JP2009066534A - Pleated filter cartridge for liquid - Google Patents
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Abstract
Description
この発明は、液体濾過用フィルターとして使用し得る耐圧性を有する高分子系ナノファイバー不織布を使用した新規プリーッ式フィルターカートリッジに関する。 The present invention relates to a novel pleated filter cartridge using a polymer nanofiber nonwoven fabric having pressure resistance that can be used as a filter for liquid filtration.
高分子系ナノファイバー不織布は、通常繊維間の結合力が弱いので、粘性が低く大きな差圧が発生しない気体濾過用フィルターとして知られている。しかし、流体に対する耐圧性が要求される液体用フィルターとして産業上使用し得る耐圧性を有するフィルターは知られていない。 Polymer nanofiber nonwoven fabrics are generally known as gas filtration filters that have a low viscosity and do not generate a large differential pressure because of their weak binding strength between fibers. However, there is no known filter having pressure resistance that can be used industrially as a liquid filter requiring pressure resistance against a fluid.
液体用プリーッ式フィルターカートリッジ、特に完全性を保証するような精密濾過膜(PTFE膜やPE膜)を使用したフィルターカートリッジにおいては、メインの濾過材となる精密濾過膜を保護する目的で、濾過材の前後にサポート材が用いられている。このサポート材としては、強度が高いほどサポート効果が上がるので、スパンボンド(SB)のような繊維径の太い不織布が使用されていた。 In the case of a pleated filter cartridge for liquids, especially in a filter cartridge using a microfiltration membrane (PTFE membrane or PE membrane) that guarantees completeness, the filter media is used for the purpose of protecting the microfiltration membrane that is the main filter medium. Support material is used before and after. As this support material, since the support effect increases as the strength increases, a nonwoven fabric having a large fiber diameter such as spunbond (SB) has been used.
高分子系ナノファイバー不織布は、この膜フィルター並みの濾過精度が期待されるので、精密濾過材としてナノファイバー不織布が使用できれば、膜フィルターよりも空隙率を上げることが可能となるので、圧力損失を小さくできるという点で有利である。 The polymer nanofiber nonwoven fabric is expected to have the same filtration accuracy as this membrane filter, so if the nanofiber nonwoven fabric can be used as a precision filter material, the porosity can be increased more than the membrane filter. This is advantageous in that it can be made smaller.
上記のような利点が期待されることから、高分子系ナノファイバー不織布の両面をサポート材で挟持した積層体を液体用プリーッ式フィルターとすることを試みたが、プリーツ加工時に濾材にピンホールが発生するとか、膜フィルターのサポート材として通常使用される強度の強い、繊維径の太い、粗いサポート材を二次側にすると、液圧で高分子系ナノファイバー不織布が目開きし、濾過精度が低下することが判明した。 Since the above advantages are expected, an attempt was made to use a laminated body in which both sides of the polymer nanofiber nonwoven fabric were sandwiched between support materials as a pleated filter for liquids. If a high-strength, large-fiber-diameter, coarse support material that is normally used as a support material for membrane filters is made secondary, the polymer nanofiber nonwoven fabric will open with hydraulic pressure, and the filtration accuracy will increase. It turned out to be reduced.
これを解決するため、従来膜フィルターのサポート材としては、目の粗いスパンボンド不織布(SB)よりは、サポート材として効果的でなかった目の細かいサポート材を図1に示すように流体流出側である、フィルターの二次側とすることによって、高分子系ナノファイバー不織布の目開きが低減することを見出したが、このフィルターは、完全性及び耐圧性能は要求水準に達しないことが判明した。 In order to solve this problem, as a support material of a conventional membrane filter, a fine support material that is not effective as a support material than a coarse spunbond nonwoven fabric (SB) is used as shown in FIG. The secondary side of the filter was found to reduce the opening of the polymer nanofiber nonwoven fabric, but it was found that this filter did not reach the required level of integrity and pressure resistance. .
