JP2010194423A - Deaerator - Google Patents

Deaerator Download PDF

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JP2010194423A
JP2010194423A JP2009040114A JP2009040114A JP2010194423A JP 2010194423 A JP2010194423 A JP 2010194423A JP 2009040114 A JP2009040114 A JP 2009040114A JP 2009040114 A JP2009040114 A JP 2009040114A JP 2010194423 A JP2010194423 A JP 2010194423A
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liquid
deaeration
degassing
parallel
decompression chamber
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JP5416432B2 (en
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Yukihiko Hayashi
志彦 林
Ryosuke Sato
亮介 佐藤
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Junkosha Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a deaerator which can easily change the deaeration treatment amount of liquid at a low cost, occupies a small space, and facilitates installation of vacuum piping. <P>SOLUTION: The deaerator 100 includes a deaerator unit 101 comprising a reducing chamber 110 having openings 111, 112 disposed in two sites, a first sealing member 102 provided with a vacuum suction opening 102a to seal the opening 111, and a second sealing member 103 for sealing the opening 112. The number of arranged deaeration units can be increased and decreased according to the deaeration treatment amount of liquid. As a result, it is structured that one vacuum chamber is provided with one vacuum suction opening, whereby the installation of the vacuum piping can be simplified and the occupation space can be made small, and it is structured that the number of the arranged deaeration units can be easily increased and decreased, whereby coping with a change in the deaeration treatment amount of liquid can be easily performed without requiring time and labor, and cost. <P>COPYRIGHT: (C)2010,JPO&amp;INPIT

Description

本発明は、液体の脱気装置に関する。   The present invention relates to a liquid deaeration device.

従来、液体中の溶存ガスを脱気処理する脱気装置のひとつに、減圧チャンバー内に気体透過性チューブを収容し、この気体透過性チューブの両端を減圧チャンバーに設けられた液体流入口及び液体排出口に接続したものがある。この脱気装置によれば、減圧チャンバーに設けられた真空吸引口から減圧チャンバー内を真空吸引して減圧し、液体流入口から気体透過性チューブへ液体を流入することにより、液体中の溶存ガスを脱気処理して該液体を液体排出口から排出させることができる。   Conventionally, a gas permeable tube is accommodated in a decompression chamber as one of degassing devices for degassing dissolved gas in a liquid, and both ends of the gas permeable tube are provided with a liquid inlet and a liquid provided in the decompression chamber. Some are connected to the outlet. According to this degassing device, the vacuum inside the vacuum chamber is vacuumed from the vacuum suction port provided in the vacuum chamber, and the liquid is introduced into the gas permeable tube from the liquid inlet, so that the dissolved gas in the liquid is discharged. Can be deaerated to discharge the liquid from the liquid outlet.

このような構成の脱気装置において、脱気処理液体の大流量化及び脱気処理の高性能化を図るためには、例えば、減圧チャンバー内における気体透過性チューブを長くするかチューブ本数を増やす必要がある。ところが、チューブ長を長くする場合は、チューブ内での圧力損失が増大するという問題がある。一方、チューブ本数を増やす場合は、圧力損失の増大は回避できるが、単純にチューブ本数を増やすとチューブ端末を融着する際に融着不良が起きて液漏れの発生するおそれ、あるいはそれに伴って、減圧チャンバ−内の真空吸引に悪影響を及ぼすおそれがある。   In the deaeration device having such a configuration, in order to increase the flow rate of the deaeration liquid and to improve the performance of the deaeration process, for example, the gas permeable tube in the decompression chamber is lengthened or the number of tubes is increased. There is a need. However, when the tube length is increased, there is a problem that the pressure loss in the tube increases. On the other hand, if the number of tubes is increased, an increase in pressure loss can be avoided, but if the number of tubes is simply increased, there is a risk that a fusion failure may occur when the tube ends are fused, and liquid leakage may occur. There is a risk of adversely affecting the vacuum suction in the decompression chamber.

