JP3375374B2 - Degassing device - Google Patents

Degassing device

Info

Publication number
JP3375374B2
JP3375374B2 JP12015793A JP12015793A JP3375374B2 JP 3375374 B2 JP3375374 B2 JP 3375374B2 JP 12015793 A JP12015793 A JP 12015793A JP 12015793 A JP12015793 A JP 12015793A JP 3375374 B2 JP3375374 B2 JP 3375374B2
Authority
JP
Japan
Prior art keywords
tubular
impermeable membrane
liquid impermeable
liquid
membrane
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 - Fee Related
Application number
JP12015793A
Other languages
Japanese (ja)
Other versions
JPH06327904A (en
Inventor
裕志 新免
貞勝 浜崎
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.)
W.L.Gore&Associates G.K.
W.L.Gore&Associates,Co.,LTD.
Japan Gore Tex Inc
Original Assignee
W.L.Gore&Associates G.K.
W.L.Gore&Associates,Co.,LTD.
Japan Gore Tex Inc
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 W.L.Gore&Associates G.K., W.L.Gore&Associates,Co.,LTD., Japan Gore Tex Inc filed Critical W.L.Gore&Associates G.K.
Priority to JP12015793A priority Critical patent/JP3375374B2/en
Publication of JPH06327904A publication Critical patent/JPH06327904A/en
Application granted granted Critical
Publication of JP3375374B2 publication Critical patent/JP3375374B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Degasification And Air Bubble Elimination (AREA)
  • Physical Water Treatments (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は脱気装置に係わり、より
詳しくは、流体を収容又は輸送する装置又は部品に簡単
に取り付けて不所望なガスを脱気することを可能にする
脱気装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a degassing device, and more particularly to a degassing device that can be easily attached to a device or component for containing or transporting fluids to degas unwanted gases. Regarding

【0002】[0002]

【従来の技術】各種プラントや装置、部品での空気抜き
やガス抜きは従来から行われているが、その方法は空気
やガスが溜まると予想される場所に予めバルブを設置
し、プラントや装置を動かす時に保安要員が立ち合って
バルブを開閉することによって空気やガスを抜いてい
た。
2. Description of the Related Art Air venting and gas venting in various plants, equipment and parts have been performed conventionally, but the method is to install valves in advance where air and gas are expected to accumulate, When moving, the security personnel stood by and opened and closed the valve to remove air and gas.

【0003】また、通気性、液体不透過膜を用いて流路
を形成し、流路の外側を減圧雰囲気として、この流路に
液体を流すことにより脱気を行う方法も知られている
(例えば特開昭51-28261号公報、特開昭55−121806号公
報、特開昭58-62637号公報等)。しかしながらこれ等の
方法は設備が大がかりとなり、本発明の目的を達成する
ことが出来ない。
A method is also known in which a channel is formed by using a gas-permeable, liquid-impermeable film, a depressurized atmosphere is formed on the outside of the channel, and a liquid is allowed to flow through the channel to perform deaeration. For example, JP-A-51-28261, JP-A-55-121806 and JP-A-58-62637). However, these methods require large-scale equipment and cannot achieve the object of the present invention.

【0004】[0004]

【発明が解決しようとする課題】上記の如き従来のプラ
ントや装置での空気抜き、ガス抜きでは、メンテナンス
の人達がプラント等の装置を動かす時又は停止する時に
プラントや装置の各所にあるバルブの場所にいちいち出
向いてバルブを開閉しており、大変に不便であった。
In air venting and gas venting in conventional plants and equipment as described above, the location of valves in various places of plants and equipment when maintenance personnel move or stop equipment such as plants. It was very inconvenient to visit each and open and close the valve.

【0005】また、各種プラントや装置は必ずしも水だ
けではなく、高温の温水、油脂類、硫酸や塩酸等の化学
薬品もあり、また液体の圧力も高く、作業者は非常に危
険な状態でバルブの開閉を強いられていた。そこで、本
発明は、プラントや装置において使用され、バルブの開
閉なしで、常時空気やガスを抜き、かつ液体は通過させ
ない、安全な脱気装置を提供することを目的とする。
In addition, not only water but also hot water of high temperature, oils and fats, and chemicals such as sulfuric acid and hydrochloric acid are used in various plants and equipment, and the pressure of liquid is high, so that the operator can operate the valve in a very dangerous state. Was forced to open and close. Therefore, an object of the present invention is to provide a safe degassing device which is used in a plant or an apparatus and which constantly vents air and gas and does not allow liquid to pass without opening and closing valves.