この発明は、このような点に着目してなされたものであり、完全性及び耐圧性が要求水準に達し、且つ安定して作製し得る、高分子系ナノファイバー不織布を使用した液体用プリーッ式フィルターカートリッジを提供することを目的とする。 The present invention has been made paying attention to such a point, and the pleated type for liquids using a polymer nanofiber nonwoven fabric that can achieve a required level of integrity and pressure resistance and can be stably produced. An object is to provide a filter cartridge.
上記目的を達成するため、本発明者は、鋭意研究の結果、図1に示す二次側を繊維径1〜10μmのサポート材にすると共に、挟持する両サポート材と高分子系ナノファイバー不織布とをラミネート加工により圧着一体化することにより、完全性及び耐圧性が要求水準に達した液体用プリーッ式フィルターカートリッジを安定して作製し得ることを見出し、本発明に到達した。 In order to achieve the above object, the present inventor, as a result of earnest research, made the secondary side shown in FIG. 1 a support material having a fiber diameter of 1 to 10 μm, and sandwiched both support materials and a polymer nanofiber nonwoven fabric. It has been found that a liquid pleated filter cartridge having the required integrity and pressure resistance can be stably produced by laminating and bonding the laminate by laminating, and the present invention has been achieved.
即ち本発明は、高分子系ナノファイバー不織布をサポート材で挟持して、ラミネート加工により該両サポート材と前記ナノファイバー不織布とを圧着一体化してなり、前記二次側は繊維径1〜10μmのサポート材で形成したことを特徴とする。 That is, the present invention is formed by sandwiching a polymeric nanofiber nonwoven fabric with a support material, and laminating the support material and the nanofiber nonwoven fabric, and the secondary side has a fiber diameter of 1 to 10 μm. It is made of support material.
サポート材に高分子系ナノファイバー不織布を積層した濾過材とサポート材とを、ラミネート加工により圧着一体化するのが好ましい(請求項2)。
カレンダリングによるラミネート加工により、濾材空隙率50〜80%に圧着一体化するのが好ましい(請求項3)。
It is preferable that the filter medium obtained by laminating the polymer nanofiber nonwoven fabric on the support material and the support material are pressure-bonded and integrated by laminating (Claim 2).
It is preferable to press-fit and integrate to a filter medium porosity of 50 to 80% by laminating by calendering.
前記ラミネート加工は、エンボスロールによるラミネート加工であるのが、圧着面積が小さく、全体の空隙率を高く保持できることから好ましい(請求項4)。 The laminating process is preferably an embossing roll laminating process because the area of pressure bonding is small and the overall porosity can be kept high.
前記エンボスロールにより、非圧縮部の周りに閉鎖形状若しくは隣接する非圧縮部が連通する連通部を持つ殆ど閉鎖した形状の圧着部を多数形成するのが好ましい(請求項5)。前記閉鎖若しくは殆ど閉鎖された非圧縮部の単一面積が、20mm2以下であるのが好ましい(請求項6)。 It is preferable that the embossing rolls form a large number of pressure-bonding parts having a closed shape around the non-compressed part or a substantially closed shape having a communicating part communicating with the adjacent non-compressed part (Claim 5). It is preferable that a single area of the non-compressed portion which is closed or almost closed is 20 mm 2 or less (Claim 6).
前記隣接する非圧縮部が連通する複数の連通部は、連通方向の同一直線状に無いのが好ましい(請求項7)。連通部が2以上ある場合に、少なくとも2つでも同一直線上に無いのが好ましい。
前記エンボスロールによるラミネート加工により、圧着面積率を全体の20〜60%、圧着部の濾材空隙率を10〜70%、とするのが好ましい(請求項8)。
It is preferable that the plurality of communicating portions with which the adjacent non-compressed portions communicate are not in the same straight line in the communicating direction (Claim 7). When there are two or more communicating portions, it is preferable that at least two communicating portions are not on the same straight line.
By laminating with the embossing roll, it is preferable that the pressure-bonding area ratio is 20 to 60% of the whole and the filter medium porosity of the pressure-bonding portion is 10 to 70%.
