JP2001340732A - Laminated filter element - Google Patents

Laminated filter element

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Publication number
JP2001340732A
JP2001340732A JP2000161529A JP2000161529A JP2001340732A JP 2001340732 A JP2001340732 A JP 2001340732A JP 2000161529 A JP2000161529 A JP 2000161529A JP 2000161529 A JP2000161529 A JP 2000161529A JP 2001340732 A JP2001340732 A JP 2001340732A
Authority
JP
Japan
Prior art keywords
filtration
filter element
ptfe
polyolefin
layer
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
JP2000161529A
Other languages
Japanese (ja)
Other versions
JP4495831B2 (en
Inventor
Hajime Hiranaga
一 平永
Atsushi Sakamoto
厚志 坂本
Shuichi Tsuzuki
修一 都築
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.)
Pall Corp
Original Assignee
Pall Corp
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 Pall Corp filed Critical Pall Corp
Priority to JP2000161529A priority Critical patent/JP4495831B2/en
Publication of JP2001340732A publication Critical patent/JP2001340732A/en
Application granted granted Critical
Publication of JP4495831B2 publication Critical patent/JP4495831B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Filtering Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a laminated filter element with a simple constitution capa ble of effectively removing the solid components contained in a fluid to be filtered and the gelatinous components with diameters smaller than that of the filter pore at a most downstream side. SOLUTION: PTFE filter layers are preferably arranged on a upstream side with respect to the flow of fluid to be filtered and polyolefin filter layers are arranged on a downstream side with respect to the flow of the fluid to be filtered and at this time, the PTFE filter membrane of the larger pore diameter of a pair of the PTFE filter membranes constituting the PTFE filter layers is at least arranged on the upstream side and the PTFE filter membrane of the smaller pore diameter is arranged on the downstream side. In the composite membrane filter having such constitution, the solid components in the fluid to be filtered are separate by the PTFE filter layers and the gelatinous components in the fluid to be filtered are separated by the polyolefin filter layers.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、被濾過物質として
固形状成分と固形状成分除去用最下流側濾過膜の孔径よ
りも概ね小さい径のゲル状成分とを含有する被濾過流体
から、被濾過物質を効果的に除去することができる、積
層型フィルタエレメントに関するものである。
BACKGROUND OF THE INVENTION The present invention relates to a method for converting a fluid to be filtered from a fluid containing a solid component and a gel component having a diameter substantially smaller than the pore diameter of the most downstream filtration membrane for removing the solid component. The present invention relates to a laminated filter element capable of effectively removing a filtration substance.

【0002】[0002]

【従来の技術】製造工程中のフォトレジストには固形状
成分とゲル状成分が混在するため、これを除去する必要
がある。一般に、PTFE(ポリテトラフルオロエチレ
ン、即ち、polytetrafluoroethyl
ene)を濾過膜素材とするフィルタエレメントは、固
形状異物の濾過に有効であるが、ゲル状成分を除去する
ためには孔径の極微細化を必要とし、ろ過時に大きな運
転圧力を必要とするため、ろ過効率を低下させていた。
一方、ポリオレフィンの濾過膜を素材とするフィルタエ
レメントは、ゲル状異物の濾過に有効であることが知ら
れている。このため、従来は、PTFEを濾過膜素材と
するフィルタエレメントと、ポリエチレンに代表される
ポリオレフィンの濾過膜素材とするフィルタエレメント
をそれぞれ使用して、フォトレジストを多段濾過するこ
とにより、フォトレジスト中の固形状成分とゲル状成分
を除去している。
2. Description of the Related Art Since a solid component and a gel component are mixed in a photoresist during a manufacturing process, it is necessary to remove it. Generally, PTFE (polytetrafluoroethylene, ie, polytetrafluoroethyl)
ene) is effective for filtration of solid foreign matter, but requires extremely fine pore size to remove gel-like components, and requires a large operating pressure during filtration. Therefore, the filtration efficiency has been reduced.
On the other hand, it is known that a filter element made of a polyolefin filtration membrane is effective for filtering gel-like foreign matter. For this reason, conventionally, the filter in the photoresist is subjected to multi-stage filtration by using a filter element using PTFE as a filtration membrane material and a filter element using a polyolefin filtration membrane material represented by polyethylene, respectively. Removes solid components and gel components.

【0003】[0003]

【発明が解決しようとする課題】従来、フォトレジスト
中の異物は多段濾過によって除去されているため、濾過
工程が複雑にならざるを得ない。このため、濾過装置の
保守点検作業が困難であるのみならず、濾過効率を向上
させることが困難であった。
Conventionally, the foreign matter in the photoresist has been removed by multi-stage filtration, so that the filtration process must be complicated. For this reason, not only the maintenance and inspection work of the filtration device is difficult, but also it is difficult to improve the filtration efficiency.

【0004】本発明の目的は、被濾過流体中に混在する
固形状成分と、固形状成分除去用最下流側濾過膜の孔径
よりも概ね小さい径のゲル状成分とを、効果的に除去す
ることができる、簡単な構成の積層型フィルタエレメン
トを提供することにある。
[0004] An object of the present invention is to effectively remove solid components mixed in a fluid to be filtered and a gel component having a diameter smaller than the pore diameter of the most downstream filtration membrane for removing solid components. It is an object of the present invention to provide a laminated filter element having a simple structure that can be used.

