JPH0532162Y2 - - Google Patents

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Publication number
JPH0532162Y2
JPH0532162Y2 JP1986138026U JP13802686U JPH0532162Y2 JP H0532162 Y2 JPH0532162 Y2 JP H0532162Y2 JP 1986138026 U JP1986138026 U JP 1986138026U JP 13802686 U JP13802686 U JP 13802686U JP H0532162 Y2 JPH0532162 Y2 JP H0532162Y2
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JP
Japan
Prior art keywords
tube
polytetrafluoroethylene
tubular body
tubes
porous
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
Application number
JP1986138026U
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Japanese (ja)
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JPS6343609U (en
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Priority to JP1986138026U priority Critical patent/JPH0532162Y2/ja
Publication of JPS6343609U publication Critical patent/JPS6343609U/ja
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Description

【考案の詳細な説明】 「考案の目的」 本考案は脱気用チユーブの考案に係り、各種液
体中に含有される気体分を除去するためのチユー
ブに関して通気量(脱気量)を高くし得ると共に
耐液圧性をも高く維持することができて効率的な
脱気をなすことのできる脱気用チユーブを提供し
ようとするものである。
[Detailed explanation of the invention] ``Purpose of the invention'' The present invention relates to the invention of a deaeration tube, which is designed to increase the amount of ventilation (deaeration amount) for the tube for removing gas contained in various liquids. It is an object of the present invention to provide a deaeration tube which can obtain a high temperature and maintain high liquid pressure resistance and perform efficient deaeration.

産業上の利用分野 LSI洗浄用超純水や水系溶媒樹脂フイルム原
料、液体クロマトグラフイ水系溶媒液などの脱気
機構。
Industrial applications Degassing mechanism for ultrapure water for LSI cleaning, aqueous solvent resin film raw materials, liquid chromatography aqueous solvent liquid, etc.

従来の技術 各種液体において空気その他の気体混入の好ま
しからざる場合に脱気することは従来から種々に
実施されている。即ち、例えばLSI洗浄用超純
水、水系溶媒樹脂フイルム原料あるいは液体クロ
マトグラフイ水系溶媒液などに関してそれぞれ脱
気装置が採用され、その含有気体を分離除去する
ことが行われており、斯うした目的で従来用いら
れているものとしてはポリテトラフルオロエチレ
ンの多孔質チユーブが一般的である。
BACKGROUND OF THE INVENTION Various methods have been used to deaerate liquids in cases where air or other gases are undesirably mixed in. That is, for example, deaerators are used for ultrapure water for LSI cleaning, aqueous solvent resin film raw materials, liquid chromatography aqueous solvent liquid, etc. to separate and remove the gases contained therein. Porous tubes of polytetrafluoroethylene are commonly used for this purpose.

考案が解決しようとする問題点 上記した従来のポリテトラフルオロエチレンに
よる多孔質チユーブは耐薬品性に優れ又好ましい
脱気作用をなすものであるが、通気量を高める
と、耐水圧性が低くなり、反対にこの耐水圧性を
高く維持しようとすると通気量の低いものとなら
ざるを得ない。即ちこれらの関係は第4図に示す
如くであつて、例えば通気量を5×10-2c.c./cm2
secから10×10-2c.c./cm2・secに高めると耐液圧
(水圧)性が約0.9Kg/cm2から0.3Kg/cm2に低下し、
このようなチユーブとして一般的に要求される
0.8Kg/cm2の耐圧性が得られず、液圧が高く、し
かも通気量の多い効率的な脱気処理をなし得ない
のが従来市販されているポリテトラフルオロエチ
レン多孔質チユーブである。
Problems to be solved by the invention The conventional porous tube made of polytetrafluoroethylene described above has excellent chemical resistance and has a favorable deaeration effect, but when the aeration rate is increased, the water pressure resistance becomes low. On the other hand, if this water pressure resistance is to be maintained at a high level, the amount of ventilation will inevitably be low. That is, these relationships are as shown in Fig. 4. For example, if the ventilation rate is 5 × 10 -2 cc/cm 2 .
When increasing from sec to 10×10 -2 cc/cm 2・sec, the liquid pressure (water pressure) resistance decreases from approximately 0.9Kg/cm 2 to 0.3Kg/cm 2 .
Generally required such as tube
Conventionally available polytetrafluoroethylene porous tubes do not have a pressure resistance of 0.8 Kg/cm 2 , have high liquid pressure, and cannot perform efficient deaeration treatment with a large amount of ventilation.

