は相当に高速である。In the membrane module, the total area of the membrane is S 1 , the filtration flow rate per unit area of the membrane is a 1 , the flow passage cross-sectional area of the activated carbon filling space is S 2 , and the flow passage of the activated carbon filling space is If the raw water flow rate per unit area of the cross section is a 2 , then a 2 = a 1 S 1 / S 2 , and the total area S 1 of the membrane is usually smaller than the flow path cross-sectional area S 2 of the activated carbon filled space. Since it is remarkably large, the raw water flow rate a 2 per unit area of the flow channel of the space filled with activated carbon, that is, the raw water flow velocity is considerably high.
【0004】 而して、上記従来の膜モジュ−ルにおいては、かかる高速流速箇所に粒状活性 炭を充填し、目の細かいスクリ−ンを設けているから、原水が活性炭充填スペ− スを通過するときの圧力降下が大きく、膜間有効差圧がそれだけ低くなって、濾 過流量の低下が避けられない。Thus, in the above-mentioned conventional membrane module, granular activated carbon is filled in such a high-velocity flow velocity portion and a fine screen is provided, so that raw water passes through the activated carbon filling space. The pressure drop during the operation is large and the effective transmembrane pressure difference is so low that the filtration flow rate cannot be avoided.
【0005】 また、膜モジュ−ルの使用前に行わなければならないエアリ−クテストに対し ても、活性炭充填スペ−スのために、エア流れ抵抗が大となり、原水室内エア圧 を所定の圧力にするには、使用エア圧を相当に高くしなければならず、エアリ− クテストも困難になる。Further, even in the air leak test that must be performed before using the membrane module, the air flow resistance becomes large due to the activated carbon filling space, and the air pressure in the raw water chamber becomes a predetermined pressure. In order to do so, the air pressure used must be increased considerably, and the air leak test becomes difficult.
【0006】 更に、活性炭が原水室の手前側(原水入口側)に存在するため、原水室内の原 水は消毒剤を含有せず、通水の長期停止時、原水室内の滞留原水中で雑菌がかな りのスピ−ドで繁殖するから、活性炭の吸着能力が短期間で低下し、また、死菌 の悪臭が膜を通って漏出することも往々にしてある。Further, since the activated carbon is present on the front side (raw water inlet side) of the raw water chamber, the raw water in the raw water chamber does not contain a disinfectant, and when the water flow is stopped for a long time, various bacteria are accumulated in the raw water in the raw water chamber. Since it propagates at a tremendous speed, the adsorption capacity of activated carbon is reduced in a short period of time, and the malodor of dead bacteria is often leaked through the membrane.
【0007】 本考案の目的は、水道水中の消毒剤を活性炭で吸着除去したうえで水道水の濾 過を行う膜モジュ−ルにおいて、活性炭の付設による原水圧力の低下並びにエア リ−クテスト時のエア抵抗の増大をよく防止し、高い濾過流量を保障でき、エア リ−クテストを容易に行い得、しかも通水停止時の原水室内での雑菌繁殖をよく 抑制できる膜モジュ−ルを提供することにある。The object of the present invention is to remove the disinfectant in tap water by adsorbing and removing it with activated carbon and then filtering the tap water. (EN) A membrane module that can prevent an increase in air resistance, can ensure a high filtration flow rate, can easily perform an air leak test, and can well suppress the growth of various bacteria in the raw water chamber when water flow is stopped. It is in.
【0008】[0008]
本考案の膜モジュ−ルは、一端に原水入口を、他端に濾過水出口をそれぞれ有 するケ−ス内に濾過膜を設け、原水室側において濾過膜をシ−ト状繊維活性炭で 覆ったことを特徴する構成である。 The membrane module of the present invention is provided with a filtration membrane in a case having a raw water inlet at one end and a filtered water outlet at the other end, and the filtration membrane is covered with sheet-like activated carbon on the raw water chamber side. This is a characteristic feature.
【0009】[0009]
活性炭を付設してある膜表面の原水流速が原水入口での原水流速に較べて一段 と小さいこと、並びに活性炭の形状自体が多間隙のシ−ト状繊維形態であって原 水通過に対し低抵抗体であることから、膜間有効差圧を高く保持でき、濾過流量 の低下をよく排除できる。 The flow velocity of raw water on the surface of the membrane to which activated carbon is attached is much smaller than the flow velocity of raw water at the raw water inlet, and the shape of activated carbon itself is a sheet-like fiber form with many pores, which is low for the passage of raw water. Since it is a resistor, the effective transmembrane pressure can be kept high, and the reduction in filtration flow rate can be eliminated well.
【0010】 また、原水入口と原水室との間に実質上エア抵抗体が介在せず、原水室内にエ ア圧を圧損なく作用させ得るから、エアリ−クテストを容易に行うことができる 。 更に、原水室内の水道水が消毒剤を含有した状態となるから、通水停止時で の原水室内滞留水中の雑菌の繁殖を充分に防止できる。Further, since the air resistor is not substantially interposed between the raw water inlet and the raw water chamber, and the air pressure can act in the raw water chamber without pressure loss, the air leak test can be easily performed. Furthermore, since the tap water in the raw water chamber contains the disinfectant, it is possible to sufficiently prevent the growth of bacteria in the accumulated water in the raw water chamber when the water flow is stopped.