【0006】[0006]

【課題を解決するための手段】本発明は、上記目的を達
成するために、脱気すべき流体を収容又は輸送する装置
又は部品等に液密に取り付け可能な端部と筒状通気性液
体不透過膜を装着するための筒状部とを有する脱気装置
本体に、該本体の該端部から筒内を通って該筒状部の側
面に通ずる空隙部を設け、かつ該筒状通気性液体不透過
膜を該筒状部の側面に存在する該空隙部の開口部を覆う
ように該筒状部に液密に装着して成り、かつ該筒状通気
性液体不透過膜は非晶質フルオロポリマーで処理された
膜又は通気性液体不透過多孔質膜のみを複数層巻回一体
化して作成された膜で構成され、よって前記流体から該
筒状通気性液体不透過膜を介して装置外へ気体を選択的
に透過せしめることを特徴とする脱気装置を提供する。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides an end portion and a cylindrical breathable liquid which can be liquid-tightly attached to a device or a component for containing or transporting a fluid to be degassed. A degassing apparatus main body having a tubular portion for mounting an impermeable membrane, a void portion is provided from the end portion of the main body through the inside of the tubular body to the side surface of the tubular portion, and the tubular ventilation is provided. Permeable liquid impermeable membrane is liquid-tightly attached to the tubular portion so as to cover the opening of the cavity existing on the side surface of the tubular portion, and the tubular permeable liquid impermeable membrane is non-permeable. Multiple layers wound only with a film treated with crystalline fluoropolymer or a porous film impermeable to air-permeable liquid
( EN) A deaeration device comprising a membrane formed by converting the fluid into a gas, and selectively permeating gas from the fluid to the outside of the device through the tubular permeable liquid impermeable membrane.

【0007】本発明の特徴の1つは、通気性液体不透過
膜を用いてプラントや装置内の流体から空気やガスを抜
くことにある。本発明で用いる通気性液体不透過膜は、
通気性が有り、液体を透過させない性質を有するもので
ある。この様なものとしては、合成樹脂より得られる公
知の連続多孔質体が使用可能である。ポリエチレン、ポ
リプロピレン等のポリオレフィン樹脂の連続多孔質体を
用いる場合は、フッ素系撥水剤、シリコーン系撥水剤等
により撥水処理を付与するのがよい。フッ素樹脂多孔質
体としては、ポリテトラフルオロエチレン、テトラフル
オロエチレン/ヘキサフルオロプロピレン共重合体、ポ
リフッ化ビニル、ポリフッ化ビニリデン等の多孔質体が
使用出来るが、なかでもポリテトラフルオロエチレンを
延伸処理して得られる多孔質膜は、耐薬品性、耐熱性、
耐圧性に優れ好ましい。多孔質ポリテトラフルオロエチ
レン膜は、焼成品でも未焼成品でもよい。
One of the features of the present invention is to remove air or gas from the fluid in the plant or equipment by using the gas permeable liquid impermeable membrane. The breathable liquid impermeable membrane used in the present invention,
It has the property of being breathable and impermeable to liquids. As such a material, a known continuous porous body obtained from a synthetic resin can be used. When using a continuous porous body of a polyolefin resin such as polyethylene or polypropylene, it is preferable to apply a water repellent treatment with a fluorine type water repellent, a silicone type water repellent or the like. As the fluororesin porous material, polytetrafluoroethylene, tetrafluoroethylene / hexafluoropropylene copolymer, polyvinyl fluoride, polyvinylidene fluoride, or other porous material can be used. Among them, polytetrafluoroethylene is stretched. The resulting porous film has chemical resistance, heat resistance,
It has excellent pressure resistance and is preferable. The porous polytetrafluoroethylene film may be a fired product or a non-fired product.

【0008】本発明の第2の特徴は、通気性液体不透過
膜を筒状で用いることである。筒状にすることによって
下記第3の特徴とも関連するが、大面積で高強度の通気
性液体不透過膜を得ることができ、加圧下のプラントや
装置においても通気性液体不透過膜の有効面積を大きく
脱気効率が高いかつ安全な脱気装置として用いることが
可能になる。ちなみに、通気性液体不透過膜をフィルム
状またはシート状として用いても本発明の目的を達成で
きない。さらに、本発明の筒状通気性液体不透過膜は非
晶質フルオロポリマーで処理された膜又は通気性液体不
透過多孔質膜のみを複数層巻回一体化して作成された膜
で構成されていることを特徴とする。筒状通気性液体不
透過膜をこのように構成することにより、筒状通気性液
体不透過膜の耐圧性あるいは強度をさらに向上させるこ
とができ、耐圧性および強度が要求される各種プラント
や装置等におけるガス抜き用途に適することができる。
The second feature of the present invention is that the breathable liquid impermeable membrane is used in a tubular shape. By making it cylindrical, it is possible to obtain a high-strength breathable liquid-impermeable membrane with a large area even though it is related to the following third feature, and the breathable liquid-impermeable membrane is effective even in a plant or a device under pressure. It can be used as a safe degassing device with a large area and high degassing efficiency. By the way, even if the breathable liquid-impermeable membrane is used in the form of a film or sheet, the object of the present invention cannot be achieved. Further, the tubular breathable liquid impermeable membrane of the present invention is a membrane or breathable liquid impermeable membrane treated with an amorphous fluoropolymer.
It is characterized in that it is composed of a membrane formed by winding a plurality of layers of a permeable porous membrane alone . By configuring the tubular breathable liquid impermeable membrane in this way, it is possible to further improve the pressure resistance or strength of the tubular breathable liquid impermeable membrane, and various plants and devices that require pressure resistance and strength. It is suitable for degassing applications such as.

