JPH0628176Y2 - Support structure of porous thin film - Google Patents
Support structure of porous thin filmInfo
- Publication number
- JPH0628176Y2 JPH0628176Y2 JP1988025978U JP2597888U JPH0628176Y2 JP H0628176 Y2 JPH0628176 Y2 JP H0628176Y2 JP 1988025978 U JP1988025978 U JP 1988025978U JP 2597888 U JP2597888 U JP 2597888U JP H0628176 Y2 JPH0628176 Y2 JP H0628176Y2
- Authority
- JP
- Japan
- Prior art keywords
- thin film
- porous thin
- protrusion
- support structure
- support
- 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.)
- Expired - Lifetime
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- Separation Using Semi-Permeable Membranes (AREA)
Description
【考案の詳細な説明】 考案の目的 (産業上の利用分野) 本考案は、平板状多孔性薄膜を濾材として用いたフィル
タエレメントにおいて、フィルタ機能を発揮させる有効
膜面積を最大限に利用する構造によって薄膜を支持し、
かつ濾過された清浄流体の流路を有効に確保するように
した多孔性薄膜の支持体構造に関するものである。[Detailed Description of the Invention] Purpose of the Invention (Industrial Application Field) The present invention is a filter element using a flat plate-like porous thin film as a filter medium, and a structure for maximally utilizing an effective membrane area for exerting a filter function. Support the thin film by
The present invention also relates to a support structure of a porous thin film that effectively secures a flow path of a filtered clean fluid.
(従来の技術) 一般に、平板状多孔性薄膜を濾材として用いる単層及び
二層以上の積層タイプに使用されている膜支持体の構造
は、膜を支持する凸状の突出部が連続したリブ(例え
ば、同芯円状のリブ)を有したものと、単に支持板に多
数の流出口を有したものとがある。(Prior Art) In general, the structure of a membrane support used in a single layer or a laminated type of two or more layers using a flat plate-like porous thin film as a filter medium is a rib in which convex protrusions for supporting the membrane are continuous. There are those having (for example, concentric circular ribs) and those having only a large number of outflow ports on the support plate.
上記したリブ形状を有する前者の支持板は、凸部が一定
巾を持ち、かつ連続しており、これが一定間隔に濾材全
域を支持するごとく配置され、その連続したリブの一部
に濾過された清浄流体がフィルタ流出口に連通するスリ
ットが設けられている。また、後者のものは、リブの代
わりにフィルタ流出口に連通する多数の細孔が設けられ
たフィルム状のものや、多孔体、メッシュ等のものが存
在している。In the former support plate having the rib shape described above, the convex portions have a constant width and are continuous, and they are arranged so as to support the entire area of the filter medium at regular intervals, and the ribs are partially filtered. A slit is provided in which the clean fluid communicates with the filter outlet. Further, as the latter, there are a film-like one having a large number of pores communicating with the filter outlet instead of the rib, a porous body, a mesh and the like.
上記のような支持体を使用して、平板状多孔性薄膜1層
をその外周縁上をOリング、平パッキン等のゴム弾性体
で封止して使用する手法が実験室でよく使用されてい
る。更に、この薄膜を支持板の片面又は両面の周縁にお
いて、熱、有機溶剤等で接着封止してこれをユニットと
し、このユニットを何等かの手段で連続、積層したエレ
メントを組み込んだフィルタが工業レベルで使用されて
いる。A method in which one layer of the flat plate-like porous thin film is sealed on the outer peripheral edge thereof with a rubber elastic body such as an O-ring or a flat packing using the support as described above is often used in a laboratory. There is. Further, the thin film is bonded and sealed on one or both sides of the support plate with heat, an organic solvent or the like to form a unit, and a filter incorporating an element in which the unit is continuous or laminated by some means is industrial. Used in the level.
(考案が解決しようとする課題) 上記した従来例による連続したリブ状突起を形成した支
持板においては、次のような矛盾点を有するため、上記
課題を解決した開発が求められている現状にある。(Problems to be Solved by the Invention) The above-mentioned conventional support plate having rib-shaped projections has the following contradictions. is there.