そこで、数十本の所定本数の気体透過性チューブを両端部において結束してチューブ束とし、1つのチューブ束を1つの減圧チャンバー内に収容してチューブ束の両端を液体流入口及び液体排出口に接続した脱気装置が提案されている(特許文献1参照)。この脱気装置を複数並列配置し、各脱気装置の液体流入口を並列接続すると共に液体排出口を並列接続することにより、脱気処理液体の大流量化及び脱気処理の高性能化を図ることができる。ところが、この並列型の脱気装置では、各脱気装置の真空吸引口も並列接続する必要があるため、真空配管の取り回しに手間が掛かり、また、減圧チャンバーも個々に必要なため、占有スペースが大きくなるという問題がある。そこで、かかる問題を解消する脱気装置として、複数の液体流入口及び液体排出口を減圧チャンバーに設け、複数のチューブ束を1つの減圧チャンバー内に収容して各チューブ束の両端を各液体流入口及び各液体排出口に接続した一体型の脱気装置が提案されている(特許文献2参照)。   Therefore, dozens of predetermined number of gas permeable tubes are bundled at both ends to form a tube bundle, one tube bundle is accommodated in one decompression chamber, and both ends of the tube bundle are connected to a liquid inlet and a liquid outlet. There has been proposed a deaeration device connected to (see Patent Document 1). A plurality of deaeration devices are arranged in parallel, and the liquid inlets of each deaeration device are connected in parallel and the liquid discharge ports are connected in parallel to increase the flow rate of the deaeration liquid and to improve the performance of the deaeration process. Can be planned. However, in this parallel type deaeration device, it is necessary to connect the vacuum suction port of each deaeration device in parallel, so it takes time to handle the vacuum pipes, and the decompression chambers are also individually required. There is a problem that becomes larger. Therefore, as a deaeration device that solves such a problem, a plurality of liquid inlets and liquid outlets are provided in a decompression chamber, a plurality of tube bundles are accommodated in one decompression chamber, and both ends of each tube bundle are connected to each liquid stream. An integrated deaeration device connected to the inlet and each liquid discharge port has been proposed (see Patent Document 2).

特開平10−57946号公報Japanese Patent Laid-Open No. 10-57946 特開平11−28307号公報Japanese Patent Laid-Open No. 11-28307

上述した特許文献2に記載の一体型の脱気装置では、該脱気装置の最大処理量を超えた量の液体を脱気処理しなければならない場合、もしくは液体の脱気処理量が減少した場合、最大処理量の異なる同様の脱気装置を多数用意しておき、これらの脱気装置から必要な脱気装置を選択して、元の脱気装置に並列接続し、もしくは元の脱気装置と交換する必要がある。このため、最大処理量の異なる多数の脱気装置を保存管理しなければならず、手間やコストが掛かるという問題がある。   In the integrated deaeration device described in Patent Document 2 described above, when the amount of liquid that exceeds the maximum throughput of the deaeration device has to be deaerated, or the amount of liquid deaeration is reduced. In this case, prepare a number of similar degassing devices with different maximum throughputs, select the necessary degassing devices from these degassing devices, and connect them in parallel to the original degassing devices, or It needs to be replaced with a device. For this reason, it is necessary to store and manage a large number of deaeration devices having different maximum processing amounts, which causes a problem of labor and cost.

本発明は、上記のような種々の課題に鑑みなされたものであり、その目的は、液体の脱気処理量を簡易に且つ低コストで可変でき、占有スペースが小さく、真空配管が容易な脱気装置を提供することにある。   The present invention has been made in view of the various problems as described above, and its purpose is to easily and inexpensively change the amount of liquid deaeration, to occupy a small space, and to easily remove vacuum piping. To provide a Qi device.

