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JP2011224431A - Gas-liquid separator - Google Patents

Gas-liquid separator Download PDF

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Publication number
JP2011224431A
JP2011224431A JP2010094273A JP2010094273A JP2011224431A JP 2011224431 A JP2011224431 A JP 2011224431A JP 2010094273 A JP2010094273 A JP 2010094273A JP 2010094273 A JP2010094273 A JP 2010094273A JP 2011224431 A JP2011224431 A JP 2011224431A
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filter
exhaust pipe
liquid
upstream filter
upstream
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JP5384420B2 (en
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Toshiyuki Seki
利行 関
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TLV Co Ltd
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TLV Co Ltd
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  • Separating Particles In Gases By Inertia (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a gas-liquid separator preventing a filter from clogging relatively early.SOLUTION: A swirl vane 12 is arranged in an annular space 11 formed by a body 1 and an exhaust pipe 10. The space above the swirl vane 12 is connected to an inlet 6. The space above the exhaust pipe 10 is connected to an outlet 7 through an inside hole of the exhaust pipe 10. A liquid storage chamber 15 is formed below the annular space 11, and the lower end of the liquid storage chamber 15 is connected to a liquid discharge outlet 8. A filter 22 for filtrating fluid is arranged between the exhaust pipe 10 and the liquid storage chamber 15. An upstream filter 24 for filtrating the fluid is arranged between the exhaust pipe 10 and the liquid storage chamber 15 outside the filter 22. The filtrating particle size of the upstream filter 24 is formed greater than the filtrating particle size of the filter 22. An impinging plate 25 is arranged in the outer periphery of the upstream filter 24 in the axial direction of the upstream filter 24.

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、環状空間の下方に液溜室を形成して該液溜室の下端を排液口に連結し、排気管と液溜室の間に流体をろ過する円筒状のフィルター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 liquid is placed below the annular space. A reservoir chamber is formed, the lower end of the liquid reservoir chamber is connected to a drainage port, and a cylindrical filter for filtering a fluid is disposed between the exhaust pipe and the liquid reservoir chamber.

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、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, the filter for filtering the fluid is clogged relatively early due to the accumulation of foreign matter such as dust and scales, so the filter must be frequently disassembled and cleaned or replaced. There was a problem that had to be done.

したがって本発明が解決しようとする課題は、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 to provide a gas-liquid separator that can prevent the filter from being clogged relatively early.

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、環状空間の下方に液溜室を形成して該液溜室の下端を排液口に連結し、排気管と液溜室の間に流体をろ過する円筒状のフィルターを配置したものにおいて、排気管と液溜室の間に流体をろ過する円筒状の上流フィルターをフィルターの外側に配置し、上流フィルターのろ過粒度をフィルターのろ過粒度よりも大きく形成し、上流フィルターの外周囲に上流フィルターの軸方向に沿って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. A cylindrical shape that connects the upper side to the outlet, forms a liquid storage chamber below the annular space, connects the lower end of the liquid storage chamber to the drainage port, and filters the fluid between the exhaust pipe and the liquid storage chamber A cylindrical upstream filter that filters the fluid between the exhaust pipe and the liquid storage chamber is disposed outside the filter, and the upstream filter has a filtration particle size larger than that of the filter. The collision plate is arranged along the axial direction of the upstream filter around the outer periphery of the upstream filter.

本発明によれば、排気管と液溜室の間に流体をろ過する円筒状の上流フィルターをフィルターの外側に配置し、上流フィルターのろ過粒度をフィルターのろ過粒度よりも大きく形成し、上流フィルターの外周囲に上流フィルターの軸方向に沿って衝突板を配置したことにより、粒度の中程度の異物が衝突板に衝突して分離され衝突板に沿って液溜室に流下するので、また粒度の小さな異物が上流フィルターで捕捉されるので、粒度の微小な異物がフィルターで捕捉されることとなり、フィルターが比較的早期に詰まることを防止でき、フィルターを頻繁に洗浄したり交換したりする必要がないという効果を奏する。 According to the present invention, the cylindrical upstream filter for filtering the fluid between the exhaust pipe and the liquid storage chamber is disposed outside the filter, and the upstream filter has a filtration particle size larger than the filtration particle size of the filter. By arranging the collision plate along the axial direction of the upstream filter around the outer periphery of the filter, medium-sized foreign matter collides with the collision plate and is separated and flows down along the collision plate to the liquid reservoir. Since small foreign particles are trapped by the upstream filter, fine particles of small particle size are captured by the filter, preventing the filter from clogging relatively early, and the filter needs to be frequently washed and replaced. There is an effect that there is no.