前記サポート材は、高分子系ナノファイバー不織布と同一かそれよりも高い温度で融解するのが、溶着部プレートへの刺さりこみ強度が高められるので、プリーッフィルター端面の熱溶着加工時の封止を完全に行うことができることから好ましい(請求項9)。 The support material melts at a temperature equal to or higher than that of the polymer nanofiber nonwoven fabric, which increases the penetration strength into the weld plate, so that the end face of the pleated filter is sealed during the heat welding process. Is preferable because it can be performed completely (claim 9).
前記ナノファイバー不織布の繊維径は5〜1000nmであり、目付は0.2〜10g/m2であるのが好ましい(請求項10)。 The nanofiber nonwoven fabric preferably has a fiber diameter of 5 to 1000 nm and a basis weight of 0.2 to 10 g / m 2 (claim 10).
前記一次側のサポート材は、繊維径が10〜30μmであり、前記二次側のサポート材は、繊維径は1〜10μmであるのが好ましい(請求項11)。前記一次側及び二次側のサポート材の目付が、10〜100g/m2であるのが好ましい(請求項12)。 The primary side support material preferably has a fiber diameter of 10 to 30 μm, and the secondary side support material preferably has a fiber diameter of 1 to 10 μm. The basis weight of the primary side and secondary side support materials is preferably 10 to 100 g / m 2 (claim 12).
本発明によれば、従来液体用プリーッ式フィルターの精密濾過材として使用し得ないと考えられていた高分子系ナノファイバー不織布を、耐圧性を有する液体用プリーッ式フィルターの精密濾過材とすることに初めて成功したものであって、膜フィルターよりも空隙率の大きいフィルターとすることが可能となり、圧力損失の低下が期待されるほか、コストダウンも期待されるという絶大な効果を奏する。 According to the present invention, a polymer nanofiber nonwoven fabric, which has been conventionally considered to be unusable as a precision filter material for a liquid pleated filter, is used as a pressure proof liquid pleated filter precision filter material. This is the first successful method, and it is possible to make a filter having a larger porosity than a membrane filter, and it is expected that the pressure loss is reduced and cost reduction is also expected.
本発明の効果の原因は、二次側に目の細かいサポート材を使用し、ナノファイバー不織布と表裏のサポート材とを、ラミネート加工により圧着一体化したことにある。本発明で圧着一体化というのは、各層が自由には移動しないが、ナノファイバー不織布が溶融しない程度にフィルターの一部若しくは全部に圧着することを意味する。 The cause of the effect of the present invention lies in that a fine support material is used on the secondary side, and the nanofiber nonwoven fabric and the front and back support materials are bonded together by lamination. In the present invention, the pressure-bonding integration means that each layer does not move freely, but is pressure-bonded to a part or all of the filter to such an extent that the nanofiber nonwoven fabric does not melt.
次に、本発明の実施の形態を説明する。 Next, an embodiment of the present invention will be described.
高分子系ナノファイバー不織布をサポート材で挟持して、ラミネート加工により圧着して一体化するには、サポート材にナノファイバー不織布を積層した濾過材を用いて、これとナノファイバー不織布の表層を保護するサポート材とを圧着一体化するのが良い。 In order to sandwich a polymer nanofiber nonwoven fabric with a support material and compress it by laminating and integrating it, a filter material in which the nanofiber nonwoven fabric is laminated on the support material is used to protect the surface layer of the nanofiber nonwoven fabric. It is better to press-fit the supporting material to be integrated.
液体用プリーッ式フィルターカートリッジの二次側は、1〜10μmの繊維径を有するサポート材とする。このようなものとしてはメルトブロー(MB)不織布が挙げられる。このような繊維径のサポート材を二次側に使用することによって、ナノファイバー不織布の目開きを効果的に防止することができる。 The secondary side of the liquid pleated filter cartridge is a support material having a fiber diameter of 1 to 10 μm. Examples of such a material include a melt blown (MB) nonwoven fabric. By using a support material having such a fiber diameter on the secondary side, the opening of the nanofiber nonwoven fabric can be effectively prevented.