【0009】本発明の第3の特徴は、通気性液体不透過
膜が筒状であることにより、本体の筒状部に装着する際
に、筒状の膜の両端部で装着する構造が可能になり、特
に天然ゴムや合成ゴム等で形成されているOリングを介
して通気性液体不透過膜を上から金属リングでカシメる
方法を採用することができ、これらによって特に耐圧
性、耐経時変化に優れた液密の装着を可能にする。ちな
みに通気性液体不透過膜を単に上部よりカシメたり、押
えたりしても経時変化を起し、内圧や外圧により容易に
リークを起こすことが判明した。
A third feature of the present invention is that the breathable liquid-impermeable membrane has a tubular shape, so that when it is attached to the tubular portion of the main body, it can be attached at both ends of the tubular membrane. In particular, it is possible to adopt a method in which the breathable liquid-impermeable membrane is caulked from above with a metal ring through an O-ring formed of natural rubber or synthetic rubber. Enables liquid-tight mounting that excels in changes. By the way, it was found that even if the breathable liquid impermeable membrane is simply crimped or pressed from above, it will change over time and easily leak due to internal or external pressure.

【0010】一般的に、プラントや装置等でよく使用さ
れる圧力は0〜1kg/cm2 、0〜10kg/cm2 、10〜
20kg/cm2 等であり、このような圧力に耐える通気性
液体不透過膜は多孔質ポリテトラフルオロエチレンの膜
厚を変更して対応可能であるが、本発明では一般的に膜
厚5〜2000μm、多孔質の孔径0.01〜5μm、
空孔率30〜90%の範囲内の多孔質ポリテトラフルオ
ロエチレンを好ましく使用することができ、この場合の
耐圧力性の範囲は0〜20kg/cm2 の範囲である。
[0010] Generally, the pressure is often used in plant and equipment such as 0~1kg / cm 2, 0~10kg / cm 2, 10~
The air-permeable liquid impermeable membrane that withstands such a pressure is 20 kg / cm 2 or the like, and the film thickness of the porous polytetrafluoroethylene can be changed to deal with it. 2000 μm, porous pore size 0.01 to 5 μm,
Porous polytetrafluoroethylene having a porosity in the range of 30 to 90% can be preferably used, and the pressure resistance range in this case is in the range of 0 to 20 kg / cm 2 .

【0011】本発明に於ては、通気性液体不透過膜の耐
圧力性を向上させる為、さらにこの膜を非晶質フルオロ
ポリマーで処理することができる。非晶質フルオロポリ
マーとしては、60〜90%のパーフルオロ−2,2−
ジメチル−1,3−ジオキソールと、10〜40モル%
のテトラフルオロエチレン、及び任意に少量のその他の
モノマーよりなる非晶質コポリマーが好ましい。この非
晶質コポリマーの例としては、デュポン社の「テフロン
AF1600」(ジオキソール単位が約65モル%の商
品)、「テフロンAF2400」(ジオキソール単位が
約85モル%の商品)などがある。
In the present invention, in order to improve the pressure resistance of the breathable liquid-impermeable membrane, this membrane can be further treated with an amorphous fluoropolymer. As the amorphous fluoropolymer, 60 to 90% of perfluoro-2,2-
Dimethyl-1,3-dioxole, 10-40 mol%
Amorphous copolymers of tetrafluoroethylene of ## STR3 ## and optionally small amounts of other monomers are preferred. Examples of this amorphous copolymer include “Teflon AF1600” (a product containing about 65 mol% of dioxole units) and “Teflon AF2400” (a product containing about 85 mol% of dioxole units) manufactured by DuPont.

【0012】このような非晶質フルオロポリマーは溶剤
として、例えばペルフルオロ(2−ブチルテトラヒドロ
フラン)〔住友スリーエム社の「フロリナートFC−7
5」として入手可能〕に溶解して、得られる溶液を通気
性液体不透過膜の処理液とする。この溶液は、この膜の
通気性を残すために希釈する必要があり、通常は0.0
1〜5.0重量%の濃度が好ましい。
Such an amorphous fluoropolymer is used as a solvent, for example, perfluoro (2-butyltetrahydrofuran) [“Fluorinert FC-7” manufactured by Sumitomo 3M Ltd.].
5) ”, and the resulting solution is used as a treatment liquid for the gas permeable liquid impermeable membrane. This solution needs to be diluted to leave the membrane breathable, typically 0.0
A concentration of 1 to 5.0% by weight is preferred.