即ち、第6図A、Bに示すように、従来の連続したリブ
状突起22aを形成した支持板22においては、 薄膜21の実効膜面積を増大させ流量を多く採るため
には、リブ状突起22aの幅を極力狭く、かつ、リブ状
突起22a相互の間隔を極力広く設計する必要がある
が、反面濾過圧力によって薄膜21が破損又はたわみ、
支持板22の底部に密着し、逆に流量が低下するといっ
た問題が発生するおそれがある(第6図A参照)。That is, as shown in FIGS. 6A and 6B, in the conventional support plate 22 in which the continuous rib-shaped projections 22a are formed, in order to increase the effective film area of the thin film 21 and increase the flow rate, the rib-shaped projections are required. It is necessary to design the width of the ribs 22a as narrow as possible and the distance between the rib-shaped projections 22a as wide as possible, but on the other hand, the thin film 21 is damaged or bent by the filtration pressure.
There is a possibility that problems may occur such that the support plate 22 comes into close contact with the bottom portion thereof and the flow rate decreases on the contrary (see FIG. 6A).
薄膜21が濾過圧力に十分に抗し、破損又はたわみに
よって支持板22の底部密着による流量低下の危険性を
回避するためには、リブ状突起22aの幅を極力広く、
かつ、リブ状突起22aの間隔を狭く設計する必要があ
るが、反面薄膜21と突起22aとの密着による薄膜2
1の実効膜面積が減少するといった問題が発生する(第
6図B参照)。In order for the thin film 21 to sufficiently withstand the filtration pressure and to avoid the risk of a decrease in the flow rate due to the bottom contact of the support plate 22 due to breakage or bending, the width of the rib-shaped projection 22a should be as wide as possible.
In addition, it is necessary to design the interval between the rib-shaped projections 22a to be narrow, but on the other hand, the thin film 2 due to the close contact between the thin film 21 and the projections 22a.
The problem that the effective film area of No. 1 is reduced occurs (see FIG. 6B).
以上の説明から明らかなように、薄膜21と支持板22
のリブ状突起22aは、薄膜21の強度によって一義的
に決定されるものであり、膜と支持板上のリブの密着に
よる膜面積の損失はある程度止むをえないものとされて
いた。As is clear from the above description, the thin film 21 and the support plate 22
The rib-shaped projections 22a are uniquely determined by the strength of the thin film 21, and the loss of the film area due to the close contact between the film and the ribs on the support plate is unavoidable to some extent.
また、実質膜面積が大きくなり、コンパクト化できな
い等が挙げられる。更に、薄膜で濾過された清浄流体の
流路を確保する空間層の高さが一定であることは、圧力
損失が大きくなればなるほど、空間領域の減少を来た
し、流路抵抗の増大から流路閉塞までに至ることもあ
る等の種々の問題点がある。In addition, the substantial membrane area becomes large and it cannot be made compact. Furthermore, the fact that the height of the space layer that secures the passage of the clean fluid filtered by the thin film is constant means that the larger the pressure loss is, the smaller the space area is, and the passage resistance is increased. There are various problems such that it may lead to blockage.
本考案は、上記の技術的課題を解決するために開発した
ものであり、その目的とするところは、支持体と膜との
接触面積を最少に抑え、もって、膜支持と流路の有効な
確保を図り、しかも、高流量化やコンパクト化を可能と
した平板状多孔性薄膜の支持体構造を提供することにあ
る。The present invention was developed in order to solve the above technical problems, and its purpose is to minimize the contact area between the support and the membrane, and thus to provide an effective membrane support and flow channel. Another object of the present invention is to provide a support structure for a flat plate-like porous thin film, which can be secured, and can achieve a high flow rate and a compact size.
考案の構成 (課題を解決するための手段) 上記の目的を達成するため、本考案は、平板状多孔性薄
膜を支持板の片面又は両面の周縁を封止してユニット部
材を形成し、このユニット部材の1又は2以上で構成さ
れるフィルタエレメントの支持体構造において、上記し
た支持板の多孔性薄膜接触面に突部を多数形成すると共
に、この多孔性薄膜接触面には、フィルタエレメントの
出口流路と連通する集束口を形成し、この集束口の近傍
位置に形成した突出部は、上記した突部より大きく形成
する構成を採用した。また、この支持板に形成した突部
及び突出部は、正三角形配置で、かつ不連続に配設した
り、また、突出部の形状は、半球または円弧状に形成す
るようにする。Configuration of the Invention (Means for Solving the Problems) In order to achieve the above-mentioned object, the present invention forms a unit member by sealing a flat porous thin film on one or both peripheral edges of a support plate. In a filter element support structure composed of one or more unit members, a large number of protrusions are formed on the porous thin film contact surface of the above-mentioned support plate, and the porous thin film contact surface has a filter element A converging port communicating with the outlet channel is formed, and the projecting portion formed in the vicinity of this converging port is formed to be larger than the projecting portion described above. The protrusions and protrusions formed on the support plate are arranged in an equilateral triangle and discontinuously, and the shape of the protrusions is formed in a hemisphere or arc shape.