カレンダリングによるラミネート加工により、濾材空隙率50〜80%に圧着一体化するのが好ましい。濾材空隙率が少なすぎると、ΔPが上昇するし、多すぎると、耐圧性能が低下する。 It is preferable to compress and integrate the filter medium with a porosity of 50 to 80% by laminating by calendering. If the filter medium porosity is too small, ΔP will increase, and if it is too high, pressure resistance will decrease.
前記カレンダリングによるラミネート加工は、通常のラミネート加工で行えばよいが、高分子系ナノファイバー不織布が溶融しない程度に圧着する必要がある。 Lamination by calendering may be performed by ordinary lamination, but it is necessary to press-bond to such an extent that the polymer nanofiber nonwoven fabric does not melt.
エンボスロールによるラミネート加工を行って、圧着面積率を全体の20〜60%、圧着部の濾材空隙率を10〜70%とすると、ΔPをあまり上昇させないで、耐圧性能を高めることができることから好ましい。これは、通常のエンボス加工のように、ナノファイバー不織布は溶融させない。尚、圧着面積率(%)は、図2に示すように、圧着面積率(%)=(B 部面積)/(A 部面積+B 部面積)×100から求められる。 Lamination with an embossing roll is preferable because the pressure-bonding area ratio is 20 to 60% of the whole, and the filter medium porosity of the pressure-bonding part is 10 to 70%, because the pressure-resistant performance can be improved without significantly increasing ΔP. . This does not melt the nanofiber nonwoven fabric as in normal embossing. The crimping area ratio (%) is obtained from the crimping area ratio (%) = (B part area) / (A part area + B part area) × 100 as shown in FIG.
エンボスロールにより、非圧縮部の周りに閉鎖形状若しくは隣接する非圧縮部が連通する連通部を持つ殆ど閉鎖した形状の圧着部を多数形成する(多数の非圧着部が互いに独立するように)方が、圧着面積が低減でき、全体の濾材空隙率を高く保って、閉鎖形状若しくは殆ど閉鎖した形状内のナノファイバー不織布の目開きを防ぎ、耐圧性能を向上させることができる。閉鎖形状としては、多角形、円形、楕円形等が挙げられるが特に限定されない。六角形、四角形、三角形などとすれば、同形状のエンボス部を多数連設できるので好ましい。
図2に示すように、前記閉鎖若しくは殆ど閉鎖された非圧縮部の個々の面積(A部)が、20mm2以下であるのが好ましい。また、前記隣接する非圧縮部が連通する複数の連通部(開口部)は、図3Aのa及びbに示すように、連通方向の同一直線状にあると、連通方向の目開きが起きる。図3Bに示すように、連通部が連通方向の同一直線上に無い場合は、目開きは防止される。
By embossing roll, forming many closed parts with closed shape around the non-compressed part or communication parts where the adjacent non-compressed parts communicate with each other (so that many non-compressed parts are independent from each other) However, the pressure-bonding area can be reduced, the overall filter medium porosity can be kept high, the opening of the nanofiber nonwoven fabric in the closed shape or the almost closed shape can be prevented, and the pressure resistance can be improved. Examples of the closed shape include, but are not limited to, a polygon, a circle, and an ellipse. A hexagonal shape, a quadrangular shape, a triangular shape, or the like is preferable because a large number of embossed portions having the same shape can be provided continuously.
As shown in FIG. 2, the individual area (A part) of the closed or almost closed non-compressed part is preferably 20 mm 2 or less. Further, when the plurality of communicating portions (openings) communicating with the adjacent non-compressed portions are in the same straight line in the communicating direction, as shown in a and b of FIG. 3A, opening in the communicating direction occurs. As shown in FIG. 3B, when the communication portions are not on the same straight line in the communication direction, the opening is prevented.