【0013】この溶液で通気性液体不透過膜を処理する
方法は特に限定されず、コーティング、含浸、スプレー
法等により処理できる。処理した材料は風乾もしくは熱
処理して溶剤を蒸発させる。筒状通気性液体不透過膜、
特に筒状多孔質ポリテトラフルオロエチレン膜の製造方
法としては、チューブ状に押出成形する方法、フィルム
を筒状にロール巻してチューブを成形する方法、これら
の組合せ等の方法を採用することができる。強度の観点
からは少なくともフィルムを組み合わせた製品が好まし
い。押出チューブは一軸延伸に限られるが、フィルムは
2軸延伸が可能であるため、強度に方向性がなくなるか
らと考えられる。
The method for treating the gas-permeable liquid-impermeable membrane with this solution is not particularly limited, and it can be treated by coating, impregnation, spraying or the like. The treated material is air dried or heat treated to evaporate the solvent. Tubular breathable liquid impermeable membrane,
In particular, as a method for producing a tubular porous polytetrafluoroethylene film, a method of extruding into a tubular shape, a method of rolling a film into a tubular shape to form a tube, or a method of combining these may be adopted. it can. From the viewpoint of strength, a product in which at least a film is combined is preferable. It is considered that the extruded tube is limited to uniaxial stretching, but the film can be biaxially stretched, so that the strength has no directionality.

【0014】[0014]

【作用】金具と一体化した取り付け容易な簡易構造であ
り、かつ人為的なバルブの開閉操作なしで、常時、液体
を透過させないで空気又はガスを抜くことができるの
で、操作員の労力を大幅に削減でき、また安全性も向上
する。
[Operation] It has a simple structure that is integrated with the metal fittings and is easy to install, and since it is possible to vent air or gas without allowing liquid to pass through at all times without artificial opening / closing of the valve, the labor of the operator is greatly reduced. Can be reduced and the safety is improved.

【0015】[0015]

【実施例】図1に本発明の実施例の脱気装置の断面を示
す。装置本体1はステンレス鋼製(例えば、SUS30
4)で、プラント又は装置等に取り付けるための手段
(テーパネジ溝)3を有する端部2と、筒状通気性液体
不透過膜5を装着するための筒状部4とを含む。装置本
体1はステンレス鋼製に限られず、金属、セラミックス
などの各種の材料を用いることができるが、剛性、耐蝕
性等からステンレス鋼が好ましい。端部2の取り付け手
段3はプラント又は装置等に液密に取り付け可能であれ
ばよく、ネジ溝に限られないことは勿論である。
EXAMPLE FIG. 1 shows a cross section of a deaerator according to an example of the present invention. The device body 1 is made of stainless steel (for example, SUS30
In 4), it includes an end portion 2 having means (tapered thread groove) 3 for attaching to a plant or an apparatus and the like, and a tubular portion 4 for mounting a tubular gas-permeable liquid impermeable membrane 5. The device body 1 is not limited to stainless steel, and various materials such as metal and ceramics can be used, but stainless steel is preferable from the viewpoint of rigidity, corrosion resistance and the like. It is needless to say that the attaching means 3 of the end portion 2 is not limited to the thread groove as long as it can be attached to the plant or the device in a liquid-tight manner.

【0016】装置本体1の内側には、端部2から筒状部
4の筒状通気性液体不透過膜5を装着する側面へ至る空
隙部6を有する。この空隙部6の内径(寸法)はプラン
ト又は装置等の脱気されるべき流体、特に気体が自由に
抵抗なく流入できる程度に大きければよい。空隙部6の
構造は図1の如く1つ穴である必要はなく、例えば、入
口と出口を持つ2方向性の構造でもよい。
Inside the apparatus main body 1, there is a void portion 6 extending from the end portion 2 to the side surface of the tubular portion 4 on which the tubular air-permeable liquid impermeable membrane 5 is mounted. The inner diameter (dimension) of the void 6 may be large enough to allow a fluid to be degassed, such as a plant or a device, particularly a gas, to freely flow without resistance. The structure of the void 6 does not have to be a single hole as shown in FIG. 1, and may be, for example, a bidirectional structure having an inlet and an outlet.