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.

旋回室14と排気管10の内側のフィルター22の外側に長尺円筒状の中空上流フィルター24を配置する。上流フィルター24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に溶接により固定して閉止状態とする。上流フィルター24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フィルター22側へ排出するものである。上流フィルター24のろ過粒度は20マイクロから100マイクロ程度が好適である。上流フィルター24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。上流フィルター24の外周囲に上流フィルター24の軸方向に沿って衝突板25を配置する。本実施の形態では衝突板25は放射状に左右及び前後に4枚配置する。衝突板25は上端を排気管10の下端に当接させ、下端部をプラグ23に溶接により固定する。衝突板24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中程度の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。旋回室14と液溜室15の間に隔壁部材17を配置する。隔壁部材17は円板形状で外周に4個の突起18を有し、突起18の外端を底蓋6に溶接によりして固定する。突起18の間の隔壁部材17外周縁と底蓋6内周壁との間に液体通過用隙間19を形成する。 A long cylindrical hollow upstream filter 24 is disposed outside the swirl chamber 14 and the filter 22 inside the exhaust pipe 10. The upper end of the upstream filter 24 is brought into contact with the lower inner wall of the exhaust pipe 10 and the lower end thereof is fixed to the plug 23 by welding so as to be closed. The upstream filter 24 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 filter 22 side. The filtration particle size of the upstream filter 24 is preferably about 20 to 100 microns. About 10% of the total length of the upstream filter 24 is located in the exhaust pipe 10, and the remaining 90% is located in the swirl chamber 14. A collision plate 25 is disposed around the outer periphery of the upstream filter 24 along the axial direction of the upstream filter 24. In the present embodiment, four collision plates 25 are arranged radially on the left and right and front and rear. The collision plate 25 has its upper end in contact with the lower end of the exhaust pipe 10 and has its lower end fixed to the plug 23 by welding. The collision plate 24 separates medium-sized foreign matters such as dust and scale from the fluid flowing down the annular space 11 by collision and flows down to the liquid storage chamber 15. A partition member 17 is disposed between the swirl chamber 14 and the liquid reservoir chamber 15. The partition member 17 has a disk shape and has four protrusions 18 on the outer periphery, and the outer ends of the protrusions 18 are fixed to the bottom lid 6 by welding. A liquid passage gap 19 is formed between the outer peripheral edge of the partition wall member 17 between the protrusions 18 and the inner peripheral wall of the bottom cover 6.

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、突起18の間の液体通過用隙間19を通って液溜室15に流入し、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中程度の異物は、衝突板25に衝突して分離され衝突板25に沿って旋回室14を流下し、突起18の間の液体通過用隙間19を通って液溜室15に流入し、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、上流フィルター24を通過する際に捕捉されて分離される。上流フィルター24の内側へ通過した粒度の微小な異物は、フィルター22を通過する際に捕捉されて分離される。フィルター22の内側へ通過した気体は連通口9を通して出口5から流出する。 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 by the action of centrifugal force and separated, flows down along the inner peripheral wall of the main body 1, and accumulates through a liquid passage gap 19 between the protrusions 18. It flows into the chamber 15 and is discharged out of the system through the drainage port 8. Medium-sized foreign matter contained in the swirling flow collides with the collision plate 25 and is separated, flows down the swirl chamber 14 along the collision plate 25, and passes through the liquid passage gap 19 between the protrusions 18. It flows into the chamber 15 and is discharged out of the system through the drainage port 8. The small foreign matter contained in the swirling flow is captured and separated when passing through the upstream filter 24. Fine foreign matter having a particle size that has passed to the inside of the upstream filter 24 is captured and separated when passing through the filter 22. The gas that has passed to the inside of the filter 22 flows out from the outlet 5 through the communication port 9.