前記サポート材は、高分子系ナノファイバー不織布と同一かそれよりも高い温度で融解する材料とするのが良い。そのためには、サポート材の融点が同一かそれよりも高い融点のものを使用すればよいが、サポート材の融点がナノファイバー不織布より若干低くとも、繊維径が太い関係でナノファイバー不織布よりも同一かそれよりも高い温度で融解すれば差し支えない。このようなサポート材を使用すれば、プリーッフィルター端面の熱溶着加工時の封止を完全に行うことができる。 The support material may be a material that melts at a temperature equal to or higher than that of the polymer nanofiber nonwoven fabric. To that end, it is sufficient to use a support material having the same melting point or higher melting point, but even if the support material has a slightly lower melting point than the nanofiber nonwoven fabric, it is the same as the nanofiber nonwoven fabric due to the large fiber diameter. Or it can be melted at a higher temperature. If such a support material is used, it is possible to completely seal the end face of the prep filter during the heat welding process.
前記ナノファイバー不織布の繊維径は、5〜1000nmであり、目付は0.2〜10g/m2とするのが好ましい。繊維径が小さすぎるとポアサイズが安定しないし、大きすぎると精密濾過材として不適当となる。
前記二次側のサポート材の繊維径は1〜10μmであり、前記一次側のサポート材は、繊維径が10〜30μmとするのが好ましい。
Fiber diameter of the nanofiber nonwoven fabric is 5 to 1000 nm, a basis weight is preferably between 0.2 to 10 g / m 2. If the fiber diameter is too small, the pore size will not be stable, and if it is too large, it will be inappropriate as a microfiltration material.
The fiber diameter of the support material on the secondary side is preferably 1 to 10 μm, and the fiber diameter of the support material on the primary side is preferably 10 to 30 μm.
前記一次側及び二次側のサポート材の目付は、10〜100g/m2であるのが好ましい。目付が小さすぎると、ナノファイバー不織布が露出する場合が生じるからである。 The basis weight of the primary side and secondary side support materials is preferably 10 to 100 g / m 2 . This is because if the basis weight is too small, the nanofiber nonwoven fabric may be exposed.
高分子系ナノファイバー不織布としては、電解紡糸法で形成したものが好適に使用されるが、例えば、PA、PVA、PAN、PVDF、PES、PS、PET、PU、PP等の単独若しくは複数の樹脂から製造されたものが挙げられる。
サポート材としては、例えば、PA、PVA、PVDF、PES、PS、PET、PU、PP、ガラス、セラミックス、カーボン等を好適に使用することができる。
As the polymer nanofiber nonwoven fabric, those formed by electrospinning are preferably used. For example, single or plural resins such as PA, PVA, PAN, PVDF, PES, PS, PET, PU, PP, etc. Manufactured from the above.
As the support material, for example, PA, PVA, PVDF, PES, PS, PET, PU, PP, glass, ceramics, carbon, and the like can be suitably used.
次に実施例、比較例を挙げて本発明を更に説明するが、本発明はこれら実施例に限定されない。尚実施例、比較例で使用した高分子系ナノファイバー不織布は、電解紡糸法で形成したものを使用した。
比較例 1
スパンボンド(SB)上に積層した高分子系ナノファイバー不織布(表中●印)に次表1に記載のサポート材を単に積層して、液体用プリーッ式フィルターカートリッジを作製し、フィルター成形性、完全性、耐圧性及びΔP(圧力損失)を測定した。結果を次表1に示す。
EXAMPLES Next, although an Example and a comparative example are given and this invention is further demonstrated, this invention is not limited to these Examples. In addition, what was formed by the electrospinning method was used for the polymeric nanofiber nonwoven fabric used by the Example and the comparative example.
Comparative Example 1
By simply laminating the support material described in the following table 1 on the polymer nanofiber nonwoven fabric (● in the table) laminated on the spunbond (SB), a pleated filter cartridge for liquid is produced, and the filter moldability, Integrity, pressure resistance and ΔP (pressure loss) were measured. The results are shown in Table 1 below.
上記結果より、二次側に目の細かいメルトブロー繊維(MB)を使用したほうが(c)、フィルターの耐圧性が向上する。しかしこの構造でも、目標耐圧性能(0.55MPa×10回パルス負荷)には達していない。 From the above results, the pressure resistance of the filter is improved by using fine blown fibers (MB) on the secondary side (c) (c). However, even with this structure, the target pressure resistance performance (0.55 MPa × 10 times pulse load) has not been achieved.