【0011】[0011]
以下、図面により本考案の実施例を説明する。 図1において、1はケ−スであり、濾過水出口111を有するケ−ス本体11と 原水入口121を有するキャップ12とにより構成してある。2は中空糸膜(一端 を開口し、他端を閉塞した中空糸膜の束、またはU字状に曲げた中空糸膜の束) であり、束状でケ−ス1内に収容し、一端側を注型樹脂3でケ−ス本体11に固 定して中空糸膜2の開口端21を注型樹脂3の上面側に開通させてある。この注 型樹脂3によりケ−ス1内が濾過水室41と原水室42とに仕切られている。 An embodiment of the present invention will be described below with reference to the drawings. In FIG. 1, reference numeral 1 denotes a case, which is composed of a case body 11 having a filtered water outlet 111 and a cap 12 having a raw water inlet 121. Reference numeral 2 denotes a hollow fiber membrane (a bundle of hollow fiber membranes having one end opened and the other end closed, or a bundle of hollow fiber membranes bent in a U-shape), which is housed in a case 1 in a bundle, One end of the hollow fiber membrane 2 is fixed to the case body 11 with the casting resin 3, and the open end 21 of the hollow fiber membrane 2 is opened to the upper surface side of the casting resin 3. The casting resin 3 divides the inside of the case 1 into a filtered water chamber 41 and a raw water chamber 42.
【0012】 5は中空糸膜の所定本数ごとに被せたシ−ト状繊維活性炭であり、所定本数の 中空糸膜(中空糸膜群)の両側に添付し、下端側を結着してある。これら両側の シ−ト状繊維活性炭の巾両端は結着してもよいが開放させておくこともできる。 6は中空糸膜群間に介在させた網状流路材であり、ポリエチレン、ポリプロピレ ン、ナイロン、ポリサルホン等の網を使用できる。 この網状流路材6の上端部並びに上記シ−ト状繊維活性炭5の上端部は注型樹 脂3内に埋め込んでもよい。Reference numeral 5 is a sheet-like activated carbon fiber covering a predetermined number of hollow fiber membranes, which is attached to both sides of a predetermined number of hollow fiber membranes (hollow fiber membrane group) and is bound at the lower end side. .. Both ends of the width of the sheet-like activated carbon on both sides may be bound, but may be left open. Reference numeral 6 is a mesh channel material interposed between the hollow fiber membrane groups, and a mesh of polyethylene, polypropylene, nylon, polysulfone or the like can be used. The upper end of the reticulated channel material 6 and the upper end of the sheet-like fiber activated carbon 5 may be embedded in the casting resin 3.
【0013】 上記において、シ−ト状繊維活性炭5には、抗菌性粉末51、例えば、銅,銀 ,亜鉛,キトサン等の粉末を適当量付着させることもできる。 上記において、中空糸膜束内に網状流路材を、同心円状,渦巻き状,平行スリ ット状の原液通路間隙を形成するように介在させ、この網状流路材により分けら れた各中空糸膜群にシ−ト状繊維活性炭を被せてもよい。In the above, an appropriate amount of antibacterial powder 51, for example, powder of copper, silver, zinc, chitosan or the like can be attached to the sheet-like fiber activated carbon 5. In the above description, a mesh channel material is interposed in the hollow fiber membrane bundle so as to form a concentric circular, spiral, or parallel slit-shaped stock solution passage gap, and each of the hollows separated by the mesh channel material. The yarn film group may be covered with the sheet-like fiber activated carbon.
【0014】 上記において、シ−ト状繊維活性炭の密度は、膜の単位面積に対して必要な所 定の活性炭表面積を確保できるように定めるが、全シ−ト状繊維活性炭の総面積 が広いので、その密度を粗にでき、シ−ト状繊維の流路抵抗を充分に小さくでき る。 上記の実施例においては、膜に中空糸膜を使用しているが、この膜に代え、2 枚の平膜を袋状に、袋内部を濾過水通路とするように形成し、これをスパイラル 状に巻回したもの、多数枚の袋を積層したもの等を使用することもできる。In the above description, the density of the sheet-like fiber activated carbon is determined so that a required surface area of the activated carbon required per unit area of the membrane can be secured, but the total area of all sheet-like fiber activated carbon is wide. Therefore, the density can be made coarse and the flow path resistance of the sheet fiber can be made sufficiently small. In the above embodiments, a hollow fiber membrane is used as the membrane, but instead of this membrane, two flat membranes are formed into a bag shape and the inside of the bag is used as a filtered water passage, and this is used as a spiral. It is also possible to use a roll wound into a shape, a stack of a large number of bags, or the like.