【0017】装置本体1の筒状部4の周りに筒状通気性
液体不透過膜5を装着するが、この実施例では筒状通気
性液体不透過膜5と筒状部4の間にOリング7を用い、
これと対応する筒状通気性液体不透過膜5の外側に金属
製リング8を用い、この金属製リング8をカシメること
によって筒状通気性液体不透過膜5を筒状部4に液密に
装着する。このとき、カシメによってもOリング7が必
要以上に変形しないような構造、高さに筒状部4のOリ
ング7受けを作成する。このような構造にすることによ
って、筒状通気性液体不透過膜5が経時変化してもOリ
ング7の弾性によって液体のリークが防止される。Oリ
ング7はシリコーン、含フッ素ゴム等の製品を使用する
と耐薬品性に優れることができる。また、筒状通気性液
体不透過膜5の装着方法はカシメに限定されず、ハドメ
式締めつけ等でもよいが、カシメによれば多孔質ポリテ
トラフルオロエチレン膜を充実膜にしたり、一定のカシ
メ率で安定な製品を作成できるなどの点で好ましい。
A tubular breathable liquid impermeable membrane 5 is mounted around the tubular portion 4 of the apparatus main body 1. In this embodiment, O is provided between the tubular breathable liquid impermeable membrane 5 and the tubular portion 4. Using ring 7,
A metal ring 8 is used on the outer side of the tubular breathable liquid impermeable membrane 5 corresponding to this, and the metal breathable ring 5 is caulked to seal the tubular breathable liquid impermeable membrane 5 to the tubular portion 4. Attach to. At this time, the O-ring 7 receiver of the tubular portion 4 is formed in a structure and height such that the O-ring 7 is not deformed more than necessary even by caulking. With such a structure, even if the tubular permeable liquid impermeable membrane 5 changes with time, the elasticity of the O-ring 7 prevents the liquid from leaking. If the O-ring 7 is made of a product such as silicone or fluorine-containing rubber, it can have excellent chemical resistance. Further, the method of mounting the tubular breathable liquid impermeable membrane 5 is not limited to caulking, but may be a tightening method such as a tightening method. It is preferable in that a stable product can be produced.

【0018】また、この筒状通気性液体不透過膜5の装
着の際、筒状通気性液体不透過膜5と装置本体1の筒状
部4の外周面との間には空隙9が形成されるようにし
て、筒状通気性液体不透過膜5のできるだけ広い面積で
内部流体と接して脱気効率を高めるようにする。筒状通
気性液体不透過膜5は、金属製パイプ(マンドレル)の
表面に例えば膜厚30μm、空孔率70%、最大孔径
0.30μmの未焼成延伸ポリテトラフルオロエチレン
フィルムを膜厚が0.5mmになるまで複数枚ロール巻き
して焼成(ヒートロック)し、それから金属製パイプか
ら取出して、長さ45mm、内径14mmφの多孔質ポリテ
トラフルオロエチレンチューブを得る。この多孔質ポリ
テトラフルオロエチレンチューブを装置本体1のステン
レス製筒状部4に上記の如くして取り付ける。
When the tubular breathable liquid impermeable membrane 5 is attached, a gap 9 is formed between the tubular breathable liquid impermeable membrane 5 and the outer peripheral surface of the tubular portion 4 of the apparatus body 1. In this way, the cylindrical air-permeable liquid impermeable membrane 5 is brought into contact with the internal fluid in the largest possible area to enhance the degassing efficiency. The tubular breathable liquid impermeable membrane 5 has, for example, an unfired stretched polytetrafluoroethylene film having a thickness of 30 μm, a porosity of 70%, and a maximum pore diameter of 0.30 μm on the surface of a metal pipe (mandrel). A plurality of rolls are rolled up to 0.5 mm and fired (heat lock), and then taken out from the metal pipe to obtain a porous polytetrafluoroethylene tube having a length of 45 mm and an inner diameter of 14 mmφ. This porous polytetrafluoroethylene tube is attached to the stainless steel tubular portion 4 of the apparatus main body 1 as described above.

【0019】このようにして得られる多孔質ポリテトラ
フルオロエチレンチューブは、通常、耐水性4.5kg/
cm2 以上、耐破壊圧力20kg/cm2 以上である。なお、
多孔質ポリテトラフルオロエチレン膜の最大孔径を0.
2μmにすると膜厚60μm、空孔率75%で耐水圧4
kg/cm2 、耐破壊圧力4.8kg/cm2 になり、また最大
孔径0.2μm、空孔率50%、膜厚30μmの膜を積
層し焼成後の膜厚が2mmであると耐水圧10kg/cm2
耐破壊圧力50kg/cm2 以上であった。
The porous polytetrafluoroethylene tube thus obtained usually has a water resistance of 4.5 kg /
cm 2 or more, puncture resistance 20 kg / cm 2 or more. In addition,
The maximum pore size of the porous polytetrafluoroethylene membrane is 0.
When the thickness is 2 μm, the film thickness is 60 μm, the porosity is 75%, and the water pressure resistance is 4
kg / cm 2 and rupture resistance of 4.8 kg / cm 2 , and when the maximum film thickness is 0.2 μm, the porosity is 50%, and the film thickness is 30 μm, the water pressure resistance is 2 mm. 10 kg / cm 2 ,
The puncture resistance was 50 kg / cm 2 or more.