従つてこのような従来の脱気用チユーブで脱気
量を高めるにはチユーブを長くして表面積を増加
するか、チユーブの本数を多くする方法しかない
が、前者は管内抵抗を増加するから液圧を高くす
ることが必要であり、後者は設備の大型化を招
き、何れにしても不利な設備、操業とならざるを
得ない。即ち今日における各種工業の高精度化は
液中における気体の存在もゆるがせにできないよ
うになつており、前記LSI洗浄水中のガスはLSI
表面に付着して後加工の妨害となり、樹脂系原料
中のガスはフイルム成形時その他におけるピンホ
ール発生原因となるなどの事由から脱気をなるべ
くコンパクトな設備において効率的に実施するこ
とについては強い要請があるにも拘わらず、この
ような要請に対し適切に応じ得ない。
Therefore, the only way to increase the amount of deaeration with conventional deaeration tubes is to increase the surface area by making the tube longer, or to increase the number of tubes, but the former increases the internal resistance of the liquid. It is necessary to increase the pressure, and the latter leads to an increase in the size of the equipment, which inevitably results in disadvantageous equipment and operation. In other words, the high precision of various industries today has made it impossible to ignore the presence of gas in the liquid, and the gas in the LSI cleaning water is
Gases in resin raw materials can adhere to surfaces and interfere with post-processing, and gases in resin raw materials can cause pinholes during film molding and other processes, so it is strongly recommended that deaeration be carried out efficiently in as compact equipment as possible. Despite requests, we are unable to respond appropriately to such requests.

「考案の構成」 問題点を解決するための手段 柔軟性を有するポリテトラフルオロエチレンチ
ユーブによる内側チユーブと外側チユーブを有
し、これら内外側チユーブの間にポリテトラフル
オロエチレンによる平均孔径が0.2〜0.8μmで、前
記内外側チユーブの平均孔径より小さい孔径の平
面的延伸多孔質フイルムで形成された管状体を介
装したことを特徴とする脱気用チユーブ。
"Structure of the invention" Means for solving the problem It has an inner tube and an outer tube made of flexible polytetrafluoroethylene tube, and between these inner and outer tubes, an average pore diameter of 0.2 to 0.8 is made of polytetrafluoroethylene. A degassing tube characterized in that a tubular body formed of a planar stretched porous film having a pore diameter smaller than the average pore diameter of the inner and outer tubes in μm is inserted.

作 用 内外側チユーブの間にポリテトラフルオロエチ
レンによる平均孔径が0.2〜0.8μmで、前記内外側
チユーブの平均孔径より小さい平面的延伸多孔質
フイルムで形成された管状体を介装することによ
り該管状体が脱気作用の主体をなし、即ちその微
細孔組織と平面的延伸による薄層性は材質自体の
発水性と相俟つて通気性を適切に確保し、しかも
透水を有効に防止する。更にこのような平面的延
伸組織は好ましい強度性を有していて空孔率の高
い組織において耐水圧性の優れたものとなり効率
的な脱気を行わしめる。
Function By interposing between the inner and outer tubes a tubular body formed of a planar stretched porous film made of polytetrafluoroethylene and having an average pore diameter of 0.2 to 0.8 μm and smaller than the average pore diameter of the inner and outer tubes. The tubular body plays a main role in the degassing action, that is, its microporous structure and thin layer property due to planar stretching, together with the water repellency of the material itself, ensure appropriate air permeability and effectively prevent water permeation. Furthermore, such a planar stretched structure has preferable strength, and a structure with a high porosity has excellent water pressure resistance, allowing efficient degassing.