(作用) 支持体の膜接触面に形成した半球状或は円弧状の凸状リ
ブである突部と突出部により保持された平板状多孔性薄
膜を通過した清浄流体は、突部と突出部で形成された薄
膜との空間層である流路を経て、フィルタ出口流路に連
通する集束口へと流れ、フィルタ出口流路から清浄流体
が流出する。(Function) The clean fluid which has passed through the flat porous thin film held by the projection and the projection, which are hemispherical or arc-shaped convex ribs formed on the membrane contact surface of the support, has the projection and the projection. After passing through the flow path which is a space layer with the thin film formed in step (4), the clean fluid flows to the converging port communicating with the filter outlet flow path, and the clean fluid flows out from the filter outlet flow path.
この状態において、平板状多孔性薄膜は、流入圧力の増
大に対し、集束口の近傍位置に形成した突出部をその他
の突部より大きく形成したから、薄膜のたわみを抑え、
安定した流量特性を確保することができる。In this state, the flat plate-shaped porous thin film has a protrusion formed in the vicinity of the focusing port formed larger than the other protrusions with respect to an increase in inflow pressure, so that the deflection of the thin film is suppressed,
It is possible to secure stable flow characteristics.
(実施例) 第1図は本考案における平板状多孔性薄膜の支持体で構
成したフィルタエレメントをハウジングに収納したフィ
ルタの縦断面図、第2図Aはエレメントの分離斜視図、
第2図Bは支持体の低面図、第3図はエレメントの部分
断面図、第4図は支持体の一例を示した部分平面図、第
5図は支持体の他例を示した部分平面図である。(Embodiment) FIG. 1 is a longitudinal sectional view of a filter in which a filter element constituted by a support of a flat plate-like porous thin film according to the present invention is housed in a housing, and FIG. 2A is a separated perspective view of the element.
2B is a bottom view of the support, FIG. 3 is a partial cross-sectional view of the element, FIG. 4 is a partial plan view showing an example of the support, and FIG. 5 is a part showing another example of the support. It is a top view.
平板状多孔性薄膜1を支持板2の両面の周縁を封止して
ユニット部材3を形成し、このユニット部材3を突起部
4aを有するスペーサ4を介して積層し、フィルタエレ
メント5を構成する。上記した支持板2の多孔性薄膜接
触面2aに突部6を多数形成するとともに、この多孔性
薄膜接触面2aには、フィルタエレメント5の出口流路
7と連通する集束口8a、8bを形成する。集束口8a
は、支持板2の両面に連通する孔で、放射状に複数個形
成し、集束口8bは、フィルタ出口流路7の円周に配置
し、フィルタ出口流路7に直結する孔である。この集束
口8a、8bの近傍位置に形成した突出部9は、上記し
た突部6より大きく形成する。また、集束口8a、8b
の全体の開口面積は、1個のユニット部材3のフィルタ
出口流路7の面積と同等以上でなければならない。集束
口8a、8bを円弧状とした場合、その大きさは、射出
成形上、φ0、8mm以上が必要である。ここで、突部6
を円弧状にした場合の例について説明する。φ0、7m
m、高さ0、3mmの突部6をピッチ1、4mmで正三角形
に配置したとき、集束口8aは突部6間に設置困難であ
る。このため、突部6間に集束口8aを設けると、集束
口8a周辺の突部6間は、対角距離が2、8mmとなる。
この場合、薄膜は、流入圧力の増大にともない、延伸
さ、流路域の空間層を減少させ、流路閉塞に至ってしま
う。この現象は、薄膜のこしが弱い程、顕著であり、一
定の流入圧力時においても、時間の経過と共に、流量が
減少していき、最終的にはある一定量の流量値に到達す
る。そこで、集束口8a周辺の突起部9をφ1、0mm、
高さ0、4mmに大きくした。これによって、薄膜による
延伸による流路閉塞が防止ができ、流入圧力増大によっ
ても、安定した流量特性が確保できた。また、集束口8
aの中央部に縦リブ8cを設けることにより、更に安定
した流量特定が確保できる。このように支持板2に形成
した突部6及び突出部9は、正三角形配置で、かつ不連
続に配設し、突部6及び突出部9の形状は、半球または
円弧状に形成する。突出部9の大きさは、集束口開口面
積の0、5〜10倍になる直径を有し、高さが0、2〜
2mmが好ましいことが確認できた。更に、平板状多孔性
薄膜1は、孔径0、01〜5μm、開孔率20%以上、
厚み50〜200μmの高分子フィルムであり、材質とし
て、テトラフルオロエチレン、酢酸セルロース、硝酸セ
ルロース、ポリプロピレン、ポリビニルアルコール、ポ
リアミド、ポリメチルメタクリレート、ポリサルフォ
ン、ポリエーテルサルフォン、ポリ塩化ビニル等の高分
子を実施に応じて任意に選択するものとする。The flat porous thin film 1 is sealed on both sides of the support plate 2 to form the unit member 3, and the unit member 3 is laminated via the spacer 4 having the protrusion 4a to form the filter element 5. . A large number of protrusions 6 are formed on the porous thin film contact surface 2a of the support plate 2 described above, and focusing holes 8a, 8b communicating with the outlet flow path 7 of the filter element 5 are formed on the porous thin film contact surface 2a. To do. Focusing port 8a