【0020】そして、これらの多孔質ポリテトラフルオ
ロエチレンチューブをOリングを使ってカシメて上記の
如く装着したところ、いずれの場合にも液体のリークは
認められなかった。次いで、こうして製造した脱気装置
に空気と水の混合体を入れ、10kg/cm2で加圧して試
験したところ、空気は瞬時に透過し、水は50時間後も
なんら漏れず、実際にプラント等で使用できることが確
認できた。また、80℃の温水を入れて10kg/cm2
加圧して試験したところ、水蒸気が微量透過したが、温
水の漏れはなかった。
When these porous polytetrafluoroethylene tubes were caulked with O-rings and mounted as described above, no liquid leak was observed in any case. Next, when a mixture of air and water was put into the deaerator manufactured in this way and tested by pressurizing at 10 kg / cm 2 , the air permeated instantly and water did not leak even after 50 hours. It was confirmed that it can be used in the same way. In addition, when hot water of 80 ° C. was added and the pressure was increased to 10 kg / cm 2 , a test was conducted, but a slight amount of water vapor was transmitted, but there was no leakage of hot water.

【0021】図2〜4を参照して多孔質ポリテトラフル
オロエチレンチューブの製造方法について説明する。図
2は多孔質ポリテトラフルオロエチレンフィルム11を
巻いてチューブを製造する様子を示す。ロール状に巻い
た後加熱すれば多孔質ポリテトラフルオロエチレンフィ
ルムは融着する。
A method of manufacturing a porous polytetrafluoroethylene tube will be described with reference to FIGS. FIG. 2 shows a state in which a porous polytetrafluoroethylene film 11 is wound to produce a tube. The porous polytetrafluoroethylene film is fused by winding it in a roll and then heating it.

【0022】図3は押出成形の多孔質ポリテトラフルオ
ロエチレンチューブ12と、このチューブ12の上に多
孔質ポリテトラフルオロエチレンフィルム13を巻き、
焼成する方法を示す。図4は同じく押出成形の多孔質ポ
リテトラフルオロエチレンチューブ12の周りに多孔質
ポリテトラフルオロエチレンフィルム14を巻くが、こ
の多孔質ポリテトラフルオロエチレンフィルム14はテ
ープ状であり、このテープ14をチューブ12の周りに
螺旋状に巻いて複合チューブを製造する態様を示す。
FIG. 3 shows an extruded porous polytetrafluoroethylene tube 12, and a porous polytetrafluoroethylene film 13 wound on the tube 12.
A method of firing will be described. In FIG. 4, a porous polytetrafluoroethylene film 14 is wound around an extrusion-molded porous polytetrafluoroethylene tube 12, and this porous polytetrafluoroethylene film 14 is in the form of a tape. An embodiment of manufacturing a composite tube by spirally winding around 12 is shown.

【0023】図5は本発明の脱気装置を配管系に取り付
けた例を示す。図5中、21は配管、22,23,24
はバルブ、25は本発明の脱気装置である。気体を含ん
だ液体が配管21中を流れて脱気装置25のところを通
過すると分岐管26を介して脱気装置25から気体だけ
が透過し、脱気される。このように、本発明の脱気装置
をプラントや装置等に設置すると、従来の脱気装置(バ
ルブ)の場合のように、空気やガスを含んだ液体が配管
中を流れて音を発生したり、流量の的確な検出を阻害し
たり、流量の不規則を生じたりして、液体供給が円滑に
行われない不都合がなくなり、円滑な液体供給が可能に
なる。
FIG. 5 shows an example in which the deaerator of the present invention is attached to a piping system. In FIG. 5, 21 is piping, 22, 23, 24
Is a valve and 25 is a deaerator of the present invention. When the liquid containing gas flows in the pipe 21 and passes through the deaerator 25, only the gas permeates from the deaerator 25 through the branch pipe 26 and is deaerated. As described above, when the deaerator of the present invention is installed in a plant, a device, or the like, a liquid containing air or gas flows in the pipe to generate sound, as in the case of a conventional deaerator (valve). In addition, there is no problem that the liquid is not smoothly supplied due to the impediment of the accurate detection of the flow rate or the irregularity of the flow rate, and the liquid can be smoothly supplied.