【0005】本発明において、固形状成分除去用最下流
側濾過膜の孔径よりも概ね小さい径のゲル状成分とは固
形成分除去用最下流の濾過膜の孔径をゲル状成分が変形
して通過し得る径以下の径のゲル状成分を意味し、孔径
はJIS K 3832精密ろ過膜エレメント及びモジュ
ールのバブルポイント試験法による測定であって、フィ
ルタ全面からの気泡を認めたときのバブルポイントによ
って測定した孔径、すなわち、実質的には平均孔径を意
味する。
In the present invention, a gel component having a diameter substantially smaller than the pore diameter of the most downstream filtration membrane for removing solid components is defined as a gel component which passes through the pore diameter of the most downstream filtration membrane for removing solid components. Means a gel component having a diameter smaller than the diameter that can be obtained, and the pore size is measured by a bubble point test method of JIS K 3832 microfiltration membrane element and module, and is measured by a bubble point when air bubbles are recognized from the entire surface of the filter. Pore diameter, that is, substantially the average pore diameter.

【0006】本発明の積層型フィルタエレメントによっ
て処理される流体は、固形状成分と当該固形状成分除去
用最下流側濾過膜の孔径よりも概ね小さい径のゲル状成
分とを含有する流体である限り、フォトレジストに限定
されるものではない。
The fluid to be treated by the laminated filter element of the present invention is a fluid containing a solid component and a gel component having a diameter substantially smaller than the pore diameter of the most downstream filtration membrane for removing the solid component. However, the present invention is not limited to photoresist.

【0007】[0007]

【課題を解決するための手段】本発明の積層型フィルタ
エレメントには、PTFE濾過膜によって構成されたP
TFE濾過層と、ポリオレフィン濾過膜によって構成さ
れたポリオレフィン濾過層とを組合わせて構成された、
複合素材の、所謂、複合膜フィルタエレメントと、PT
FE濾過層とポリオレフィン濾過層とのいずれか一方を
使用して構成された、単一素材の積層型フィルタエレメ
ントとが含まれる。
According to the present invention, there is provided a laminated filter element comprising a P filter formed of a PTFE filtration membrane.
A TFE filtration layer, constituted by combining a polyolefin filtration layer constituted by a polyolefin filtration membrane,
Composite material, so-called composite membrane filter element, PT
And a single-material laminated filter element configured using one of the FE filtration layer and the polyolefin filtration layer.

【0008】本発明におけるポリオレフィン濾過膜は低
分子量から超高分子量までのポリプロピレン、ポリエチ
レン及びそれらが混合されたポリエチレン等のポリオレ
フィンから製膜された多孔膜及び/又は微多孔膜が適用
できる。また、PTFE濾過膜には多孔膜或は/及び微
多孔膜が適用できる。
As the polyolefin filtration membrane in the present invention, a porous membrane and / or a microporous membrane formed from a polyolefin such as polypropylene or polyethylene having a low molecular weight to an ultra-high molecular weight and polyethylene mixed with them can be applied. A porous membrane and / or a microporous membrane can be applied to the PTFE filtration membrane.

【0009】本発明の積層型フィルタエレメントのう
ち、複合膜フィルタに相当する構成を備えた積層型フィ
ルタエレメントは、PTFE濾過層が複数のPTFE濾
過膜を積層することによって構成され、これらの複数の
PTFE濾過膜のうち、少なくとも一対のPTFE濾過
膜が、PTFE濾過膜毎に異なる孔径を有する。
[0009] Among the laminated filter elements of the present invention, the laminated filter element having a configuration corresponding to a composite membrane filter is formed by laminating a plurality of PTFE filtration membranes on a PTFE filtration layer. At least one pair of PTFE filtration membranes among the PTFE filtration membranes has a different pore size for each PTFE filtration membrane.

【0010】この複合膜フィルタエレメントは、PTF
E濾過層を被濾過流体の流れに関して上流側に配置し、
ポリオレフィン濾過層を被濾過流体の流れに関して下流
側に配置することが望ましく、このとき、前述の少なく
とも一対のPTFE濾過膜のうち、孔径の大きい方のP
TFE濾過膜は上流側に配置され、孔径の小さい方のP
TFE濾過膜は下流側に配置される。
This composite membrane filter element is made of PTF
An E-filter layer disposed upstream with respect to the flow of the fluid to be filtered;
It is desirable to arrange the polyolefin filtration layer on the downstream side with respect to the flow of the fluid to be filtered. At this time, of the at least one pair of PTFE filtration membranes, P
The TFE filtration membrane is arranged on the upstream side, and the smaller pore size P
The TFE filtration membrane is located downstream.