管状体の内外側に位置する内側チユーブと外側
チユーブとは該管状体を適切に薄層化することを
可能とし、前記のような効率的脱気性を確保す
る。
The inner and outer tubes located on the inner and outer sides of the tubular body allow the tubular body to be appropriately thinned and ensure efficient deaeration as described above.

各チユーブおよび管状体が共にポリテトラフル
オロエチレンであることにより各部材のなじみが
よく、又耐熱性や耐薬品性などの特性においても
優れ、しかも各チユーブにおける孔径が比較的大
であることおよび管状体の空孔率が比較的大であ
ることは脱気用チユーブ全体に柔軟性を維持せし
め任意に屈曲せしめた自在な脱気設備を設計させ
る。
Since each tube and the tubular body are both made of polytetrafluoroethylene, each member is compatible with each other, and has excellent properties such as heat resistance and chemical resistance. The relatively large porosity of the body allows the entire degassing tube to maintain flexibility and allow for the design of flexible degassing equipment that can be bent at will.

実施例 本考案によるものの具体的な実施態様を添附図
面に示すものについて説明すると、本考案におい
てもポリテトラフルオロエチレン多孔質チユーブ
を用いるが、第1図に示すようにこのポリテトラ
フルオロエチレン多孔質チユーブによるものを内
側チユーブ1と外側チユーブ3として用い、しか
もこれらチユーブ1,3の間に平面的延伸ポリテ
トラフルオロエチレン多孔質フイルム4による管
状体2を介装したものである。
EXAMPLE To explain a specific embodiment of the present invention as shown in the attached drawings, a polytetrafluoroethylene porous tube is also used in the present invention, and as shown in FIG. A tube is used as the inner tube 1 and the outer tube 3, and a tubular body 2 made of a planar stretched polytetrafluoroethylene porous film 4 is interposed between the tubes 1 and 3.

前記管状体2を得るためには第2図に示すよう
に所要の幅をもつた多孔質フイルム4の両側を融
着5などしてパイプ状となし、このものを内側チ
ユーブ1の外側に覆着し、更にその外側にチユー
ブ3を覆着することによつて簡易に製作し得る。
In order to obtain the tubular body 2, as shown in FIG. It can be easily manufactured by attaching the tube 3 to the outer surface of the tube 3 and then covering the outside thereof with the tube 3.

前記した多孔質フイルム4はポリテトラフルオ
ロエチレン膜材を平面的に圧延、延伸して多孔組
織となし、即ち多数の微小結節部間に無数の微細
繊維がくもの巣状に形成したものとして得られる
ことは公知の通りで、ポリテトラフルオロエチレ
ンは平面的延伸により材質的に精度の高い多孔質
化が得られることは一般的に知られている通りで
あつて、その微細な繊維構造と樹脂自体の有する
撥水性とが相俟つて通気は許容するものの液体
(特に水)を通過せしめず、従つて本考案にあつ
てはこのようなフイルム4による管状体2が脱気
作用の主体をなすものである。このためその多孔
組織における孔径が重要であり、即ちフイルムで
あるからその厚さも30〜100μmのようにチユーブ
の場合よりは少なくとも数分の1以下とされた薄
いものとすることが通気量を大とする上において
枢要であり、又このような厚さに延伸などで容易
に成形し得るが、斯うした条件下において前記の
ような微細繊維間に形成される孔径としては0.2
〜0.8μm程度とする。即ちこの孔径が0.8μmを超
えるものにおいては耐液圧性が充分に得られず、
例えば1.0Kg/cm2以上の水圧条件で水分が一部透
過し、有効な脱気作用を求め得ない。一方孔径が
0.2μm以下ともなると通気性が適切に得られない
こととなる傾向が認められる。
The porous film 4 described above is obtained by flatly rolling and stretching a polytetrafluoroethylene film material to form a porous structure, that is, a countless number of fine fibers are formed in a spider web shape between a large number of micro nodules. It is generally known that polytetrafluoroethylene can be made porous with high precision through planar stretching, and its fine fiber structure and resin itself Combined with its water repellency, it allows ventilation but does not allow liquid (particularly water) to pass through. Therefore, in the present invention, the tubular body 2 made of such a film 4 plays the main role in degassing. It is. For this reason, the pore size of the porous structure is important; in other words, since it is a film, its thickness should be at least a fraction of that of a tube, such as 30 to 100 μm, to increase the amount of ventilation. Although it is important to achieve this thickness and can be easily formed by stretching etc. under such conditions, the diameter of the pores formed between the above-mentioned fine fibers is 0.2.
It should be about 0.8 μm. In other words, if the pore size exceeds 0.8 μm, sufficient liquid pressure resistance cannot be obtained.
For example, under water pressure conditions of 1.0 Kg/cm 2 or more, some water will permeate, making it impossible to obtain an effective deaeration effect. On the other hand, the pore diameter
When the thickness is less than 0.2 μm, there is a tendency that proper air permeability cannot be obtained.

1例として平均孔径が0.2〜1μmで、膜厚が
65μmであり、空孔率85%のポリテトラフルオロ
エチレンフイルムの耐水圧値と通気量の関係は第
3図に示す如くであつて、耐水圧1.0Kg/cm2で通
気量10c.c./cm2・secを充分に確保し、耐水圧0.5
Kg/cm2では30c.c./cm2・secを充分に得しめること
ができる。
As an example, the average pore size is 0.2 to 1 μm and the film thickness is
The relationship between the water pressure resistance value and the air permeability of a polytetrafluoroethylene film with a diameter of 65 μm and a porosity of 85% is shown in Figure 3. When the water pressure resistance is 1.0 Kg/cm 2 , the air permeability is 10 c.c./cm 2 . Ensuring sufficient cm 2 sec, water pressure resistance 0.5
Kg/cm 2 can sufficiently obtain 30 c.c./cm 2 sec.

前記したように脱気機能の主体はポリテトラフ
ルオロエチレンの平面的延伸による多孔質フイル
ム4による管状体2であることから内側チユーブ
1および外側チユーブ3の作用は、それが成程材
質的には同じポリテトラフルオロエチレン多孔質
体であつてもその技術的性格を従来の脱気用チユ
ーブの場合と異にしたものとなり、前記管状体2
の支持体ないし保護体となる。従つてその孔径、
厚さなどはこのような意味において決定されるこ
ととなり、その孔径については平面的延伸多孔質
フイルム4の孔径より大きい(従つて平面的延伸
多孔質フイルムの孔径はこれらのチユーブ1,3
の孔径より小)ものとする。なお前記フイルム4
による管状体2の汚れ、疵を防止し、耐薬品性や
耐熱性などの要求される場合においても、このポ
リテトラフルオロエチレンによるチユーブ1,3
が適切であつて、特に液体クロマトグラフイ用の
脱気チユーブなどでは溶出を考慮することが必要
で前記のようなポリテトラフルオロエチレンによ
る多孔質チユーブがこの点においても有効であ
る。
As mentioned above, since the main body of the degassing function is the tubular body 2 made of the porous film 4 made of planar stretching of polytetrafluoroethylene, the functions of the inner tube 1 and the outer tube 3 are Even though the polytetrafluoroethylene porous body is the same, its technical characteristics are different from those of the conventional degassing tube, and the tubular body 2
serves as a support or protector for Therefore, the pore size,
The thickness etc. are determined in this sense, and the pore diameter is larger than the pore diameter of the planar stretched porous film 4 (therefore, the pore diameter of the planar stretched porous film is larger than that of the tubes 1 and 3).
(smaller than the pore diameter). Note that the film 4
The tubes 1 and 3 made of polytetrafluoroethylene can be used to prevent stains and scratches on the tubular body 2 due to
In particular, elution must be taken into account in degassing tubes for liquid chromatography, and porous tubes made of polytetrafluoroethylene as described above are effective in this respect as well.