【0024】[0024]

【発明の効果】本発明の脱気装置によれば、簡単な装置
で、人為的なバルブの開閉操作なしで、脱気が可能にな
り、操作、メンテナンスのコストが大幅に低減すると共
に、安全性の点での改善が著しく、また円滑な流体の供
給が可能になる等の効果がある。
According to the deaeration device of the present invention, deaeration can be performed with a simple device without artificial opening / closing operation of the valve, and the operating and maintenance costs can be greatly reduced, and the safety can be improved. There is an effect that the improvement of the property is remarkable and that the fluid can be smoothly supplied.

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

【図1】図1は実施例の脱気装置の断面図である。FIG. 1 is a sectional view of a deaerator of an embodiment.

【図2】図2は多孔質ポリテトラフルオロエチレンチュ
ーブの製造を説明する図である。
FIG. 2 is a diagram explaining the production of a porous polytetrafluoroethylene tube.

【図3】図3は多孔質ポリテトラフルオロエチレンチュ
ーブの製造を説明する図である。
FIG. 3 is a diagram for explaining the production of a porous polytetrafluoroethylene tube.

【図4】図4は多孔質ポリテトラフルオロエチレンチュ
ーブの製造を説明する図である。
FIG. 4 is a diagram for explaining the production of a porous polytetrafluoroethylene tube.

【図5】図5は脱気装置を配管系に設置した様子を示す
図である。
FIG. 5 is a diagram showing a state in which a deaerator is installed in a piping system.

【符号の説明】[Explanation of symbols]

1…脱気装置 2…端部 3…テーパネジ溝 4…筒状部 5…筒状通気性液体不透過膜 6…空隙部 7…Oリング 8…金属製リング 9…空隙 11…多孔質ポリテトラフルオロエチレン膜 12…多孔質ポリテトラフルオロエチレンチューブ 13…多孔質ポリテトラフルオロエチレンフィルム 14…多孔質ポリテトラフルオロエチレンテープ 21…配管 22,23,24…バルブ 26…分岐管 1 ... Deaerator 2 ... end 3 ... Taper thread groove 4 ... Cylindrical part 5 ... Cylindrical breathable liquid impermeable membrane 6 ... void 7 ... O-ring 8 ... Metal ring 9 ... void 11 ... Porous polytetrafluoroethylene film 12 ... Porous polytetrafluoroethylene tube 13 ... Porous polytetrafluoroethylene film 14 ... Porous polytetrafluoroethylene tape 21 ... Piping 22, 23, 24 ... Valve 26 ... Branch pipe

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平2−283542(JP,A) 特開 平2−273503(JP,A) 特開 昭64−88542(JP,A) 特開 昭60−82107(JP,A) 特開 平2−2802(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 19/00 - 19/04 ─────────────────────────────────────────────────── --Continued from the front page (56) References JP-A-2-283542 (JP, A) JP-A-2-273503 (JP, A) JP-A 64-88542 (JP, A) JP-A 60- 82107 (JP, A) JP-A-2-2802 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) B01D 19/00-19/04