【0011】ポリオレフィン濾過膜は同一孔径を有する
PTFE濾過膜よりもゲル状成分を効果的に捕捉する特
性を有し、且つ、PTFE濾過膜の孔径よりも数倍以上
大きくてもそのゲル状成分を捕捉する特性が大きくは損
なわれないから、PTFE濾過膜層の間にポリオレフィ
ン濾過膜層を配置することができる。これら二つの濾過
膜層は被濾過流体の流れに関して上流側から下流側に向
かって孔径が連続的に及び/又は段階的に小さくなるよ
うに配置する。かかる構成を有する複合膜フィルターエ
レメントにおいては被濾過流体中の固形成分とゲル状成
分の同時濾過が可能であり、従来からおこなわれてきた
様な極微小孔径PTFEろ過膜を用いることで発生して
いたろ過時の運転圧力を大きく減じることが出来る。
[0011] The polyolefin filtration membrane has a property of trapping the gel-like component more effectively than the PTFE filtration membrane having the same pore size, and even if it is several times larger than the pore size of the PTFE filtration membrane, the gel-like component is not removed. Since the capturing property is not significantly impaired, a polyolefin filtration membrane layer can be arranged between the PTFE filtration membrane layers. These two filtration membrane layers are arranged such that the pore diameter decreases continuously and / or stepwise from the upstream side to the downstream side with respect to the flow of the fluid to be filtered. In the composite membrane filter element having such a configuration, it is possible to simultaneously filter the solid component and the gel component in the fluid to be filtered, and this is caused by using an ultra-fine pore size PTFE filtration membrane as conventionally performed. The operating pressure during filtration can be greatly reduced.

【0012】本発明の複合膜フィルタエレメントは、P
TFE濾過層を一対のPTFE濾過膜を積層することに
よって構成し、ポリオレフィン濾過層を単一のポリオレ
フィン濾過膜によって構成することができる。
The composite membrane filter element of the present invention has a P
The TFE filtration layer can be constituted by laminating a pair of PTFE filtration membranes, and the polyolefin filtration layer can be constituted by a single polyolefin filtration membrane.

【0013】PTFE濾過膜は延伸法よる薄膜が適用で
きる。ポリオレフィン濾過膜は、相分離法による薄膜ま
たは延伸法よる薄膜が適用できる。ポリオレフィン濾過
膜層をゲル状成分の濾過と予備濾過の目的にも配置する
場合は、被濾過流体の流れに関して、ポリオレフィン濾
過層の上流側に不織布を配置してもよい。
As the PTFE filtration membrane, a thin film formed by a stretching method can be used. As the polyolefin filtration membrane, a thin film by a phase separation method or a thin film by a stretching method can be applied. When the polyolefin filtration membrane layer is arranged for the purpose of filtering the gel component and pre-filtration, a nonwoven fabric may be arranged on the upstream side of the polyolefin filtration layer with respect to the flow of the fluid to be filtered.

【0014】不織布は、被濾過流体の上流側から下流側
に向けて、その密度勾配を大きくなるようにしたもの
(その空隙率の勾配を小さくしたもの)、その繊維径も
細くしたもの、空隙率をある好適な一定の値に保ちなが
らその繊維径を細くしたものが好適であるが、均一密度
でその繊維径を細くしたもの或はその繊維径を一定とし
たものも適用できる。
The nonwoven fabric has a density gradient that increases from the upstream side to the downstream side of the fluid to be filtered (the gradient of the porosity is reduced), the nonwoven fabric has a reduced fiber diameter, It is preferable that the fiber diameter is reduced while maintaining the ratio at a certain preferable constant value. However, a fiber having a reduced fiber diameter at a uniform density or a fiber having a constant fiber diameter is also applicable.

【0015】本発明の複合膜フィルタエレメントは、前
述の一対のPTFE濾過膜のうち、上流側のPTFE濾
過膜の孔径を0.45から10μmとし、下流側のPT
FE濾過膜の孔径を0.05から0.45μmとし、ポ
リオレフィン濾過膜の孔径を0.1から1.0μmにす
ることができる。
According to the composite membrane filter element of the present invention, of the pair of PTFE filtration membranes, the upstream PTFE filtration membrane has a pore size of 0.45 to 10 μm and the downstream PTFE filtration membrane has a pore size of 0.45 to 10 μm.
The pore diameter of the FE filtration membrane can be 0.05 to 0.45 μm, and the pore diameter of the polyolefin filtration membrane can be 0.1 to 1.0 μm.

【0016】本発明の積層型フィルタエレメントは、P
TFEを濾過膜素材とするPTFE濾過膜を複数枚積層
させてPTFE濾過層を構成し、これらの複数のPTF
E濾過膜のうち、少なくとも一対のPTFE濾過膜が、
PTFE濾過膜毎に異なる濾過口径を有するように構成
される。ここで、前述の少なくとも一対のPTFE濾過
膜のうち、濾過口径が大きい方のPTFE濾過膜が被濾
過流体の流れに関して上流側に配置され、孔径が小さい
方のPTFE濾過膜が被濾過流体の流れに関して下流側
に配置される。
The multilayer filter element of the present invention has a P
A PTFE filtration layer is formed by laminating a plurality of PTFE filtration membranes using TFE as a filtration membrane material.
Of the E filtration membrane, at least one pair of PTFE filtration membranes,
The PTFE filtration membrane is configured to have a different filtration aperture. Here, of the at least one pair of PTFE filtration membranes, the PTFE filtration membrane having a larger filtration aperture is disposed on the upstream side with respect to the flow of the fluid to be filtered, and the PTFE filtration membrane having a smaller pore diameter is the flow of the fluid to be filtered. Is located downstream.