実施例 1
スパンボンド(SB)上に積層した高分子系ナノファイバー不織布(表中●印)に次表2に記載のサポート材を積層して、カレンダリング(d ,e)及びエンボスロール(f)によるラミネート加工により一体化した後、液体用プリーッ式フィルターカートリッジを作製し、フィルターの成形性、完全性、耐圧性及びΔPを測定した。結果を次表2に示す。
Example 1
Laminate the support materials listed in the following table 2 on the polymer nanofiber nonwoven fabric (marked with ● in the table) laminated on the spunbond (SB), and laminate by calendering (d, e) and embossing roll (f) After integration by processing, a pleated filter cartridge for liquid was prepared, and the moldability, integrity, pressure resistance and ΔP of the filter were measured. The results are shown in Table 2 below.
上記実施例に使用したfを図4に示す。図4に示すように、f(圧着部の比率:約30%)の●に圧力が掛かった場合、矢印の方向に繊維が目開きすると考えられる。
上記したように、fは、目開きする範囲が小さいため、高い耐圧性能を有していると考えられる。また、eが一番高い耐圧性能であったのは、全体が三層一体化していて目開きしにくいためと考えられる、しかし、カレンダリングによるラミネート品は、ΔPが上昇する。
比較例 2
スパンボンド(SB)上に積層した高分子系ナノファイバー不織布(表中●印)にサポート材として次表3に記載のカレンダー加工したMB不織布を積層して、液体用プリーッ式フィルターカートリッジを作製し、フィルター成形性、完全性、耐圧性及びΔPを測定した。結果を次表3に示す。
実施例 2
次に、上記フィルターを使用して、耐圧性能試験と流量特性測定を行った。試験条件は、次の通りである。
(耐圧性能試験条件)
目詰まり物質 :牛乳
試験圧力 :正圧(0.2、0.3、0.4、0.55MPa)
温度 :常温
流量 :10〜13L/min
インターバル :加圧10秒、休止5秒
(耐圧性能試験方法)
(1)
牛乳にてフィルターを目詰まりさせる。
(2)
上記試験流量、所定圧力で脈動をかける。
(完全性確認試験)
ディフュージョンテストにて確認した。
(3)
完全に水で濡らしたフィルターをハウジングにセットし、0.02MPaに加圧する。
(4)
二次側に押し出されてきた気体の流量を測定する。
実施例 3
フィルターをハウジングにセットし、フィルターのIN側及びOUT側に圧力計を設置し、各流量時におけるIN側、OUT側の圧力を測定しその差を差圧(MPa)として記録した。結果を次表5に示す。
(流量特性の測定条件)
流体 :精製水
温度 :常温
流量 :10,20,30,40L/min
フィルターサイズ:250mm
実施例 4
次表6に記載の高分子系ナノファイバー不織布及びサポート材から作製したプリーッをプレートに熱溶着加工をして、完全性を確認した。結果を次表6及び図5に示す。
フィルター(2)は、一次側サポート材にナノファイバー不織布層と同じPAを使用しているので、融点が同じであるから、プレート端面からの発泡は生じない。
次に、上記実施例及び比較例で使用したプリーッフィルターの詳細な構造を示す。
bの詳細な構造
cの詳細な構造
dの詳細な構造
eの詳細な構造
fの詳細な構造
gの詳細な構造
FIG. 4 shows f used in the above embodiment. As shown in FIG. 4, it is considered that the fibers open in the direction of the arrow when pressure is applied to the mark ● of f (compression bonding ratio: about 30%).
As described above, f is considered to have a high pressure resistance because the opening range is small. The reason why e is the highest pressure resistance performance is considered to be that the entire three layers are integrated and difficult to open, but ΔP is increased in the laminate by calendering.
Comparative Example 2
The polymer nanofiber non-woven fabric laminated on spunbond (SB) (● in the table) is laminated with the calendared MB non-woven fabric listed in the following table 3 as a support material to produce a pleated filter cartridge for liquid. The filter moldability, completeness, pressure resistance and ΔP were measured. The results are shown in Table 3 below.
Example 2
Next, the pressure resistance performance test and the flow rate characteristic measurement were performed using the filter. The test conditions are as follows.