【0015】[0015]
本考案の膜モジュ−ルは上述した通り、原水中の活性炭を吸着除去するための 活性炭を、繊維状とし、これを織成によりシ−トにして膜の原水側表面に被せた 構成であり、膜表面での原水流速が原水入口に較べて著しく小であり、しかも、 活性炭自体が流体通過抵抗の小さい繊維織成形態であるから、原水供給圧を殆ど 低下させること無く膜表面に作用させ得、膜間有効差圧を高くでき、高濾過流量 を保持できる。 As described above, the membrane module of the present invention has a structure in which the activated carbon for adsorbing and removing the activated carbon in the raw water is made into a fibrous shape, which is woven to form a sheet and covered on the raw water side surface of the membrane. Since the flow velocity of raw water on the membrane surface is significantly smaller than that of the raw water inlet, and the activated carbon itself is a fiber woven form with low fluid passage resistance, it can be applied to the membrane surface with almost no decrease in raw water supply pressure. As a result, the effective transmembrane pressure can be increased, and a high filtration flow rate can be maintained.
【0016】 また、原水入口から原水室に至る間にエア−流れに対し実質的に抵抗として作 用するものが存在せず、原水入口から原水室内にエア圧をそのまま作用させるこ とができるから、エアリ−クテストを容易に行うことができる。In addition, since there is nothing that substantially acts as a resistance to the air flow from the raw water inlet to the raw water chamber, the air pressure can be directly applied from the raw water inlet to the raw water chamber. The air leak test can be easily performed.
【0017】 更に、原水室内の水道水(原水)が消毒剤を含有したままの状態であり、通水 停止中での原水室内での雑菌の繁殖をよく抑制でき、特に、シ−ト状繊維活性炭 に抗菌性粉末を付着させておけば、その雑菌繁殖をより効果的に防止できるから 、活性炭の吸着性能を長期にわたって保持でき、悪臭の発生を排除できる。Further, since the tap water (raw water) in the raw water chamber still contains the disinfectant, it is possible to well suppress the growth of various bacteria in the raw water chamber while the water flow is stopped. If the antibacterial powder is attached to the activated carbon, the proliferation of various bacteria can be prevented more effectively, so that the adsorption performance of the activated carbon can be maintained for a long period of time and the generation of malodor can be eliminated.
【図1】本考案の実施例を示す断面説明図である。FIG. 1 is an explanatory sectional view showing an embodiment of the present invention.
1 ケ−ス 2 膜 42 原水室 5 シ−ト状繊維活性炭 1 case 2 membrane 42 raw water chamber 5 sheet-like fiber activated carbon
Claims (2)
れぞれ有するケ−ス内に濾過膜を設け、原水室側におい
て濾過膜をシ−ト状繊維活性炭で覆ったことを特徴とす
る膜モジュ−ル。1. A filter membrane is provided in a case having a raw water inlet at one end and a filtered water outlet at the other end, and the filter membrane is covered with sheet-like activated carbon on the raw water chamber side. Membrane module to do.
れている請求項1記載の膜モジュ−ル。2. The membrane module according to claim 1, wherein antibacterial powder is attached to the sheet-shaped activated carbon.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3852592U JPH0593593U (en) | 1992-05-11 | 1992-05-11 | Membrane module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3852592U JPH0593593U (en) | 1992-05-11 | 1992-05-11 | Membrane module |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0593593U true JPH0593593U (en) | 1993-12-21 |
Family
ID=12527697
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3852592U Pending JPH0593593U (en) | 1992-05-11 | 1992-05-11 | Membrane module |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0593593U (en) |
-
1992
- 1992-05-11 JP JP3852592U patent/JPH0593593U/en active Pending
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP3655365B1 (en) | Method and device for removing particles from waste water | |
| US5480553A (en) | Hollow fiber membrane module | |
| RU87365U1 (en) | LIQUID CLEANING CARTRIDGE (OPTIONS) | |
| KR102138010B1 (en) | Composit filter of water purifier | |
| US4826519A (en) | Multilayer filter element | |
| JPS599203B2 (en) | Oil/water separation method by coarse graining | |
| JP2005535425A (en) | Filter to reduce white blood cells from blood products | |
| KR102594953B1 (en) | Filter for water purifier and method for making the filter media | |
| RU60874U1 (en) | CARTRIDGE FILTER ELEMENT (OPTIONS) | |
| KR20090006213A (en) | Pleated Filter Cartridge | |
| JPH0593593U (en) | Membrane module | |
| DK2510992T3 (en) | Filter material for cleaning a fluid | |
| JP7309389B2 (en) | Filtration method, filter body, filtration device, and filter laminate | |
| JP2003047809A (en) | Filter element | |
| JP4107724B2 (en) | Spiral membrane element | |
| JPH09187605A (en) | Pleat cartridge filter and fitter for power plant condensate system using the same | |
| JP2002102845A (en) | Water purifier | |
| JPH0244563B2 (en) | ||
| JP2505757Y2 (en) | Filtration filter | |
| JP3951457B2 (en) | Water purification cartridge and water purifier using the same | |
| JPH0351032Y2 (en) | ||
| JPH0533885U (en) | Water purifier | |
| WO2014025689A1 (en) | Filter for a water purifier, and a water purifier including the same | |
| JP3130997B2 (en) | Hollow fiber membrane module | |
| JP3164661B2 (en) | Honeycomb structure filter |