【0017】本発明の積層型フィルタエレメントは、ポ
リオレフィンを濾過膜素材とするポリオレフィン濾過膜
を複数枚積層させてポリオレフィン濾過層を構成し、複
数のポリオレフィン濾過膜のうち、少なくとも一対のポ
リオレフィン濾過膜が、ポリオレフィン濾過膜毎に異な
る孔径を有するように構成することができる。このと
き、前述の少なくとも一対のポリオレフィン濾過膜のう
ち、孔径が大きい方のポリオレフィン濾過膜を被濾過流
体の流れに関して上流側に配置し、孔径が小さい方のポ
リオレフィン濾過膜を被濾過流体の流れに関して下流側
に配置することが望ましい。
In the laminated filter element of the present invention, a polyolefin filtration layer is formed by laminating a plurality of polyolefin filtration membranes using polyolefin as a filtration membrane material, and at least one pair of the polyolefin filtration membranes among the plurality of polyolefin filtration membranes is used. It can be configured so that each polyolefin filtration membrane has a different pore size. At this time, among the at least one pair of polyolefin filtration membranes, the polyolefin filtration membrane having a larger pore diameter is disposed upstream with respect to the flow of the fluid to be filtered, and the polyolefin filtration membrane having the smaller pore diameter is arranged with respect to the flow of the fluid to be filtered. It is desirable to be located downstream.

【0018】なお、本発明の積層型フィルタエレメント
は、前述の複合フィルタエレメントも含めて、図3のよ
うに支持層/排水層13、14と共に濾過層を互いに重
ね合わせた状態でプリーツ状に湾曲成形し、更に、前記
積層型フィルタエレメントを、部分断面図4のように全
体として筒状の形態にすることができる。
The laminated filter element of the present invention, including the above-described composite filter element, is bent in a pleated shape in a state where the filter layers are overlapped with the support / drain layers 13 and 14 as shown in FIG. After being molded, the multilayer filter element can be formed into a cylindrical shape as a whole as shown in FIG.

【0019】プリーツの形状は、プリーツの山部の長手
方向をコア20の軸方向と平行或は直角にして隣接する
プリーツの壁面同士ができるだけ接触しないようにして
もよく、この場合は上流側の支持層/排水層13、14
を省略することも可能である。
The pleat shape may be such that the longitudinal direction of the pleated portion is parallel or perpendicular to the axial direction of the core 20 so that the wall surfaces of adjacent pleats do not contact each other as much as possible. Support layer / Drainage layer 13, 14
May be omitted.

【0020】[0020]