粒度の中程度の異物が衝突板25に衝突して分離され衝突板25に沿って液溜室15に流下するので、また粒度の小さな異物が上流フィルター24で捕捉されるので、粒度の微小な異物がフィルター22で捕捉されることとなる。そのため、フィルター22が比較的早期に詰まることを防止でき、フィルター22を頻繁に洗浄したり交換したりする必要がない。 Medium foreign particles having a particle size collide with the collision plate 25 and are separated and flow down along the collision plate 25 to the liquid storage chamber 15, and foreign particles with a small particle size are captured by the upstream filter 24. Foreign matter is captured by the filter 22. Therefore, it is possible to prevent the filter 22 from being clogged relatively early, and it is not necessary to frequently wash or replace the filter 22.

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
17 隔壁部材
18 突起
19 液体通過用隙間
22 フィルター
23 プラグ
24 上流フィルター
25 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 17 Partition member 18 Protrusion 19 Liquid passage gap 22 Filter 23 Plug 24 Upstream filter 25 Collision plate

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、環状空間の下方に液溜室を形成して該液溜室の下端を排液口に連結し、排気管と液溜室の間に流体をろ過する円筒状のフィルターを配置したものにおいて、排気管と液溜室の間に流体をろ過する円筒状の上流フィルターをフィルターの外側に配置し、上流フィルターのろ過粒度をフィルターのろ過粒度よりも大きく形成し、上流フィルターの外周囲に上流フィルターの軸方向に沿って衝突板を配置したことを特徴とする気液分離器。 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 liquid storage chamber is formed below the annular space. The lower end of the liquid reservoir chamber is connected to the drainage port, and a cylindrical filter that filters the fluid is disposed between the exhaust pipe and the liquid reservoir chamber. A cylindrical upstream filter is filtered outside the filter, the upstream filter has a larger filter particle size than the filter particle size, and a collision plate is placed around the upstream filter along the axial direction of the upstream filter. A gas-liquid separator characterized by that.
JP2010094273A 2010-04-15 2010-04-15 Gas-liquid separator Expired - Fee Related JP5384420B2 (en)

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JP5384420B2 JP5384420B2 (en) 2014-01-08

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102940998A (en) * 2012-11-23 2013-02-27 广州市怡文环境科技股份有限公司 Inner-tower and cellular type gas-water separator
CN109694819A (en) * 2019-01-11 2019-04-30 肇庆市新大力设备制造安装有限公司 A kind of fermentation tail gas recyclable device
CN116059754A (en) * 2023-03-07 2023-05-05 苏州宇薄新能源科技有限公司 Guide ring filter element and gas-liquid separator

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63160923U (en) * 1987-04-09 1988-10-20
JPH0725954U (en) * 1993-10-22 1995-05-16 甲南電機株式会社 Cyclone separator
JPH11262610A (en) * 1998-03-17 1999-09-28 Shuuetsu Technica:Kk Element for air filter
JPH11267434A (en) * 1998-03-26 1999-10-05 Ckd Corp Vacuum filter

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63160923U (en) * 1987-04-09 1988-10-20
JPH0725954U (en) * 1993-10-22 1995-05-16 甲南電機株式会社 Cyclone separator
JPH11262610A (en) * 1998-03-17 1999-09-28 Shuuetsu Technica:Kk Element for air filter
JPH11267434A (en) * 1998-03-26 1999-10-05 Ckd Corp Vacuum filter

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102940998A (en) * 2012-11-23 2013-02-27 广州市怡文环境科技股份有限公司 Inner-tower and cellular type gas-water separator
CN102940998B (en) * 2012-11-23 2015-01-07 广州市怡文环境科技股份有限公司 Inner-tower and cellular type gas-water separator
CN109694819A (en) * 2019-01-11 2019-04-30 肇庆市新大力设备制造安装有限公司 A kind of fermentation tail gas recyclable device
CN109694819B (en) * 2019-01-11 2023-09-26 肇庆市新大力设备制造安装有限公司 Fermentation tail gas recovery device
CN116059754A (en) * 2023-03-07 2023-05-05 苏州宇薄新能源科技有限公司 Guide ring filter element and gas-liquid separator
CN116059754B (en) * 2023-03-07 2023-11-07 苏州宇薄新能源科技有限公司 Guide ring filter element and gas-liquid separator

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