Is a hole communicating with both surfaces of the support plate 2, and a plurality of holes are formed in a radial pattern, and the converging ports 8b are holes arranged in the circumference of the filter outlet channel 7 and directly connected to the filter outlet channel 7. The protrusion 9 formed in the vicinity of the focusing ports 8a and 8b is formed larger than the protrusion 6. Also, the focusing ports 8a and 8b
The total opening area of the above must be equal to or larger than the area of the filter outlet channel 7 of one unit member 3. When the converging ports 8a and 8b are formed in an arc shape, the size thereof needs to be φ0, 8 mm or more in view of injection molding. Here, the protrusion 6
An example of the case of arc shape will be described. φ0, 7m
When the protrusions 6 having m, height 0, and 3 mm are arranged in an equilateral triangle with a pitch of 1 and 4 mm, it is difficult to install the focusing port 8 a between the protrusions 6. Therefore, when the focusing port 8a is provided between the protrusions 6, the diagonal distance between the protrusions 6 around the focusing port 8a is 2.8 mm.
In this case, as the inflow pressure increases, the thin film is stretched, and the space layer in the flow channel region is reduced, resulting in the blockage of the flow channel. This phenomenon becomes more remarkable as the thinness of the thin film is weaker, and the flow rate decreases with time even at a constant inflow pressure, and finally reaches a certain flow rate value. Therefore, the protrusion 9 around the focusing port 8a is φ1, 0 mm,
The height was increased to 0, 4 mm. As a result, it was possible to prevent the flow path from being blocked due to the thin film stretching, and it was possible to secure stable flow characteristics even when the inflow pressure increased. Also, the focusing port 8
By providing the vertical rib 8c in the central portion of "a", more stable flow rate identification can be secured. The protrusions 6 and the protrusions 9 thus formed on the support plate 2 are arranged in an equilateral triangle and discontinuously, and the protrusions 6 and the protrusions 9 are formed in a hemispherical shape or an arc shape. The size of the projecting portion 9 has a diameter that is 0, 5 to 10 times the area of the opening of the focusing port, and the height is 0, 2 to 2.
It was confirmed that 2 mm is preferable. Furthermore, the flat plate-shaped porous thin film 1 has a pore size of 0, 01 to 5 μm, an opening ratio of 20% or more,
It is a polymer film with a thickness of 50 to 200 μm, and the material is polymer such as tetrafluoroethylene, cellulose acetate, cellulose nitrate, polypropylene, polyvinyl alcohol, polyamide, polymethylmethacrylate, polysulfone, polyethersulfone, polyvinyl chloride, etc. It should be arbitrarily selected according to the implementation.
なお、図中10はフィルタエレメント5を収納するため
のハウジング、11はOリング、12は原液流入口、1
3はハウジング10の清浄流体流出口である。In the figure, 10 is a housing for housing the filter element 5, 11 is an O-ring, 12 is a stock solution inlet,
Reference numeral 3 is a clean fluid outlet of the housing 10.
次に上記実施例の作用を説明する。Next, the operation of the above embodiment will be described.
支持板2の膜接触面2aに形成した半球状或は円弧状の
凸状リブである突部6と突出部9により保持された平板
状多孔性薄膜1を通過した清浄流体は、突部6と突出部
9で形成された薄膜1との空間層である流路1aを経
て、フィルタ出口流路7に連通する集束口8bへと流
れ、フィルタ出口流路7から清浄流体が流出することに
なる。The clean fluid passing through the flat plate-shaped porous thin film 1 held by the projections 6 and the projections 9 which are hemispherical or arcuate convex ribs formed on the membrane contact surface 2a of the support plate 2 is projected. Through the flow path 1a, which is a space layer between the thin film 1 formed by the protrusions 9 and the protrusions 9, to the focusing port 8b communicating with the filter outlet flow path 7, and the clean fluid flows out from the filter outlet flow path 7. Become.
この状態において、平板状多孔性薄膜1は、流入圧力の
増大に対し、集束口8a、8bの近傍位置に形成した突
出部9をその他の突部6より大きく形成したから、薄膜
1のたわみを抑え、安定した流量特性を確保することが
できる。In this state, in the flat plate-shaped porous thin film 1, the protrusions 9 formed near the focusing ports 8a and 8b are formed larger than the other protrusions 6 with respect to the increase of the inflow pressure. It is possible to suppress and secure stable flow characteristics.
ここで、従来品と本考案における実施例品との流量特性
を下表に示す。Here, the flow rate characteristics of the conventional product and the product of the present invention are shown in the table below.
考案の効果 以上のことから明らかなように、本考案によると、流入
圧力の増大に対し、集束口の近傍位置に形成した突出部
をその他の突部より大きく形成したから、支持体と膜と
の接触面積を最少にし、かつ薄膜のたわみを抑えて安定
した流量特性を確保することができ、しかも、フィルタ
の高流量化やコンパクト化をも可能とし、フィルタエレ
メントとして極めて使用価値の高いものを提供すること
ができる。 As is apparent from the above, according to the present invention, the protrusion formed near the focusing port is formed larger than the other protrusions with respect to the increase of the inflow pressure. The contact area of the filter can be minimized, and the deflection of the thin film can be suppressed to ensure stable flow characteristics. In addition, the filter can be made to have a high flow rate and be compact, and it is extremely useful as a filter element. Can be provided.
殊に、半導体分野における担体ガス、エッチング用ガ
ス、パージガス等は、近年の半導体の高密度化、高集積
化に伴い、高い清浄性と、可能な限り低圧損のフィルタ
が望まれているが、本考案は、その条件をも確実に満足
するフィルタを提供することができる。In particular, carrier gas, etching gas, purge gas, etc. in the field of semiconductors are required to have filters with high cleanliness and low pressure loss as much as possible due to the recent high density and high integration of semiconductors. The present invention can provide a filter that surely satisfies that condition.
第1図乃至第5図は本考案の実施例を示したもので、第
1図は、本考案における平板状多孔性薄膜の支持体で構
成したエレメントをハウジングに収納したフィルタの縦
断面図、第2図Aは、第1図のエレメントの分離斜視
図、第2図Bは、第2図Aにおける支持体の低面図、第
3図は、エレメントの部分断面図、第4図は、支持体の
一例を示した部分平面図、第5図は支持体の他例を示し
た部分平面図であり、第6図A、Bは従来例を示したフ
ィルタエレメントの部分拡大断面説明図である。 1……平板状多孔性薄膜 2……支持板 2a……多孔性薄膜接触面 3……ユニット部材 5……フィルタエレメント 6……突部 7……フィルタ出口流路 8a、8b……集束口 9……突出部1 to 5 show an embodiment of the present invention, and FIG. 1 is a vertical cross-sectional view of a filter in which an element constituted by a support of a plate-like porous thin film in the present invention is housed in a housing, 2A is an isolated perspective view of the element of FIG. 1, FIG. 2B is a bottom view of the support in FIG. 2A, FIG. 3 is a partial sectional view of the element, and FIG. FIG. 5 is a partial plan view showing an example of a support, FIG. 5 is a partial plan view showing another example of the support, and FIGS. 6A and 6B are partially enlarged sectional explanatory views of a filter element showing a conventional example. is there. 1 ... Flat porous thin film 2 ... Supporting plate 2a ... Porous thin film contact surface 3 ... Unit member 5 ... Filter element 6 ... Projection 7 ... Filter outlet flow path 8a, 8b ... Convergence port 9 ... Projection
Claims (4)
周縁で封止してユニット部材を形成し、この支持板の両
面の多孔性薄膜接触面に多数の突部を形成すると共に、
この多孔性薄膜接触面には、支持体の中央部に設けた出
口流路と連通する集束口を形成し、上記した突部のう
ち、集束口の近傍位置に配設した突部を突出部とし、こ
の突出部は他の突部より大きく形成され、この突部及び
突出部は、正三角形配置で配設され、更に、突部及び突
出部の断面形状を、半球又は円弧状に形成したことを特
徴とする多孔性薄膜の支持体構造。1. A flat porous thin film is sealed on both sides of a single support plate to form a unit member, and a large number of protrusions are formed on the porous thin film contact surfaces on both sides of this support plate. With
On this porous thin film contact surface, a converging port communicating with the outlet channel provided in the central part of the support is formed, and among the above-mentioned projecting parts, the projecting part disposed in the vicinity of the converging port is the projecting part. The protrusion is formed to be larger than the other protrusions, the protrusion and the protrusion are arranged in an equilateral triangle arrangement, and the protrusion and the protrusion are formed to have a hemispherical or arcuate cross-sectional shape. A support structure of a porous thin film, characterized in that
5〜10倍になる直径を有し、高さが、0、2〜2mmで
ある請求項1記載の支持体構造。2. The size of the projecting portion is 0, which is the area of the aperture of the focusing port,
2. The support structure according to claim 1, having a diameter of 5 to 10 times and a height of 0,2 to 2 mm.
m、開孔率20%以上、厚み50〜200μmの高分子フィ
ルムである請求項1又は2記載の支持体構造。3. The plate-like porous thin film has a pore size of 0, 01 to 5 μm.
The support structure according to claim 1 or 2, which is a polymer film having m, a porosity of 20% or more, and a thickness of 50 to 200 µm.
レン、酢酸セルロース、硝酸セルロース、ポリプロピレ
ン、ポリビニルアルコール、ポリアミド、ポリメチルメ
タクリレート、ポリサルフォン、ポリエーテルサルフォ
ン、ポリ塩化ビニル等の高分子である請求項3記載の支
持体構造。4. The flat plate-like porous thin film is a polymer such as tetrafluoroethylene, cellulose acetate, cellulose nitrate, polypropylene, polyvinyl alcohol, polyamide, polymethylmethacrylate, polysulfone, polyethersulfone, polyvinyl chloride and the like. Item 3. The support structure according to item 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1988025978U JPH0628176Y2 (en) | 1988-03-01 | 1988-03-01 | Support structure of porous thin film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1988025978U JPH0628176Y2 (en) | 1988-03-01 | 1988-03-01 | Support structure of porous thin film |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01132201U JPH01132201U (en) | 1989-09-07 |
JPH0628176Y2 true JPH0628176Y2 (en) | 1994-08-03 |
Family
ID=31247182
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1988025978U Expired - Lifetime JPH0628176Y2 (en) | 1988-03-01 | 1988-03-01 | Support structure of porous thin film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0628176Y2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6078848B2 (en) * | 2012-11-20 | 2017-02-15 | 公益財団法人神奈川科学技術アカデミー | Method for forming lipid bilayer membrane and instrument therefor |
JP6084686B2 (en) * | 2013-04-26 | 2017-02-22 | 長瀬フィルター株式会社 | Filter retainer and filter using the same |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5962320A (en) * | 1982-09-30 | 1984-04-09 | Tsuchiya Mfg Co Ltd | Built-up filter unit made of plastic |
JPH0337701Y2 (en) * | 1985-10-31 | 1991-08-09 |
-
1988
- 1988-03-01 JP JP1988025978U patent/JPH0628176Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH01132201U (en) | 1989-09-07 |
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