本考案によるものの若干の製造例について説明
すると、以下の如くである。
Some manufacturing examples according to the present invention will be described below.

製造例 1 外径7.2mm、内径6.0mm、空孔率が50%で、孔径
が3.5μmのポリテトラフルオロエチレンによる内
側チユーブ1の外側に、厚さ50μm、空孔率85%、
孔径0.45μmの平面的延伸ポリテトラフルオロエ
チレンフイルムによる管状体2を被覆し、更にそ
の外側に外径10.0mm、内径8.0mmで空孔率、孔径
が前記内側チユーブ1と同じである外側チユーブ
3を覆着して本考案による製品を得た。
Manufacturing example 1 On the outside of the inner tube 1 made of polytetrafluoroethylene, which has an outer diameter of 7.2 mm, an inner diameter of 6.0 mm, a porosity of 50%, and a pore diameter of 3.5 μm, a thickness of 50 μm, a porosity of 85%,
A tubular body 2 made of a planar stretched polytetrafluoroethylene film with a pore diameter of 0.45 μm is coated, and an outer tube 3 having an outer diameter of 10.0 mm, an inner diameter of 8.0 mm, and the same porosity and pore diameter as the inner tube 1 is provided on the outside thereof. A product according to the present invention was obtained by covering the product.

斯うした本考案チユーブ内に25℃の水溶液を
1.5Kg/cm2の圧力で流入し、しかもチユーブの外
側を70cmHgの真空状として脱気処理したときに
管状体2を通過して外側に出る空気量は、8.0×
10-2c.c./cm2・secであり、内部の水はチユーブ1
を透過して管状体2に達するが、該管状体2から
滲み出ることなしに有効な脱気処理をなすことが
でき、設備のコンパクト化を図ることだできた。
An aqueous solution at 25℃ is placed inside the tube of this invention.
When the air flows in at a pressure of 1.5Kg/cm 2 and the outside of the tube is degassed with a vacuum of 70cmHg, the amount of air passing through the tubular body 2 and exiting outside is 8.0×
10 -2 cc/cm 2・sec, and the water inside tube 1
However, effective deaeration treatment can be performed without leaking out from the tubular body 2, and the equipment can be made more compact.

製造例 2 外径7.2mm、内径6.0mm、空孔率が70%で、孔径
が1.0μmのポリテトラフルオロエチレンによる内
側チユーブ1に対し、厚さ50μm、空孔率85%、
孔径0.8μmのポリテトラフルオロエチレン多孔質
フイルムによる管状体2を重合し、更にその外側
に外径10.0mm、内径8.0mm、空孔率70%で、孔径
が1.0μmのポリテトラフルオロエチレンチユーブ
3を覆装して本考案の製品を得た。
Manufacturing example 2 Inner tube 1 made of polytetrafluoroethylene with an outer diameter of 7.2 mm, an inner diameter of 6.0 mm, a porosity of 70%, and a pore diameter of 1.0 μm, a thickness of 50 μm, a porosity of 85%,
A tubular body 2 made of polytetrafluoroethylene porous film with a pore diameter of 0.8 μm is polymerized, and a polytetrafluoroethylene tube 3 with an outer diameter of 10.0 mm, an inner diameter of 8.0 mm, a porosity of 70%, and a pore diameter of 1.0 μm is placed on the outside of the tubular body 2. The product of the present invention was obtained by masking.

このものに対し、製造例1におけると同じ条件
で脱気処理した場合、その脱気可能量は、5.0×
10-2c.c./cm2・secであり、内部の水が漏出するこ
とのないことは製造例1と同じであつた。
When this product is degassed under the same conditions as in Production Example 1, the amount that can be degassed is 5.0 ×
10 -2 cc/cm 2 ·sec, and as in Production Example 1, no internal water leaked out.