上記目的達成のため、本発明の脱気装置では、液体流入口、液体排出口、及び2箇所の開口部が設けられた減圧チャンバー、並びに一端が前記液体流入口に接続され、他端が前記液体排出口に接続されて前記減圧チャンバー内に収納された気体透過性チューブを有する脱気ユニットと、真空吸引口が設けられ、一方の前記開口部を密閉する第1密閉部材と、他方の前記開口部を密閉する第2密閉部材とを備え、前記減圧チャンバー内を前記真空吸引口から真空吸引して減圧し、前記液体流入口から前記気体透過性チューブを介して前記液体排出口へと流される液体を脱気処理する脱気装置であって、前記液体の脱気処理量に基づいて前記脱気ユニットの配置数の増減が可能であり、前記脱気ユニットが複数のときは、各減圧チャンバーの前記開口部同士が対向するように該脱気ユニットを並列配置して、対向する前記開口部同士を密着し、並列配置した前記脱気ユニットの両側の前記開口部のうち一方を前記第1密閉部材で密閉し他方を前記第2密閉部材で密閉し、各減圧チャンバーの前記液体流入口を並列接続し前記液体排出口を並列接続した構成とすることを特徴としている。   In order to achieve the above object, in the deaeration device of the present invention, a liquid inlet, a liquid outlet, a decompression chamber provided with two openings, one end is connected to the liquid inlet, and the other is connected to the liquid inlet. A deaeration unit having a gas permeable tube connected to a liquid discharge port and housed in the decompression chamber; a vacuum suction port; a first sealing member for sealing one of the openings; and the other A second sealing member that seals the opening, and the vacuum chamber is vacuum-sucked from the vacuum suction port to depressurize and flow from the liquid inlet to the liquid outlet through the gas permeable tube. A degassing device for degassing the liquid, wherein the number of degassing units can be increased or decreased based on the degassing amount of the liquid. Said chamber The degassing units are arranged in parallel so that the mouths face each other, the openings facing each other are in close contact with each other, and one of the openings on both sides of the degassing units arranged in parallel is the first sealing member. The other is sealed with the second sealing member, the liquid inlets of the decompression chambers are connected in parallel, and the liquid outlets are connected in parallel.

この脱気装置によれば、1つの減圧チャンバーに1つの真空吸引口が設けられた構成であるため、従来の並列型の脱気装置のように各脱気装置の真空吸引口を並列接続する必要がなく、真空配管の取り回しを簡易なものとすることができ、また、従来の並列型の脱気装置のように減圧チャンバーも個々に必要はなく、占有スペースを小さなものとすることができる。また、脱気ユニットの配置数を簡易に増減することができる構成であるため、従来の一体型の脱気装置のように最大処理量の異なる多数の脱気装置を保存管理する必要はなく、液体の脱気処理量が変化しても手間やコストを掛けずに容易に対応することができる。   According to this deaeration device, since one vacuum suction port is provided in one decompression chamber, the vacuum suction ports of the deaeration devices are connected in parallel as in the conventional parallel type deaeration device. There is no need, and the handling of the vacuum piping can be simplified, and there is no need for individual decompression chambers as in the conventional parallel type deaeration device, and the occupied space can be reduced. . In addition, since the number of deaeration units can be easily increased or decreased, there is no need to store and manage a large number of deaeration devices having different maximum throughputs as in the conventional integrated deaeration device, Even if the amount of liquid deaeration is changed, it can be easily handled without labor and cost.

また、本発明の脱気装置では、前記気体透過性チューブは、外周に薄肉チューブが配設されていることを特徴としている。これにより、気体透過性チューブの折れ曲がりを防止することができると共に、隣接する気体透過性チューブの干渉による傷付けを防止することができる。   In the deaeration device of the present invention, the gas permeable tube is characterized in that a thin tube is disposed on the outer periphery. As a result, the gas permeable tube can be prevented from being bent and can be prevented from being damaged due to interference between adjacent gas permeable tubes.

本発明の実施形態に係る脱気装置の断面平面図である。It is a section top view of the deaeration device concerning the embodiment of the present invention. (A)、(B)は、図1の脱気装置を構成する脱気ユニットの断面側面図及び断面平面図である。(A), (B) is the cross-sectional side view and cross-sectional top view of the deaeration unit which comprise the deaeration apparatus of FIG. (A)、(B)は、図1の脱気装置の継手の接続例を示す断面図である。(A), (B) is sectional drawing which shows the connection example of the coupling of the deaeration apparatus of FIG.

以下、本発明の実施形態を、図面を参照して説明する。尚、以下に説明する実施形態は特許請求の範囲に係る発明を限定するものではなく、また実施形態の中で説明されている特徴の組み合わせの全てが本発明の成立に必須であるとは限らない。   Embodiments of the present invention will be described below with reference to the drawings. The embodiments described below do not limit the invention according to the scope of claims, and all combinations of features described in the embodiments are not necessarily essential to the establishment of the present invention. Absent.

図1は、本発明の実施形態に係る脱気装置の断面平面図、図2(A)、(B)は、図1の脱気装置を構成する脱気ユニットの断面側面図及び断面平面図、図3(A)、(B)は、図1の脱気装置の継手の接続例を示す断面図である。この脱気装置100は、図1に示すように、複数(本例では5つ)の脱気ユニット101と、2つのカバー(第1及び第2密閉部材)102,103とを備えている。脱気ユニット101は、中空の直方体状に形成された減圧チャンバー110と、複数本(本例では91本)の気体透過性の中空糸体121の端末部において、その断面がハニカム構造となるように束ねた気体透過性チューブ120とを備えている。脱気装置100は、5つの脱気ユニット101が並列配置されて密着され、その両側にカバー102,103がそれぞれ配置されて密着され、それらが図略のボルト及びナットにより締結されて一体化された構成となっている。   1 is a cross-sectional plan view of a deaeration device according to an embodiment of the present invention, and FIGS. 2A and 2B are a cross-sectional side view and a cross-sectional plan view of a deaeration unit constituting the deaeration device of FIG. FIGS. 3A and 3B are cross-sectional views showing connection examples of joints of the deaeration device of FIG. As shown in FIG. 1, the deaeration device 100 includes a plurality (five in this example) of deaeration units 101 and two covers (first and second sealing members) 102 and 103. The deaeration unit 101 includes a decompression chamber 110 formed in a hollow rectangular parallelepiped shape and a terminal portion of a plurality (91 in this example) of gas-permeable hollow fiber bodies 121 so that the cross section has a honeycomb structure. And a gas permeable tube 120 bundled together. In the deaeration apparatus 100, five deaeration units 101 are arranged in close contact with each other, and covers 102 and 103 are arranged on both sides thereof to be in close contact with each other. It has become the composition.

減圧チャンバー110は、図2に示すように、例えばポリプロピレン(PP)等の樹脂により、対向する2つの側面が開口部111,112となるように形成されている。そして、一方の開口部112の端面には、Oリング等のパッキング材104が嵌め込まれるパッキング溝112aが形成されている。これにより、複数の減圧チャンバー110を並列配置して隣接する減圧チャンバー110の開口部111の端面と開口部112の端面とを密着したときに、該密着面の気密性をパッキング材104により持たせることができる。   As shown in FIG. 2, the decompression chamber 110 is formed of, for example, a resin such as polypropylene (PP) so that two opposing side surfaces become openings 111 and 112. A packing groove 112 a into which a packing material 104 such as an O-ring is fitted is formed on the end surface of one opening 112. Thus, when the plurality of decompression chambers 110 are arranged in parallel and the end face of the opening 111 of the adjacent decompression chamber 110 and the end face of the opening 112 are brought into close contact with each other, the tightness of the contact face is provided by the packing material 104. be able to.

また、減圧チャンバー110の上面には、液体流入口113及び液体排出口114が形成されている。液体流入口113及び液体排出口114には、並列接続用の継手115,116が嵌挿されている。継手115,116は、例えばテトラフルオロエチレン−パーフルオロアルキルビニルエーテル共重合体(PFA)等のフッ素樹脂によりT字状に形成されて上部両端が並列接続可能に形成されているが、終端部分のみはL字状(図1参照)に形成されて上部片端のみが接続可能に形成されている。継手115,116の挿入端部には、オネジ115a,116aが螺設されており、ナット117,118が螺合されていると共に、気体透過性チューブ120に接続されている袋ナット122,123がOリング等のパッキング材124及びフランジ125を介して螺合されている。これにより、継手115,116と気体透過性チューブ120とを接続したときに、該接続部の気密性をパッキング材124により持たせることができる。   A liquid inlet 113 and a liquid outlet 114 are formed on the upper surface of the decompression chamber 110. Joints 115 and 116 for parallel connection are inserted into the liquid inlet 113 and the liquid outlet 114. The joints 115 and 116 are formed in a T shape by a fluororesin such as tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PFA), for example, and the upper ends are formed so that they can be connected in parallel. It is formed in L shape (refer FIG. 1), and only the upper one end is formed so that connection is possible. Male screws 115 a and 116 a are screwed into the insertion ends of the joints 115 and 116, nuts 117 and 118 are screwed together, and cap nuts 122 and 123 connected to the gas permeable tube 120. Screwed together via a packing material 124 such as an O-ring and a flange 125. Thereby, when the joints 115 and 116 and the gas permeable tube 120 are connected, the packing material 124 can provide the airtightness of the connecting portion.

継手115,116の並列接続方法としては、図3(A)に示すように、隣接する継手115,116の上部端面同士を密着して密着外周部分を全周にわたって溶接115b,116bにより接合して継手115,116を並列接続する方法がある。また、図3(B)に示すように、継手115,116の上部一端に円筒状の凹部115c,116c及びOリング等のパッキング材105が嵌め込まれるパッキング溝115d,116dを形成し、継手115,116の上部他端に凹部115c,116cに嵌め込み可能な円筒状の凸部115e,116eを形成することにより継手115,116を並列接続する方法がある。これにより、複数の減圧チャンバー110を並列配置して隣接する減圧チャンバー110の継手115,116を並列接続したときに、継手115,116の気密性を溶接115b,116bもしくはパッキング材105により持たせることができる。   As a method of connecting the joints 115 and 116 in parallel, as shown in FIG. 3 (A), the upper end surfaces of the adjacent joints 115 and 116 are brought into close contact with each other and the tight outer peripheral portions are joined by welding 115b and 116b over the entire circumference. There is a method of connecting the joints 115 and 116 in parallel. Further, as shown in FIG. 3 (B), cylindrical recesses 115c and 116c and packing grooves 115d and 116d into which a packing material 105 such as an O-ring is fitted are formed at upper ends of the joints 115 and 116, respectively. There is a method in which joints 115 and 116 are connected in parallel by forming cylindrical convex portions 115e and 116e that can be fitted into the concave portions 115c and 116c at the other upper end of 116. Accordingly, when the joints 115 and 116 of the adjacent decompression chambers 110 are arranged in parallel and the joints 115 and 116 of the adjacent decompression chambers 110 are connected in parallel, the joints 115 and 116 are made airtight by the welds 115b and 116b or the packing material 105. Can do.

気体透過性チューブ120は、例えばPFA等のフッ素樹脂でなる複数本の気体透過性の中空糸体121が端末部において、その断面がハニカム構造となるように束ねられ、中空糸体121束の外周がPFAでなる薄肉チューブ126で被覆されている。さらに、中空糸体121束の両端部が熱溶着によって溶着されて、該両端部に袋ナット122,123、フランジ125及びパッキング材124が挿入された構成となっている。中空糸体121は、例えば内径0.45mm、外径0.6mm、長さ900mmのものが使用される。   The gas permeable tube 120 is formed by bundling a plurality of gas permeable hollow fiber bodies 121 made of, for example, a fluororesin such as PFA so that the cross section thereof has a honeycomb structure at the terminal portion, and the outer circumference of the bundle of hollow fiber bodies 121 Is covered with a thin tube 126 made of PFA. Furthermore, both ends of the hollow fiber body 121 bundle are welded by heat welding, and the cap nuts 122 and 123, the flange 125, and the packing material 124 are inserted into the both ends. For example, the hollow fiber body 121 having an inner diameter of 0.45 mm, an outer diameter of 0.6 mm, and a length of 900 mm is used.

薄肉チューブ126により、中空糸体121の折れ曲がりを防止することができると共に、隣接する気体透過性チューブ120の干渉による中空糸体121の傷付けを防止することができる。さらに、薄肉チューブ126には、長手方向に破線状のスリットが形成されており、これにより中空糸体121の脱気性能は担保されている。なお、薄肉チューブ126の代わりにPFAでなる薄肉テープや薄肉シートを用いても良い。そして、気体透過性チューブ120は、減圧チャンバー110内部にコイル形状に巻かれた状態で収納され、チューブ両端部が継手115,116の挿入端部にそれぞれ接続されている。   The thin-walled tube 126 can prevent the hollow fiber body 121 from being bent, and can prevent the hollow fiber body 121 from being damaged by the interference of the adjacent gas permeable tubes 120. Further, the thin-walled tube 126 is formed with a slit in the shape of a broken line in the longitudinal direction, thereby ensuring the deaeration performance of the hollow fiber body 121. Instead of the thin tube 126, a thin tape or thin sheet made of PFA may be used. The gas permeable tube 120 is housed in a coiled state in the decompression chamber 110, and both ends of the tube are connected to the insertion ends of the joints 115 and 116, respectively.

カバー102は、例えばPP等の樹脂により矩形板状に形成されており、下部に真空吸引口102aが設けられ、減圧チャンバー110の開口部111の端面と密着する側の面の部分には、Oリング等のパッキング材106が嵌め込まれるパッキング溝102bが形成されている。これにより、カバー102の面と減圧チャンバー110の開口部111の端面とを密着したときに、該接合面の気密性をパッキング材106により持たせることができる。カバー103は、例えばPP等の樹脂により矩形板状に形成されている。なお、カバー102と複数の脱気ユニット101とカバー103とを締結するボルト及びナットは、例えばステンレス等の金属もしくはポリエーテルエーテルケトン(PEEK)等の樹脂により作成されている。   The cover 102 is formed in a rectangular plate shape using, for example, a resin such as PP, and a vacuum suction port 102a is provided in the lower portion. A packing groove 102b into which a packing material 106 such as a ring is fitted is formed. Thereby, when the surface of the cover 102 and the end surface of the opening 111 of the decompression chamber 110 are brought into close contact with each other, the airtightness of the joint surface can be provided by the packing material 106. The cover 103 is formed in a rectangular plate shape using a resin such as PP, for example. The bolts and nuts that fasten the cover 102, the plurality of deaeration units 101, and the cover 103 are made of a metal such as stainless steel or a resin such as polyetheretherketone (PEEK).

この脱気装置100は、以下の手順で組み立てられる。先ず、減圧チャンバー110の液体流入口113及び液体排出口114に継手115,116を嵌挿し、継手115,116の挿入端部のオネジ115a,116aにナット117,118を螺合して締結する。これにより、継手115,116を減圧チャンバー110に固定することができる。そして、気体透過性チューブ120をコイル形状に巻回し、パッキング材124を有するチューブ両端部の袋ナット122,123を継手115,116の挿入端部のオネジ115a,116aに螺合して締結する。これにより、気体透過性チューブ120を気密性を担保しながら減圧チャンバー110内に収納することができる。以上の手順を必要な減圧チャンバー110の数分繰り返す。   This deaeration device 100 is assembled in the following procedure. First, the joints 115 and 116 are inserted into the liquid inlet 113 and the liquid outlet 114 of the decompression chamber 110, and the nuts 117 and 118 are screwed into the male screws 115a and 116a at the insertion ends of the joints 115 and 116, and fastened. Thereby, the joints 115 and 116 can be fixed to the decompression chamber 110. Then, the gas permeable tube 120 is wound into a coil shape, and the cap nuts 122 and 123 at both ends of the tube having the packing material 124 are screwed into the male screws 115a and 116a at the insertion ends of the joints 115 and 116, and fastened. Thereby, the gas permeable tube 120 can be accommodated in the decompression chamber 110 while ensuring airtightness. The above procedure is repeated for the required number of decompression chambers 110.

次に、各減圧チャンバー110の開口部112のパッキング溝112aにパッキング材104を嵌め込むと共に、カバー102のパッキング溝102bにパッキング材106を嵌め込む。そして、各減圧チャンバー110を、開口部111と開口部112とが密着するように、かつT字状の継手115,116(図1の右端の減圧チャンバー110はL字状の継手115,116)の上部端部同士が密着するように並列配置する。そして、図1の左端の減圧チャンバー110の開口部111にカバー102のパッキング溝102b側の面を密着させ、図1の右端の減圧チャンバー110の開口部112にカバー103を密着させる。最後に、図略のボルトをカバー102側から挿入し、各脱気ユニット101からカバー103へ貫通させて図略のナットを螺合して締結する。そして、隣接する継手115,116の上部端面の密着外周部分を全周にわたって溶接115b,116b等により接合する。以上により脱気装置100の組み立てが完了する。   Next, the packing material 104 is fitted into the packing groove 112 a of the opening 112 of each decompression chamber 110, and the packing material 106 is fitted into the packing groove 102 b of the cover 102. And each decompression chamber 110 is formed so that the opening 111 and the opening 112 are in close contact with each other and T-shaped joints 115 and 116 (the decompression chamber 110 at the right end in FIG. 1 is an L-shaped joint 115 and 116). Are arranged in parallel so that the upper ends of the two are in close contact with each other. Then, the packing groove 102b side surface of the cover 102 is brought into close contact with the opening 111 of the decompression chamber 110 at the left end of FIG. 1, and the cover 103 is brought into close contact with the opening 112 of the decompression chamber 110 at the right end of FIG. Finally, a bolt (not shown) is inserted from the cover 102 side, penetrated from each deaeration unit 101 to the cover 103, and a nut (not shown) is screwed and fastened. And the adhesion outer peripheral part of the upper end surface of adjacent joint 115,116 is joined by welding 115b, 116b etc. over the perimeter. Thus, the assembly of the deaeration device 100 is completed.

このような構成の脱気装置100では、各液体流入口113から各気体透過性チューブ120に流入した液体は、一体化された減圧チャンバー110内部が減圧されているので、各気体透過性チューブ120内を通過している間に溶存ガスが脱気され、各液体排出口114から排出される。この脱気装置100によれば、脱気ユニット101に配置される気体透過性チューブ120は、複数本の気体透過性の中空糸体121を束ねた構造であるため、チューブ長を増大する場合と比較して、単位容積当たりの膜面積を広くすることができると共に圧力損失を低減することができ、脱気処理液の大流量化及び脱気処理の高性能化を図ることができる。   In the deaeration device 100 having such a configuration, the liquid flowing into each gas permeable tube 120 from each liquid inlet 113 is depressurized in the integrated decompression chamber 110. While passing through the inside, the dissolved gas is degassed and discharged from each liquid outlet 114. According to this deaeration device 100, since the gas permeable tube 120 arranged in the deaeration unit 101 has a structure in which a plurality of gas permeable hollow fiber bodies 121 are bundled, the tube length is increased. In comparison, the membrane area per unit volume can be widened, the pressure loss can be reduced, the flow rate of the degassing treatment liquid can be increased, and the performance of the degassing treatment can be improved.

さらに、1つの減圧チャンバー110に1つの真空吸引口102aが設けられた構成であるため、従来の並列型の脱気装置のように各脱気装置の真空吸引口を並列接続する必要がなく、真空配管の取り回しを簡易なものとすることができ、また、従来の並列型の脱気装置のように減圧チャンバーも個々に必要はなく、占有スペースを小さなものとすることができる。また、脱気ユニット101の配置数を簡易に増減することができる構成であるため、従来の一体型の脱気装置のように最大処理量の異なる多数の脱気装置を保存管理する必要はなく、液体の脱気処理量が変化しても手間やコストを掛けずに容易に対応することができる。   Furthermore, since one vacuum suction port 102a is provided in one decompression chamber 110, there is no need to connect the vacuum suction ports of the respective degassing devices in parallel as in the conventional parallel type degassing device, The handling of the vacuum piping can be simplified, and the decompression chamber is not required individually as in the conventional parallel type deaeration device, and the occupied space can be reduced. In addition, since the number of arrangement of the deaeration units 101 can be easily increased or decreased, it is not necessary to store and manage a large number of deaeration devices having different maximum throughputs unlike the conventional integrated deaeration device. Even if the amount of liquid deaeration is changed, it can be easily handled without trouble and cost.

なお、本発明の実施形態の減圧チャンバー110は、直方体状に形成したが、円筒状に形成しても良い。   In addition, although the decompression chamber 110 of the embodiment of the present invention is formed in a rectangular parallelepiped shape, it may be formed in a cylindrical shape.

本発明の脱気装置は、脱気された液体を必要とする機器であれば、どのような機器でも適用可能である。例えば、半導体ウエハへのフォトレジスト等の塗布装置や現像装置、液晶製造装置に使用される液体の脱気装置にも適用可能である。特に、高精度の脱気性能を必要とする機器に適用した場合に大きな効果を奏するものである。   The deaeration device of the present invention can be applied to any device as long as the device requires degassed liquid. For example, the present invention can also be applied to a liquid deaeration device used in a coating device for a photoresist on a semiconductor wafer, a developing device, and a liquid crystal manufacturing device. In particular, it has a great effect when applied to a device that requires high-accuracy deaeration performance.

100 脱気装置、101 脱気ユニット、102,103 カバー、102a 真空ク吸引口、110 減圧チャンバー、111,112 開口部、113 液体流入口、114 液体排出口、115,116 継手、120 気体透過性チューブ、121 中空糸体、126 薄肉テープ DESCRIPTION OF SYMBOLS 100 Deaeration apparatus, 101 Deaeration unit, 102,103 cover, 102a Vacuum suction port, 110 Depressurization chamber, 111,112 opening part, 113 Liquid inflow port, 114 Liquid discharge port, 115,116 Joint, 120 Gas permeability Tube, 121 Hollow fiber body, 126 Thin-walled tape

Claims (2)

液体流入口、液体排出口、及び2箇所の開口部が設けられた減圧チャンバー、並びに一端が前記液体流入口に接続され、他端が前記液体排出口に接続されて前記減圧チャンバー内に収納された気体透過性チューブを有する脱気ユニットと、
真空吸引口が設けられ、一方の前記開口部を密閉する第1密閉部材と、
他方の前記開口部を密閉する第2密閉部材とを備え、
前記減圧チャンバー内を前記真空吸引口から真空吸引して減圧し、前記液体流入口から前記気体透過性チューブを介して前記液体排出口へと流される液体を脱気処理する脱気装置であって、
前記液体の脱気処理量に基づいて前記脱気ユニットの配置数の増減が可能であり、前記脱気ユニットが複数のときは、各減圧チャンバーの前記開口部同士が対向するように該脱気ユニットを並列配置して、対向する前記開口部同士を密着し、並列配置した前記脱気ユニットの両側の前記開口部のうち一方を前記第1密閉部材で密閉し他方を前記第2密閉部材で密閉し、各減圧チャンバーの前記液体流入口を並列接続し前記液体排出口を並列接続した構成とすることを特徴とする脱気装置。
A liquid inlet, a liquid outlet, and a decompression chamber provided with two openings, and one end connected to the liquid inlet and the other end connected to the liquid outlet and housed in the decompression chamber. A degassing unit having a gas permeable tube;
A first sealing member provided with a vacuum suction port and sealing one of the openings;
A second sealing member that seals the other opening,
A deaeration device that depressurizes the vacuum chamber from the vacuum suction port to depressurize the liquid flowing from the liquid inlet to the liquid outlet through the gas permeable tube. ,
The number of the degassing units can be increased or decreased based on the amount of degassing treatment of the liquid, and when there are a plurality of degassing units, the degassing is performed so that the openings of the decompression chambers face each other. Units are arranged in parallel, the opening portions facing each other are in close contact, one of the openings on both sides of the deaeration unit arranged in parallel is sealed with the first sealing member, and the other is sealed with the second sealing member. A degassing apparatus characterized in that it is sealed, and the liquid inlets of each decompression chamber are connected in parallel and the liquid outlets are connected in parallel.
前記気体透過性チューブは、外周に薄肉チューブが配設されていることを特徴とする請求項1に記載の脱気装置。   The degassing device according to claim 1, wherein a thin-walled tube is disposed on an outer periphery of the gas permeable tube.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015058544A (en) * 2013-09-17 2015-03-30 セイコーエプソン株式会社 Liquid injection device and liquid supply method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53115677A (en) * 1977-03-18 1978-10-09 Kuraray Co Ltd Fluid treating device having laminated structure
JPH0629604U (en) * 1992-06-10 1994-04-19 三浦工業株式会社 Gas separation membrane module
JPH06165923A (en) * 1992-03-04 1994-06-14 Zenon Environmental Inc Cartridge of wafer of hollow fiber thin film and module with piled cartridge
JPH07108144A (en) * 1993-10-14 1995-04-25 Ishigaki Mech Ind Co Clarifying filter
JPH08233791A (en) * 1994-12-23 1996-09-13 Hewlett Packard Co <Hp> Deaerator for liquid chromatography,basic structure thereof and basic module
JPH1057946A (en) * 1996-08-22 1998-03-03 Nitto Denko Corp Deaerator

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53115677A (en) * 1977-03-18 1978-10-09 Kuraray Co Ltd Fluid treating device having laminated structure
JPH06165923A (en) * 1992-03-04 1994-06-14 Zenon Environmental Inc Cartridge of wafer of hollow fiber thin film and module with piled cartridge
JPH0629604U (en) * 1992-06-10 1994-04-19 三浦工業株式会社 Gas separation membrane module
JPH07108144A (en) * 1993-10-14 1995-04-25 Ishigaki Mech Ind Co Clarifying filter
JPH08233791A (en) * 1994-12-23 1996-09-13 Hewlett Packard Co <Hp> Deaerator for liquid chromatography,basic structure thereof and basic module
JPH1057946A (en) * 1996-08-22 1998-03-03 Nitto Denko Corp Deaerator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015058544A (en) * 2013-09-17 2015-03-30 セイコーエプソン株式会社 Liquid injection device and liquid supply method
US9827779B2 (en) 2013-09-17 2017-11-28 Seiko Epson Corporation Liquid ejecting apparatus and liquid supply method

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