(Pressure performance test conditions)
Clogging substance: Milk Test pressure: Positive pressure (0.2, 0.3, 0.4, 0.55 MPa)
Temperature: Normal temperature Flow rate: 10-13 L / min
Interval: pressurization 10 seconds, rest 5 seconds (pressure resistance performance test method)
(1)
Clog the filter with milk.
(2)
Pulsating at the above test flow rate and predetermined pressure.
(Completeness confirmation test)
Confirmed by diffusion test.
(3)
A completely wetted filter is set in the housing and pressurized to 0.02 MPa.
(4)
The flow rate of the gas pushed out to the secondary side is measured.
Example 3
The filter was set in the housing, pressure gauges were installed on the IN side and OUT side of the filter, the pressure on the IN side and OUT side at each flow rate was measured, and the difference was recorded as the differential pressure (MPa). The results are shown in Table 5 below.
(Measurement conditions for flow characteristics)
Fluid: Purified water temperature: Room temperature Flow rate: 10, 20, 30, 40 L / min
Filter size: 250mm
Example 4
The pleats prepared from the polymer nanofiber nonwoven fabric and the support material shown in the following Table 6 were heat-welded to the plate, and the integrity was confirmed. The results are shown in the following Table 6 and FIG.
Since the filter (2) uses the same PA as the nanofiber nonwoven fabric layer for the primary side support material, the melting point is the same, so foaming from the end face of the plate does not occur.
Next, the detailed structure of the pre-filter used in the above examples and comparative examples is shown.
Detailed structure of b
c detailed structure
d detailed structure
e detailed structure
Detailed structure of f
Detailed structure of g
Claims (12)
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| JP2007238134A JP5379935B2 (en) | 2007-09-13 | 2007-09-13 | Pleated filter cartridge for liquid |
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| JP2007238134A JP5379935B2 (en) | 2007-09-13 | 2007-09-13 | Pleated filter cartridge for liquid |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012148482A (en) * | 2011-01-19 | 2012-08-09 | Kurita Water Ind Ltd | Composite membrane, method for producing the same, adsorbing filter and method for treating fluid |
| JP2012149174A (en) * | 2011-01-19 | 2012-08-09 | Kurita Water Ind Ltd | Composite membrane, method for producing the same, adsorbing filter and method for treating liquid |
| JP2013535314A (en) * | 2010-06-30 | 2013-09-12 | アモグリーンテック カンパニー リミテッド | Filter medium for liquid filter using electroradiated nanofiber web, manufacturing method thereof, and liquid filter using the same |
| US10828587B2 (en) | 2015-04-17 | 2020-11-10 | Hollingsworth & Vose Company | Stable filter media including nanofibers |
| US11452959B2 (en) | 2018-11-30 | 2022-09-27 | Hollingsworth & Vose Company | Filter media having a fine pore size distribution |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2013535314A (en) * | 2010-06-30 | 2013-09-12 | アモグリーンテック カンパニー リミテッド | Filter medium for liquid filter using electroradiated nanofiber web, manufacturing method thereof, and liquid filter using the same |
| JP2012148482A (en) * | 2011-01-19 | 2012-08-09 | Kurita Water Ind Ltd | Composite membrane, method for producing the same, adsorbing filter and method for treating fluid |
| JP2012149174A (en) * | 2011-01-19 | 2012-08-09 | Kurita Water Ind Ltd | Composite membrane, method for producing the same, adsorbing filter and method for treating liquid |
| US10828587B2 (en) | 2015-04-17 | 2020-11-10 | Hollingsworth & Vose Company | Stable filter media including nanofibers |
| US11819789B2 (en) | 2015-04-17 | 2023-11-21 | Hollingsworth & Vose Company | Stable filter media including nanofibers |
| US11452959B2 (en) | 2018-11-30 | 2022-09-27 | Hollingsworth & Vose Company | Filter media having a fine pore size distribution |
| US11890561B2 (en) | 2018-11-30 | 2024-02-06 | Hollingsworth & Vose Company | Filter media having a fine pore size distribution |
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