「考案の効果」 以上説明したような本考案によるときは高い耐
液圧性と高通気性とを具備した高性能な脱気用チ
ユーブを提供し得るもので、各種工業の高精度化
に必要な処理液の脱気処理を小型な機構において
高効率且つ低コストに実施し得るものであるから
工業的にその効果の大きい考案である。
``Effect of the invention'' The invention as explained above can provide a high-performance deaeration tube with high liquid pressure resistance and high air permeability, which is necessary for high precision in various industries. This invention is industrially very effective because it allows the degassing treatment of the treatment liquid to be carried out in a small mechanism with high efficiency and at low cost.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本考案の技術的内容を示すものであつ
て、第1図は本考案によるチユーブの断面図、第
2図はそのポリテトラフルオロエチレン多孔質フ
イルムによる管状体の斜面図、第3図はこのポリ
テトラフルオロエチレン多孔質フイルムの1例に
ついての耐水圧と通気量の関係を示した図表、第
4図は従来のポリテトラフルオロエチレン多孔質
チユーブの耐水圧と通気量の関係を示した図表で
ある。 然して前記第1,2図において、1は多孔質チ
ユーブによる内側チユーブ、2は管状体、3は多
孔質チユーブによる外側チユーブ、4は前記管状
体を形成するポリテトラフルオロエチレン多孔質
フイルム、5は融着部を示すものである。
The drawings show the technical contents of the present invention, and Fig. 1 is a cross-sectional view of a tube according to the invention, Fig. 2 is a perspective view of a tubular body made of the polytetrafluoroethylene porous film, and Fig. 3 is a cross-sectional view of a tube according to the invention. A chart showing the relationship between water pressure resistance and air permeability for one example of this polytetrafluoroethylene porous film. Figure 4 is a chart showing the relationship between water pressure resistance and air flow rate for a conventional polytetrafluoroethylene porous tube. It is. In FIGS. 1 and 2, 1 is an inner tube made of a porous tube, 2 is a tubular body, 3 is an outer tube made of a porous tube, 4 is a polytetrafluoroethylene porous film forming the tubular body, and 5 is a porous tube made of a porous tube. This shows the fused part.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 柔軟性を有するポリテトラフルオロエチレンチ
ユーブによる内側チユーブと外側チユーブを有
し、これら内外側チユーブの間にポリテトラフル
オロエチレンによる平均孔径が0.2〜0.8μmで、前
記内外側チユーブの平均孔径より小さい孔径の平
面的延伸多孔質フイルムで形成された管状体を介
装したことを特徴とする脱気用チユーブ。
It has an inner tube and an outer tube made of flexible polytetrafluoroethylene tubes, and the average pore size of polytetrafluoroethylene between these inner and outer tubes is 0.2 to 0.8 μm, which is smaller than the average pore size of the inner and outer tubes. A degassing tube characterized in that a tubular body formed of a planar stretched porous film is inserted therein.
JP1986138026U 1986-09-10 1986-09-10 Expired - Lifetime JPH0532162Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1986138026U JPH0532162Y2 (en) 1986-09-10 1986-09-10

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1986138026U JPH0532162Y2 (en) 1986-09-10 1986-09-10

Publications (2)

Publication Number Publication Date
JPS6343609U JPS6343609U (en) 1988-03-23
JPH0532162Y2 true JPH0532162Y2 (en) 1993-08-18

Family

ID=31042630

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1986138026U Expired - Lifetime JPH0532162Y2 (en) 1986-09-10 1986-09-10

Country Status (1)

Country Link
JP (1) JPH0532162Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2780331B2 (en) * 1989-04-28 1998-07-30 日東電工株式会社 Liquid degassing method
JP5133039B2 (en) * 2007-12-07 2013-01-30 日東電工株式会社 Polytetrafluoroethylene porous membrane, method for producing the same, and waterproof air-permeable filter

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5343883U (en) * 1976-09-17 1978-04-14

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5173350U (en) * 1974-12-04 1976-06-09

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5343883U (en) * 1976-09-17 1978-04-14

Also Published As

Publication number Publication date
JPS6343609U (en) 1988-03-23

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