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 脱気すべき流体を収容又は輸送する装置
又は部品等に液密に取り付け可能な端部と筒状通気性液
体不透過膜を装着するための筒状部とを有する脱気装置
本体に、該本体の該端部から筒内を通って該筒状部の側
面に通ずる空隙部を設け、かつ該筒状通気性液体不透過
膜を該筒状部の側面に存在する該空隙部の開口部を覆う
ように該筒状部に液密に装着して成り、かつ該筒状通気
性液体不透過膜は非晶質フルオロポリマーで処理された
膜で構成され、よって前記流体から該筒状通気性液体不
透過膜を介して装置外へ気体を選択的に透過せしめるこ
とを特徴とする脱気装置。
1. A degasser having an end portion that can be mounted in a liquid-tight manner on a device or a component that contains or transports a fluid to be degassed, and a tubular portion for mounting a tubular breathable liquid impermeable membrane. The apparatus main body is provided with a void portion that extends from the end of the main body through the inside of the cylinder to the side surface of the tubular portion, and the tubular breathable liquid impermeable membrane is present on the side surface of the tubular portion. Liquid-tightly attached to the tubular portion so as to cover the opening of the void, and the tubular ventilation
Liquid impermeable membrane treated with amorphous fluoropolymer
A degassing device comprising a membrane, and thus selectively permeating gas from the fluid to the outside of the device through the tubular gas-permeable liquid impermeable membrane.
【請求項2】 脱気すべき流体を収容又は輸送する装置
又は部品等に液密に取り付け可能な端部と筒状通気性液
体不透過膜を装着するための筒状部とを有する脱気装置
本体に、該本体の該端部から筒内を通って該筒状部の側
面に通ずる空隙部を設け、かつ該筒状通気性液体不透過
膜を該筒状部の側面に存在する該空隙部の開口部を覆う
ように該筒状部に液密に装着して成り、該筒状通気性液
体不透過膜は通気性液体不透過多孔質膜のみを複数層巻
回一体化して作成された膜で構成され、よって前記流体
から該筒状通気性液体不透過膜を介して装置外へ気体を
選択的に透過せしめることを特徴とする脱気装置。
2. A degasser having an end portion that can be mounted in a liquid-tight manner on a device or a component that stores or transports a fluid to be degassed, and a tubular portion for mounting a tubular breathable liquid impermeable membrane. The apparatus main body is provided with a void portion that extends from the end of the main body through the inside of the cylinder to the side surface of the tubular portion, and the tubular breathable liquid impermeable membrane is present on the side surface of the tubular portion. The tubular breathable liquid is liquid-tightly attached to the tubular portion so as to cover the opening of the void.
The body impermeable membrane consists of only a breathable liquid impermeable porous membrane wound in multiple layers.
A degassing device comprising a membrane integrally formed once , so that gas can be selectively permeated from the fluid to the outside of the device through the tubular permeable liquid impermeable membrane.
【請求項3】 前記筒状部の外側の両端部にOリングを
配置し、前記筒状部の外側を覆うように前記筒状通気性
液体不透過膜を配置し、前記筒状通気性液体不透過膜及
び前記Oリングの外側から金属リングをカシメることに
より、前記筒状通気性液体不透過膜を前記筒状部に対し
て液密に装着して成る請求項1又は2記載の脱気装置。
3. O-rings are provided at both outer ends of the tubular portion.
Place the tubular breathable so as to cover the outside of the tubular part
A liquid impermeable membrane is placed, and the tubular breathable liquid impermeable membrane and
And crimping the metal ring from the outside of the O-ring
From the tubular breathable liquid impermeable membrane to the tubular portion
The deaerator according to claim 1 or 2, which is liquid-tightly mounted .
【請求項4】 前記筒状通気性液体不透過膜が多孔質ポ
リテトラフルオロエチレンからなる請求項1、2又は3
記載の脱気装置。
4. The tubular breathable liquid impermeable membrane is a porous porous membrane.
It consists of litetrafluoroethylene, Claim 1, 2 or 3
The deaerator described.
JP12015793A 1993-05-21 1993-05-21 Degassing device Expired - Fee Related JP3375374B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12015793A JP3375374B2 (en) 1993-05-21 1993-05-21 Degassing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12015793A JP3375374B2 (en) 1993-05-21 1993-05-21 Degassing device

Publications (2)

Publication Number Publication Date
JPH06327904A JPH06327904A (en) 1994-11-29
JP3375374B2 true JP3375374B2 (en) 2003-02-10

Family

ID=14779369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12015793A Expired - Fee Related JP3375374B2 (en) 1993-05-21 1993-05-21 Degassing device

Country Status (1)

Country Link
JP (1) JP3375374B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6418976B2 (en) * 2015-02-19 2018-11-07 三井・ケマーズ フロロプロダクツ株式会社 Multilayer laminate with amorphous fluororesin coating film formed on water repellent surface

Also Published As

Publication number Publication date
JPH06327904A (en) 1994-11-29

Similar Documents

Publication Publication Date Title
EP0791383B1 (en) An assembly for deaeration of liquids
US5888275A (en) Assembly for deaeration of liquids
KR101128592B1 (en) Gas removal device
GB2134812A (en) Liquid filter
EP2366441A1 (en) Axial transfer line degassing
GB2025256A (en) A Gas Transfer Process Using a Hollow Fiber Membrane
JPH0810586A (en) Pipe collecting body and manufacture and use thereof
US11273413B2 (en) Composite ionomer membrane tubing modules and system and methods incorporating same
JP3221095B2 (en) Tubular porous multilayer film and method for producing the same
JP3685289B2 (en) Liquid degassing module
US3581900A (en) Reverse osmosis liquid purification
JP3375374B2 (en) Degassing device
GB2589669A8 (en) Thin wall polyether block amide membrane tubing and module
JP2008073640A (en) Deaeration device
JP3214222B2 (en) Tubular porous composite and method for producing the same
JPH0751505A (en) Method and apparatus for removal of gal dissolved in aqueous solution
US20220001331A1 (en) Membrane Distillation Module and Membrane Distillation Apparatus
JPH07303802A (en) Diaphragm deaeration device
JP2000033245A (en) Fluororesin composite membrane and its production
JP3734585B2 (en) Deaerator
JPH0337681Y2 (en)
US20190291054A1 (en) Composite ion conducting membrane tubing and process of making same
JPH10296005A (en) Method for ultradeaeration of liquid and deaeration apparatus thereof
JPH0788304A (en) Module for removing dissolved gas and supplying gas
JP2006297200A (en) Degassing apparatus

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20021022

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees