JP2012106154A - Gas-liquid separator - Google Patents

Gas-liquid separator Download PDF

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JP2012106154A
JP2012106154A JP2010255059A JP2010255059A JP2012106154A JP 2012106154 A JP2012106154 A JP 2012106154A JP 2010255059 A JP2010255059 A JP 2010255059A JP 2010255059 A JP2010255059 A JP 2010255059A JP 2012106154 A JP2012106154 A JP 2012106154A
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filter
liquid
exhaust pipe
gas
chamber
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JP5649919B2 (en
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Toshiyuki Seki
利行 関
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TLV Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a gas-liquid separator which improves gas-liquid separation efficiency by causing a separated liquid to easily inflow into a liquid reservoir chamber and prevents relatively early clogging of a filter.SOLUTION: The gas liquid separator is obtained by arranging a swirl vane 12 in a circular space 11 formed by a body 1 and an exhaust pipe 10; by linking the upper side of the swirl vane 12 to an entrance 6; by linking the upper side to an exit 7 through an inside opening of the exhaust pipe 10; by linking the under side of a liquid reservoir chamber 15 to a drainage opening 8 by forming a swirl chamber 14 and the liquid reservoir chamber 15 at the underside of the circular space 11; by arranging a cylindrical filter 22 used for fluid filtration and having a bottom head being in a closed state by a plug 23 in between the exhaust pipe 10 and the liquid reservoir chamber 15; by radially arranging plural impinging plates 24 for falling along an axial direction of the filter 22 in between the external wall of the plug 23 and internal walls of a body 1 and a bottom cover 4, for example, four pieces at right and left and at back and forth; and by arranging plural impinging plates 25 in the outer circumference of the filter 22 along the axial direction of the filter 22, for example, disposing four pieces at right and left and at back and forth.

Description

本発明は、蒸気や圧縮空気や各種ガス等の気体中に混入している復水や凝縮水等の液体をケーシング内に旋回流を起こし遠心力によって分離する気液分離器に関し、特にケーシング内に流体をろ過するフィルターを配置したものに関する。 The present invention relates to a gas-liquid separator that generates a swirling flow in a casing and separates the liquid such as condensate or condensed water mixed in a gas such as steam, compressed air, or various gases by centrifugal force, and particularly in the casing. And a filter for filtering fluid.

従来の気液分離器は、例えば特許文献1に開示されている。これは、ケーシングと排気管で形成する環状空間に旋回羽根を配置し、旋回羽根の上方を入口に連結し、排気管の内側の孔を通してその上方を出口に連結し、環状空間の下方に旋回室と該旋回室の下方に液溜室を形成して該液溜室の下部を排液口に連結し、排気管と液溜室の間に下端部をプラグにより閉止状態とした流体ろ過用の円筒状フィルターを配置し、旋回室と液溜室の間に外側のケーシング内周壁との間に流体通過用の隙間を設けた隔壁部材を配置したものである。 A conventional gas-liquid separator is disclosed in Patent Document 1, for example. This is because the swirl vane is arranged in an annular space formed by the casing and the exhaust pipe, the upper part of the swirl vane is connected to the inlet, the upper part is connected to the outlet through the hole inside the exhaust pipe, and the lower part of the annular space is swirled. A fluid reservoir chamber is formed below the chamber and the swirl chamber, the lower portion of the reservoir chamber is connected to the drainage port, and the lower end portion is closed by a plug between the exhaust pipe and the reservoir chamber. And a partition member having a fluid passage gap between the swirl chamber and the liquid reservoir chamber and the outer peripheral wall of the outer casing.

特開2004−340452号公報Japanese Patent Laid-Open No. 2004-340552

上記従来の気液分離器においては、旋回室の中央よりを旋回している微少な液体が液溜室に流入できないために、分離された液体が再び気体流に巻き込まれて出口に運び出されてしまい気液の分離効率が悪い問題点があった。また、流体をろ過するフィルターがゴミやスケール等の異物の堆積により比較的早期に詰まりを生じるために、頻繁に分解してフィルターを洗浄したり交換したりしなければならない問題点があった。 In the above conventional gas-liquid separator, since the minute liquid swirling from the center of the swirl chamber cannot flow into the liquid reservoir, the separated liquid is again taken up in the gas flow and carried to the outlet. As a result, the gas-liquid separation efficiency was poor. Further, since the filter for filtering the fluid is clogged relatively early due to the accumulation of foreign matters such as dust and scale, there is a problem that the filter must be frequently disassembled to clean or replace the filter.

したがって本発明が解決しようとする課題は、分離された液体が液溜室に流入し易くして気液の分離効率を向上できると共に、フィルターが比較的早期に詰まることを防止できる気液分離器を提供することである。 Therefore, the problem to be solved by the present invention is that the separated liquid can easily flow into the liquid storage chamber to improve the separation efficiency of the gas and liquid, and can prevent the filter from clogging relatively early. Is to provide.

上記の課題を解決するために、本発明の気液分離器は、ケーシングと排気管で形成する環状空間に旋回羽根を配置し、旋回羽根の上方を入口に連結し、排気管の内側の孔を通してその上方を出口に連結し、環状空間の下方に旋回室と該旋回室の下方に液溜室を形成して該液溜室の下部を排液口に連結し、排気管と液溜室の間に下端部をプラグにより閉止状態とした流体ろ過用の円筒状フィルターを配置したものにおいて、プラグの外周壁とケーシングの内周壁との間に円筒状のフィルターの軸方向に沿って流下用衝突板を配置すると共に、円筒状のフィルターの外周囲に円筒状のフィルターの軸方向に沿って分離用衝突板を配置したことを特徴とするものである。 In order to solve the above problems, the gas-liquid separator of the present invention has a swirl vane disposed in an annular space formed by a casing and an exhaust pipe, and the upper part of the swirl vane is connected to an inlet, and a hole inside the exhaust pipe. The upper part is connected to the outlet, a swirl chamber is formed below the annular space, a liquid reservoir chamber is formed below the swirl chamber, and the lower part of the liquid reservoir is connected to the drain port, and the exhaust pipe and the liquid reservoir chamber A cylindrical filter for fluid filtration with the lower end closed by a plug is arranged between the outer peripheral wall of the plug and the inner peripheral wall of the casing, and flows down along the axial direction of the cylindrical filter. A collision plate is disposed, and a separation collision plate is disposed around the outer periphery of the cylindrical filter along the axial direction of the cylindrical filter.

本発明によれば、プラグの外周壁とケーシングの内周壁との間に円筒状のフィルターの軸方向に沿って流下用衝突板を配置したことにより、旋回室の中央よりを旋回している微少な液体が流下用衝突板に衝突して流下用衝突板に沿って液溜室に流下するので、分離された液体が液溜室に流入し易くなるという効果を奏する。また、円筒状のフィルターの外周囲に円筒状のフィルターの軸方向に沿って分離用衝突板を配置したことにより、粒度の小さな異物が分離用衝突板に衝突して分離され分離用衝突板から流下用衝突板に沿って液溜室に流下するので、フィルターが比較的早期に詰まることを防止できるという効果を奏する。 According to the present invention, since the collision plate for the flow-down is arranged along the axial direction of the cylindrical filter between the outer peripheral wall of the plug and the inner peripheral wall of the casing, the microscopic swirl from the center of the swirl chamber is achieved. Since the liquid collides with the falling collision plate and flows down along the falling collision plate into the liquid reservoir chamber, there is an effect that the separated liquid easily flows into the liquid reservoir chamber. Further, by arranging the separation collision plate along the axial direction of the cylindrical filter around the outer circumference of the cylindrical filter, a small particle size foreign matter collides with the separation collision plate and is separated from the separation collision plate. Since it flows down to the liquid storage chamber along the falling collision plate, it is possible to prevent the filter from being clogged relatively early.

本発明の実施の形態に係わる気液分離器の断面図である。It is sectional drawing of the gas-liquid separator concerning embodiment of this invention.

以下、本発明の実施の形態について、図1を参照して説明する。ケーシングは円筒状本体1と出入口部材2をクランプ継手3で結合し、本体1の下部に底蓋4を溶接により結合して形成する。出入口部材2には左右同軸上に入口6と出口7を設け、上端中央にプラグ孔5を設ける。プラグ孔5は逆洗用の流体配管を接続したり圧力計を接続したりするために使用する。底蓋4には下端中央に排液口8を設ける。出入口部材2に連通口9を開けた弁座16をネジ結合する。出入口部材2と弁座16の間には排気管10の上端の内向きフランジを間に挟むことにより、排気管10を出入口部材2に固定する。排気管10は二重のほぼ円筒形状で、内側円筒の上下端部を末広がりに形成する。排気管10の外側円筒は省略して本体1で兼用することもできる。排気管10の内外円筒の間に形成される環状空間11に、排気管10と一体に旋回羽根12を形成する。 Hereinafter, an embodiment of the present invention will be described with reference to FIG. The casing is formed by connecting the cylindrical main body 1 and the entrance / exit member 2 with a clamp joint 3 and connecting the bottom lid 4 to the lower part of the main body 1 by welding. The inlet / outlet member 2 is provided with an inlet 6 and an outlet 7 on the left and right coaxial axes, and a plug hole 5 is provided at the center of the upper end. The plug hole 5 is used for connecting a fluid pipe for backwashing or connecting a pressure gauge. The bottom lid 4 is provided with a drainage port 8 at the center of the lower end. The valve seat 16 having the communication port 9 opened is connected to the doorway member 2 by screws. The exhaust pipe 10 is fixed to the entrance / exit member 2 by sandwiching an inward flange at the upper end of the exhaust pipe 10 between the entrance / exit member 2 and the valve seat 16. The exhaust pipe 10 has a double, substantially cylindrical shape, and the upper and lower end portions of the inner cylinder are formed so as to spread outwardly. The outer cylinder of the exhaust pipe 10 can be omitted, and the main body 1 can also be used. A swirl vane 12 is formed integrally with the exhaust pipe 10 in an annular space 11 formed between the inner and outer cylinders of the exhaust pipe 10.

入口4は連通孔13を通して下方の環状空間11に連結し、排気管10の内側は弁座16の連通口9を介して上方の出口5に連結する。本体1の下部内面と底蓋6の内面との間に旋回室14と、この旋回室14の下方に液溜室15を形成し、液溜室15の下端を排液口8に連結する。旋回室14と排気管10の内側に長尺円筒状の中空フィルター22を配置する。フィルター22は上端を弁座16に溶接により固定し、下端部にプラグ23を溶接により固定して閉止状態とする。フィルター22は多数の微細な貫通孔を有し、入口4と環状空間11を流下してきた流体からゴミやスケール等の異物を捕捉して流体を出口5側へ排出するものである。フィルター22のろ過粒度は0.5マイクロから10マイクロ程度が好適である。フィルター22は全長の約半分が排気管10内に位置し、残りの約半分が旋回室14内に位置する。 The inlet 4 is connected to the lower annular space 11 through the communication hole 13, and the inside of the exhaust pipe 10 is connected to the upper outlet 5 through the communication port 9 of the valve seat 16. A swirl chamber 14 is formed between the lower inner surface of the main body 1 and the inner surface of the bottom lid 6, and a liquid reservoir chamber 15 is formed below the swirl chamber 14, and the lower end of the liquid reservoir chamber 15 is connected to the drain port 8. A long cylindrical hollow filter 22 is disposed inside the swirl chamber 14 and the exhaust pipe 10. The filter 22 is closed by fixing the upper end to the valve seat 16 by welding and fixing the plug 23 to the lower end by welding. The filter 22 has a large number of fine through holes, captures foreign matters such as dust and scale from the fluid flowing down the inlet 4 and the annular space 11, and discharges the fluid to the outlet 5 side. The filtration particle size of the filter 22 is preferably about 0.5 to 10 microns. About half of the total length of the filter 22 is located in the exhaust pipe 10, and the other half is located in the swirl chamber 14.

プラグ23の外周壁と本体1及び底蓋4の内周壁との間に円筒状のフィルターの軸方向に沿って流下用衝突板24を配置する。本実施の形態では流下用衝突板24は放射状に複数枚例えば左右及び前後に4枚配置する。流下用衝突板24は上端をプラグ23の外周壁上部に溶接により固定する。流下用衝突板24は旋回室14の中央よりを旋回している微少な液体を衝突させて液溜室に流下させるものである。フィルター22の外周囲にフィルター22の軸方向に沿って分離用衝突板25を配置する。本実施の形態では分離用衝突板25は放射状に左右及び前後に4枚配置する。分離用衝突板25は上端を排気管10の下部内壁に当接させ、下端部をプラグ23に溶接により固定する。分離用衝突板25は環状空間11を流下してきた流体からゴミやスケール等の粒度の小さな異物を衝突により分離して液溜室15へ流下させるものである。分離用衝突板25は全長の約1割が排気管10内に位置し、残りの約9割が旋回室14内に位置する。 Between the outer peripheral wall of the plug 23 and the inner peripheral wall of the main body 1 and the bottom cover 4, a falling collision plate 24 is disposed along the axial direction of the cylindrical filter. In the present embodiment, a plurality of the collision plates 24 for the flow-down are arranged radially, for example, four on the left and right and front and rear. The falling plate 24 is fixed at the upper end to the upper part of the outer peripheral wall of the plug 23 by welding. The falling collision plate 24 collides a minute liquid swirling from the center of the swirl chamber 14 and flows down to the liquid reservoir chamber. A separation collision plate 25 is disposed around the outer periphery of the filter 22 along the axial direction of the filter 22. In this embodiment, four separation collision plates 25 are arranged radially on the left and right and front and rear. The separation collision plate 25 is brought into contact with the lower inner wall of the exhaust pipe 10 at the upper end and fixed to the plug 23 by welding. The separation impingement plate 25 separates foreign matters having a small particle size such as dust and scale from the fluid flowing down the annular space 11 by the collision and flows down to the liquid storage chamber 15. About 10% of the total length of the separation collision plate 25 is located in the exhaust pipe 10, and the remaining 90% is located in the swirl chamber 14.

上記の気液分離器の動作は次の通りである。入口6から入った液体やゴミやスケール等の異物を含む気体は旋回羽根12で旋回される。質量の大きな液体や粒度の大きな異物は遠心力の作用で外側に振り出されて分離され、本体1の内周壁に沿って流下し、液溜室15に流入して排液口8から系外に排出される。旋回流に含まれる粒度の小さな異物は、分離用衝突板25に衝突して分離され分離用衝突板25から流下用衝突板24に沿って旋回室14から液溜室15に流入し、排液口8から系外に排出される。旋回室14の中央よりを旋回している微少な液体は流下用衝突板24に衝突して流下用衝突板24に沿って旋回室14から液溜室15に流入し、排液口8から系外に排出される。 The operation of the gas-liquid separator is as follows. A gas containing foreign matter such as liquid, dust or scale entering from the inlet 6 is swirled by swirl vanes 12. A liquid having a large mass or a foreign substance having a large particle size is swung out and separated by the action of centrifugal force, flows down along the inner peripheral wall of the main body 1, flows into the liquid storage chamber 15, and flows out of the system from the drain port 8 To be discharged. The small foreign matter contained in the swirling flow collides with the separation collision plate 25 and is separated and flows from the separation collision plate 25 along the falling collision plate 24 into the liquid storage chamber 15 from the swirling chamber 14 and drains. It is discharged out of the system through the mouth 8. The minute liquid swirling from the center of the swirl chamber 14 collides with the falling collision plate 24 and flows into the liquid reservoir chamber 15 from the swirling chamber 14 along the falling collision plate 24, and from the drain port 8. Discharged outside.

本発明は、気体中に混入している液体をケーシング内に旋回流を起こし遠心力によって分離すると共にケーシング内に流体をろ過するフィルターを配置したあらゆる種類の気液分離器に利用することができる。 INDUSTRIAL APPLICABILITY The present invention can be used for all types of gas-liquid separators in which a liquid that is mixed in gas is swirled in the casing and separated by centrifugal force and a filter for filtering the fluid is disposed in the casing. .

1 本体
2 出入口部材
3 クランプ継手
4 底蓋
5 プラグ孔
6 入口
7 出口
8 排液口
9 連通口
10 排気管
11 環状空間
12 旋回羽根
13 連通孔
14 旋回室
15 液溜室
16 弁座
22 フィルター
23 プラグ
24 流下用衝突板
25 分離用衝突板
DESCRIPTION OF SYMBOLS 1 Main body 2 Entrance / exit member 3 Clamp joint 4 Bottom cover 5 Plug hole 6 Inlet 7 Outlet 8 Drainage port 9 Communication port 10 Exhaust pipe 11 Annular space 12 Swirling blade 13 Communication hole 14 Swivel chamber 15 Reservoir chamber 16 Valve seat 22 Filter 23 Plug 24 Collision plate for flow down 25 Collision plate for separation

Claims (1)

ケーシングと排気管で形成する環状空間に旋回羽根を配置し、旋回羽根の上方を入口に連結し、排気管の内側の孔を通してその上方を出口に連結し、環状空間の下方に旋回室と該旋回室の下方に液溜室を形成して該液溜室の下部を排液口に連結し、排気管と液溜室の間に下端部をプラグにより閉止状態とした流体ろ過用の円筒状フィルターを配置したものにおいて、プラグの外周壁とケーシングの内周壁との間に円筒状のフィルターの軸方向に沿って流下用衝突板を配置すると共に、円筒状のフィルターの外周囲に円筒状のフィルターの軸方向に沿って分離用衝突板を配置したことを特徴とする気液分離器。 A swirl vane is arranged in an annular space formed by a casing and an exhaust pipe, the upper part of the swirl vane is connected to the inlet, the upper part is connected to the outlet through a hole inside the exhaust pipe, and the swirl chamber and the lower part are connected to the lower part of the annular space. A cylindrical shape for fluid filtration in which a liquid storage chamber is formed below the swirl chamber, the lower portion of the liquid storage chamber is connected to a drain outlet, and the lower end portion is closed by a plug between the exhaust pipe and the liquid storage chamber. In the filter arrangement, a falling collision plate is arranged along the axial direction of the cylindrical filter between the outer peripheral wall of the plug and the inner peripheral wall of the casing, and the cylindrical filter is arranged around the outer periphery of the cylindrical filter. A gas-liquid separator, characterized in that a collision plate for separation is arranged along the axial direction of the filter.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106076006A (en) * 2016-08-08 2016-11-09 天津市百利溢通电泵有限公司 A kind of multi-level gas separator
CN108579220A (en) * 2018-04-28 2018-09-28 上海齐耀动力技术有限公司 A kind of gas-liquid separation device peculiar to vessel

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61181514A (en) * 1984-11-23 1986-08-14 ドムニック ハンター リミテッド Apparatus for removing carrier liquid from gas stream
US4666473A (en) * 1984-11-22 1987-05-19 Rotorcomp Verdichter, Gmbh Separator for gases and liquids
JPS63160923U (en) * 1987-04-09 1988-10-20
JP2002119813A (en) * 2000-10-13 2002-04-23 Tlv Co Ltd Gas-liquid separator
JP2011143364A (en) * 2010-01-15 2011-07-28 Tlv Co Ltd Gas-liquid separator

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4666473A (en) * 1984-11-22 1987-05-19 Rotorcomp Verdichter, Gmbh Separator for gases and liquids
JPS61181514A (en) * 1984-11-23 1986-08-14 ドムニック ハンター リミテッド Apparatus for removing carrier liquid from gas stream
JPS63160923U (en) * 1987-04-09 1988-10-20
JP2002119813A (en) * 2000-10-13 2002-04-23 Tlv Co Ltd Gas-liquid separator
JP2011143364A (en) * 2010-01-15 2011-07-28 Tlv Co Ltd Gas-liquid separator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106076006A (en) * 2016-08-08 2016-11-09 天津市百利溢通电泵有限公司 A kind of multi-level gas separator
CN108579220A (en) * 2018-04-28 2018-09-28 上海齐耀动力技术有限公司 A kind of gas-liquid separation device peculiar to vessel

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