【発明の実施の形態】本発明の積層型フィルタエレメン
トの濾過寿命と被濾過流体の濾過後の清浄度を試験する
ため、以下のような構成を有する積層型フィルタエレメ
ントA、B、C、D、Eを制作し、以下に示す試験液を
使用して、下記の試験方法で試験を行った。 (1)積層型フィルタエレメントAはPTFE濾過層の
みからなり、このPTFE濾過層は三枚のPTFE濾過
膜を積層することによって構成された。最上流側のPT
FE濾過膜の孔径は0.1μmとし、最下流側のPTF
E濾過膜の孔径は0.05μmとし、中間のPTFE濾
過膜の孔径は0.1μmとした。 (2)積層型フィルタエレメントBはポリエチレン濾過
層のみからなり、このポリエチレン濾過層は三枚のポリ
エチレン濾過膜を積層することによって構成された。最
上流側のポリエチレン濾過膜の孔径は0.45μmと
し、最下流側のポリエチレン濾過膜の孔径を0.15μ
mとし、中間のポリエチレン濾過膜の孔径を0.45μ
mとした。 (3)積層型フィルタエレメントCは、一対のPTFE
濾過膜を積層することによって構成したPTFE濾過層
と、単一のポリエチレン濾過膜によって構成したポリエ
チレン濾過層とを積層して構成された。PTFE濾過層
を構成する一対のPTFE濾過膜のうち、上流側のPT
FE濾過膜の孔径を0.45μmとし、下流側のPTF
E濾過膜の孔径を0.1μmとした。そして、ポリエチ
レン濾過層を構成するポリエチレン濾過膜の孔径を0.
45μmとした。積層型フィルタエレメントCは、PT
FE濾過層を上流側に、ポリエチレン濾過層を下流側に
配置し、前述の試験に供された。 (4)積層型フィルタエレメントDは、一対のPTFE
濾過膜を積層することによって構成したPTFE濾過層
と、単一のポリエチレン濾過膜によって構成したポリエ
チレン濾過層とを積層して構成された。PTFE濾過層
を構成する一対のPTFE濾過膜のうち、上流側のPT
FE濾過膜の孔径を5.0μmとし、下流側のPTFE
濾過膜の孔径を0.1μmとした。そして、ポリエチレ
ン濾過層を構成するポリエチレン濾過膜の孔径を0.4
5μmとした。積層型フィルタエレメントDは、PTF
E濾過層を上流側に、ポリエチレン濾過層を下流側に配
置し、前述の試験に供された。 (5)積層型フィルタエレメントEは、一対のPTFE
濾過膜を積層することによって構成したPTFE濾過層
と、単一のポリエチレン濾過膜によって構成したポリエ
チレン濾過層とを積層して構成された。PTFE濾過層
を構成する一対のPTFE濾過膜のうち、上流側のPT
FE濾過膜の孔径を10.0μmとし、下流側のPTF
E濾過膜の孔径を0.1μmとした。そして、ポリエチ
レン濾過層を構成するポリエチレン濾過膜の孔径を0.
45μmとした。積層型フィルタエレメントEは、PT
FE濾過層を上流側に、ポリエチレン濾過層を下流側に
配置し、前述の試験に供された。 (6)被濾過流体である試験液は、フェノール樹脂をシ
ンナーに溶解し、粘度を約15mPa・s(15cP)
に調整したものを使用した。 (7)フィルタの濾過寿命を評価するために、直径47
mmのディスクで試験液を濾過し、一定時間ごとの濾過
量を計測した。また、濾過後の試験液(濾液)の清浄度
を評価するため、濾液を孔径0.05μmのニュークリ
ポアメンブレンで濾過し、一定時間ごとの濾過量を計測
した。 (8)フィルタの濾過寿命の試験結果を図1に示し、濾
過後の試験液(濾液)の清浄度を図2に示す。図1に示
すように、フィルタの濾過寿命は積層型フィルタエレメ
ントDが最も優れた結果を生じた。また、図2に示すよ
うに、濾過後の試験液(濾液)の清浄度も、積層型フィ
ルタエレメントDが、PTFE濾過層のみからなる積層
型フィルタエレメントAに比べて、優れた結果を生じ
た。
BEST MODE FOR CARRYING OUT THE INVENTION In order to test the filtration life of a multilayer filter element of the present invention and the cleanliness of a fluid to be filtered after filtration, the multilayer filter elements A, B, C, and D having the following configurations are described. , E were prepared and tested by the following test methods using the test solutions shown below. (1) The laminated filter element A was composed of only a PTFE filtration layer, and this PTFE filtration layer was constituted by laminating three PTFE filtration membranes. Upstream PT
The pore size of the FE filtration membrane is 0.1 μm,
The pore diameter of the E filtration membrane was 0.05 μm, and the pore diameter of the intermediate PTFE filtration membrane was 0.1 μm. (2) The laminated filter element B was composed of only a polyethylene filtration layer, and this polyethylene filtration layer was constituted by laminating three polyethylene filtration membranes. The pore diameter of the most upstream polyethylene filtration membrane is 0.45 μm, and the pore diameter of the most downstream polyethylene filtration membrane is 0.15 μm.
m and the pore size of the intermediate polyethylene filtration membrane is 0.45μ.
m. (3) The multilayer filter element C is a pair of PTFE
A PTFE filtration layer constituted by laminating filtration membranes and a polyethylene filtration layer constituted by a single polyethylene filtration membrane were laminated. Of the pair of PTFE filtration membranes constituting the PTFE filtration layer, the upstream PT
The pore size of the FE filtration membrane is 0.45 μm,
The pore size of the E filtration membrane was 0.1 μm. Then, the pore size of the polyethylene filtration membrane constituting the polyethylene filtration layer is set to 0.
The thickness was 45 μm. The multilayer filter element C is made of PT
The FE filtration layer was arranged on the upstream side and the polyethylene filtration layer was arranged on the downstream side, and subjected to the test described above. (4) The multilayer filter element D is a pair of PTFE
A PTFE filtration layer constituted by laminating filtration membranes and a polyethylene filtration layer constituted by a single polyethylene filtration membrane were laminated. Of the pair of PTFE filtration membranes constituting the PTFE filtration layer, the upstream PT
The pore size of the FE filtration membrane was set to 5.0 μm, and the downstream PTFE was used.
The pore size of the filtration membrane was 0.1 μm. And the pore size of the polyethylene filtration membrane constituting the polyethylene filtration layer is 0.4
The thickness was 5 μm. The multilayer filter element D is made of PTF
The E filtration layer was disposed on the upstream side and the polyethylene filtration layer was disposed on the downstream side, and subjected to the above-mentioned test. (5) The multilayer filter element E is a pair of PTFE
A PTFE filtration layer constituted by laminating filtration membranes and a polyethylene filtration layer constituted by a single polyethylene filtration membrane were laminated. Of the pair of PTFE filtration membranes constituting the PTFE filtration layer, the upstream PT
The pore size of the FE filtration membrane is 10.0 μm,
The pore size of the E filtration membrane was 0.1 μm. Then, the pore size of the polyethylene filtration membrane constituting the polyethylene filtration layer is set to 0.
The thickness was 45 μm. The multilayer filter element E is made of PT
The FE filtration layer was arranged on the upstream side and the polyethylene filtration layer was arranged on the downstream side, and subjected to the test described above. (6) The test liquid, which is the fluid to be filtered, is prepared by dissolving a phenol resin in a thinner and having a viscosity of about 15 mPa · s (15 cP)
Was used. (7) In order to evaluate the filter life,
The test solution was filtered through a disc having a diameter of mm, and the amount of filtration was measured at regular intervals. Further, in order to evaluate the cleanliness of the test solution (filtrate) after filtration, the filtrate was filtered with a Nuclepore membrane having a pore size of 0.05 μm, and the amount of filtration was measured at regular intervals. (8) The test results of the filter life are shown in FIG. 1, and the cleanliness of the test liquid (filtrate) after filtration is shown in FIG. As shown in FIG. 1, the filter life of the multilayer filter element D was the most excellent for the filter life. In addition, as shown in FIG. 2, the cleanliness of the test liquid (filtrate) after the filtration was superior to that of the multilayer filter element A in which the multilayer filter element D had only the PTFE filtration layer. .

【0021】図3及び図4は、本発明の積層型フィルタ
エレメントをプリーツ11の形態に成形した場合の実施
例を示す。積層型フィルタエレメントを有する濾材10
は、図4に示すように、ポリオレフィン濾過層12と上
流側支持層/排水層13と下流側支持層/排水層14とP
TFE濾過層15とを重ね合わせ、密着させた状態で、
プリーツ11の形態に成形されている。この濾材10
は、図3に示すように、合成樹脂材料からなるコア20
の周囲に全体として環状に配置され、その周囲をケージ
30によって形状保持され、更に、濾材10の上下端部
にエンドキャップが熱融着等で接合されている。図3で
は、下部エンドキャップ40のみが図示され、上部エン
ドキャップは省略されている。また、上流側支持層/排
水層13と下流側支持層/排水層14は、ポリオレフィ
ン濾過層12とPTFE濾過層15とを支持して流路を
確保し、これによって、隣接する濾過膜同士が密着して
濾過流体が流れなくなるのを防止する。なお、濾過層
は、複数の又は単一の濾過媒体(濾過膜又は濾過層)に
よって構成されるが、図面では、濾過層として示してあ
る。
FIGS. 3 and 4 show an embodiment in which the multilayer filter element of the present invention is formed in the form of pleats 11. Filter medium 10 having laminated filter element
As shown in FIG. 4, the polyolefin filtration layer 12, the upstream support layer / drain layer 13, the downstream support layer / drain layer 14,
With the TFE filtration layer 15 superimposed and in close contact,
It is formed in the form of pleats 11. This filter medium 10
Is a core 20 made of a synthetic resin material, as shown in FIG.
Are arranged in a ring shape as a whole, the periphery thereof is held in shape by a cage 30, and an end cap is joined to the upper and lower ends of the filter medium 10 by heat fusion or the like. In FIG. 3, only the lower end cap 40 is shown, and the upper end cap is omitted. The upstream support layer / drainage layer 13 and the downstream support layer / drainage layer 14 support the polyolefin filtration layer 12 and the PTFE filtration layer 15 to secure a flow path, whereby adjacent filtration membranes are separated from each other. It prevents the filtration fluid from flowing due to close contact. In addition, although a filtration layer is comprised by several or single filtration media (filtration membrane or filtration layer), it is shown as a filtration layer in drawing.

【0022】[0022]

【発明の効果】濾過口径の異なるPTFE濾過膜を多層
化することにより、除粒子効率が向上し、濾過寿命を延
長させることができる。
According to the present invention, by forming the PTFE filtration membranes having different filtration apertures into multiple layers, the particle removal efficiency can be improved and the filtration life can be extended.

【0023】固形成分の濾過に優れた性能を有するPT
FE濾過膜と、ゲル状成分の濾過に優れたポリオレフィ
ン濾過膜を複合化して積層型フィルタエレメントを構成
することにより、フォトレジスト等の固形状成分と固形
状成分除去用最下流側濾過膜の孔径よりも概ね小さい径
のゲル状成分とが混在する濾過分野の濾過効果に優れた
フィルタを提供することができる。
PT having excellent performance in filtering solid components
Combining an FE filtration membrane and a polyolefin filtration membrane that excels in filtering gel-like components to form a laminated filter element, the solid component such as photoresist and the pore size of the most downstream filtration membrane for removing the solid components It is possible to provide a filter excellent in filtration effect in the field of filtration in which a gel component having a diameter smaller than that of the mixture is present.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 積層型フィルタエレメントA乃至Eの濾過寿
命の試験結果を表す図である。
FIG. 1 is a diagram showing test results of filtration life of laminated filter elements A to E.

【図2】 積層型フィルタエレメントA及びDの濾過液
の清浄度の試験結果を表す図である。
FIG. 2 is a diagram showing test results of the cleanliness of filtrates of the multilayer filter elements A and D.

【図3】 本発明の積層型フィルタエレメントをプリー
ツ状に成形して構成したフィルタエレメントの一部切欠
き部分を含む斜視図である。
FIG. 3 is a perspective view including a partially cut-away portion of a filter element formed by forming a laminated filter element of the present invention into a pleated shape.

【図4】 図3に示したプリーツ状のフィルタエレメン
トの部分的な拡大分解図である。 A、B、C、D、E 積層型フィルタエレメント 10 濾材 11 プリーツ 12 ポリオレフィン濾過層 13 上流側支持層/排水層 14 下流側支持層/排水層 15 PTFE濾過層 20 コア 30 ケージ 40 下部エンドキャップ
FIG. 4 is a partially enlarged exploded view of the pleated filter element shown in FIG. 3; A, B, C, D, E Multilayer filter element 10 Filter medium 11 Pleat 12 Polyolefin filtration layer 13 Upstream support layer / drainage layer 14 Downstream support layer / drainage layer 15 PTFE filtration layer 20 Core 30 Cage 40 Lower end cap

───────────────────────────────────────────────────── フロントページの続き (72)発明者 坂本 厚志 茨城県稲敷郡阿見町大字香澄の里46 日本 ポール株式会社 筑波工場内 (72)発明者 都築 修一 茨城県稲敷郡阿見町大字香澄の里46 日本 ポール株式会社 応用研究所内 Fターム(参考) 4D006 GA07 HA74 MA03 MA06 MA22 MC22X MC23 MC30X NA34 NA40 PA01 PB13 PB20 PB70 PC01 4D019 AA03 BA13 BB08 BB10 BD01 BD02 CA02  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Atsushi Sakamoto 46, Kasumi-no-sato, Oji, Ami-cho, Ibaraki Japan Inside the Pall Corporation Tsukuba Plant (72) Inventor Shuichi Tsuzuki 46, Kasumi-no-sato 46, Ami-cho, Inashiki, Ibaraki Japan Pall Corporation Applied Research Laboratory F term (reference) 4D006 GA07 HA74 MA03 MA06 MA22 MC22X MC23 MC30X NA34 NA40 PA01 PB13 PB20 PB70 PC01 4D019 AA03 BA13 BB08 BB10 BD01 BD02 CA02

Claims (13)

【特許請求の範囲】[Claims] 【請求項1】 PTFE濾過層とポリオレフィン濾過層
を積層させて成る、積層型フィルタエレメントであっ
て、前記PTFE濾過層は複数のPTFE濾過膜を積層
することによって構成され、前記複数のPTFE濾過膜
のうち、少なくとも一対のPTFE濾過膜は、PTFE
濾過膜毎に異なる孔径を有することを特徴とする、積層
型フィルタエレメント。
1. A laminated filter element comprising a PTFE filtration layer and a polyolefin filtration layer laminated, wherein said PTFE filtration layer is constituted by laminating a plurality of PTFE filtration membranes, and said plurality of PTFE filtration membranes are provided. Among them, at least one pair of PTFE filtration membranes is made of PTFE
A laminated filter element having a different pore size for each filtration membrane.
【請求項2】 請求項1に記載の積層型フィルタエレメ
ントにおいて、前記PTFE濾過層を被濾過流体の流れ
に関して上流側に配置し、前記ポリオレフィン層を被濾
過流体の流れに関して下流側に配置し、前記少なくとも
一対のPTFE濾過膜のうち、孔径が大きい方の前記P
TFE濾過膜を前記上流側に配置し、孔径が小さい方の
前記PTFE濾過膜を前記下流側に配置し、前記PTF
E濾過層によって被濾過流体中の固体成分を分離し、前
記ポリオレフィン濾過層によって被濾過流体中のゲル状
成分を分離するように構成した、前記積層型フィルタエ
レメント。
2. The laminated filter element according to claim 1, wherein the PTFE filtration layer is disposed upstream with respect to the flow of the fluid to be filtered, and the polyolefin layer is disposed downstream with respect to the flow of the fluid to be filtered. Of the at least one pair of PTFE filtration membranes, the P
Disposing the TFE filtration membrane on the upstream side, and disposing the PTFE filtration membrane having a smaller pore diameter on the downstream side,
The laminated filter element, wherein a solid component in the fluid to be filtered is separated by the E filtration layer, and a gel component in the fluid to be filtered is separated by the polyolefin filtration layer.
【請求項3】 請求項2に記載の積層型フィルタエレメ
ントにおいて、前記ポリオレフィン濾過層の孔径が前記
PTFE濾過層の最下流側の濾過膜の孔径以上であるよ
うに構成してなる、前記積層型フィルタエレメント。
3. The multilayer filter element according to claim 2, wherein the pore size of the polyolefin filtration layer is greater than or equal to the pore size of the filtration membrane on the most downstream side of the PTFE filtration layer. Filter element.
【請求項4】 請求項1に記載の積層型フィルタエレメ
ントにおいて、前記ポリオレフィン濾過層を前記PTF
E濾過層の間に配置して、被濾過流体の流れに関して上
流側から下流側に向かって前記二つの濾過層の孔径が連
続的または段階的に小さくなるように構成してなる、前
記積層型フィルタエレメント。
4. The laminated filter element according to claim 1, wherein the polyolefin filtration layer is formed of the PTF.
The stacked type, which is disposed between the E filtration layers and configured such that the pore diameters of the two filtration layers decrease continuously or stepwise from upstream to downstream with respect to the flow of the fluid to be filtered. Filter element.
【請求項5】 請求項1乃至4のうちのいずれか一項に
記載の積層型フィルタエレメントにおいて、前記PTF
E濾過層を一対のPTFE濾過膜を積層することによっ
て構成し、前記ポリオレフィン濾過層を単一のポリオレ
フィン濾過膜によって構成して成る、前記積層型フィル
タエレメント。
5. The multilayer filter element according to claim 1, wherein the PTF comprises:
The laminated filter element, wherein the E filtration layer is configured by laminating a pair of PTFE filtration membranes, and the polyolefin filtration layer is configured by a single polyolefin filtration membrane.
【請求項6】 請求項3に記載の積層型フィルタエレメ
ントにおいて、前記一対のPTFE濾過膜のうち、前記
上流側のPTFE濾過膜の孔径は0.45から10μm
であり、前記下流側のPTFE濾過膜の孔径は0.05
から0.45μmであり、前記ポリオレフィン濾過膜の
孔径は0.1から1.0μmである、前記積層型フィル
タエレメント。
6. The multilayer filter element according to claim 3, wherein the upstream PTFE filtration membrane of the pair of PTFE filtration membranes has a pore size of 0.45 to 10 μm.
And the pore size of the PTFE filtration membrane on the downstream side is 0.05
And the pore size of the polyolefin filtration membrane is 0.1 to 1.0 μm.
【請求項7】 請求項1乃至6のうちのいずれか一項に
記載の積層型フィルタエレメントにおいて、前記PTF
E濾過層と前記ポリオレフィン濾過層は、互いに重ね合
わされた状態で、プリーツ状に湾曲形成され、更に、前
記積層型フィルタエレメントは、全体として筒状の形態
を有する、前記積層型フィルタエレメント。
7. The multilayer filter element according to claim 1, wherein the PTF comprises:
The multilayer filter element, wherein the E filtration layer and the polyolefin filtration layer are formed in a pleated shape while being overlapped with each other, and the multilayer filter element has a cylindrical shape as a whole.
【請求項8】 PTFE濾過膜を複数枚積層させてPT
FE濾過層を構成し、前記複数のPTFE濾過膜のう
ち、少なくとも一対のPTFE濾過膜は、PTFE濾過
膜毎に異なる孔径を有する、積層型フィルタエレメン
ト。
8. A method in which a plurality of PTFE filtration membranes are laminated to form a PT
A laminated filter element comprising a FE filtration layer, wherein at least a pair of PTFE filtration membranes among the plurality of PTFE filtration membranes have different pore sizes for each PTFE filtration membrane.
【請求項9】 請求項8に記載の積層型フィルタエレメ
ントにおいて、前記少なくとも一対のPTFE濾過膜の
うち、孔径が大きい方の前記PTFE濾過膜を被濾過流
体の流れに関して上流側に配置し、孔径が小さい方の前
記PTFE濾過膜を被濾過流体の流れに関して下流側に
配置して成る、前記積層型フィルタエレメント。
9. The multilayer filter element according to claim 8, wherein, among the at least one pair of PTFE filtration membranes, the PTFE filtration membrane having a larger pore diameter is arranged on the upstream side with respect to the flow of the fluid to be filtered. The laminated filter element, wherein the smaller PTFE filtration membrane is disposed downstream with respect to the flow of the fluid to be filtered.
【請求項10】 請求項8又は9に記載の積層型フィル
タエレメントにおいて、前記PTFE濾過層はプリーツ
状に湾曲形成され、更に、前記積層型フィルタエレメン
トは、全体として筒状の形態を有する、前記積層型フィ
ルタエレメント。
10. The multilayer filter element according to claim 8, wherein the PTFE filtration layer is formed in a pleated shape, and the multilayer filter element has a cylindrical shape as a whole. Stacked filter element.
【請求項11】 ポリオレフィン濾過膜を複数枚積層さ
せてポリオレフィン濾過層を構成し、前記複数のポリオ
レフィン濾過膜のうち、少なくとも一対のポリオレフィ
ン濾過膜は、ポリオレフィン濾過膜毎に異なる孔を有す
る、積層型フィルタエレメント。
11. A laminated type wherein a plurality of polyolefin filtration membranes are laminated to form a polyolefin filtration layer, and at least one pair of polyolefin filtration membranes among the plurality of polyolefin filtration membranes has different holes for each polyolefin filtration membrane. Filter element.
【請求項12】 請求項11に記載の積層型フィルタエ
レメントにおいて、前記少なくとも一対のポリオレフィ
ン濾過膜のうち、孔径が大きい方の前記ポリオレフィン
濾過膜を被濾過流体の流れに関して上流側に配置し、孔
径が小さい方の前記ポリオレフィン濾過膜を被濾過流体
の流れに関して下流側に配置して成る、前記積層型フィ
ルタエレメント。
12. The multilayer filter element according to claim 11, wherein, of the at least one pair of polyolefin filtration membranes, the polyolefin filtration membrane having a larger pore diameter is disposed upstream with respect to the flow of the fluid to be filtered. The multilayer filter element, wherein the polyolefin filtration membrane having a smaller size is disposed downstream with respect to the flow of the fluid to be filtered.
【請求項13】 請求項11又は12に記載の積層型フ
ィルタエレメントにおいて、前記ポリオレフィン濾過層
はプリーツ状に湾曲形成され、更に、前記積層型フィル
タエレメントは、全体として筒状の形態を有する、前記
積層型フィルタエレメント。
13. The multilayer filter element according to claim 11, wherein the polyolefin filtration layer is formed into a pleated curve, and the multilayer filter element has a cylindrical shape as a whole. Stacked filter element.
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