JP2010024902A - Liquid pressure feeder - Google Patents

Liquid pressure feeder Download PDF

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JP2010024902A
JP2010024902A JP2008185425A JP2008185425A JP2010024902A JP 2010024902 A JP2010024902 A JP 2010024902A JP 2008185425 A JP2008185425 A JP 2008185425A JP 2008185425 A JP2008185425 A JP 2008185425A JP 2010024902 A JP2010024902 A JP 2010024902A
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liquid
pipe
sealed container
port
air supply
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JP4908463B2 (en
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Hideaki Yumoto
秀昭 湯本
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TLV Co Ltd
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TLV Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a liquid pressure feeder preventing noise and vibration when a flush steam of condensed water flowing through a drain pipe is mixed with liquid flowing through a conveying pipe. <P>SOLUTION: An air inlet 6 and an air outlet 7 for working steam and an inlet 8 and an outlet 9 for force feed liquid are provided in the liquid pressure feeder 24. An inflow pipe 21 is connected to the inlet 8, the conveying pipe 25 is connected to the outlet 9, an air supply pipe 26 is connected to the air inlet 6, and an exhaust pipe 23 is connected to the air outlet 7. The drain pipe 27 is branched off from the air supply pipe 26 and connected to the conveying pipe 25. A steam trap 28 and a discharge side check valve 29 allowing only a flow of condensed water to the conveying pipe 25 are arranged on the drain pipe 27. A mixing chamber 30 of the flush steam of the condensed water flowing through the drain pipe 27 and the liquid flowing through the conveying pipe 25 is formed on a connection part of the drain pipe 27 and the conveying pipe 25, and a nozzle part 32 injecting the flush steam into the mixing chamber 30 and a suction opening 34 sucking in the liquid by the flush stem injected from the nozzle part 32 are provided on a trailing end of the drain pipe 27. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、温水や燃料等の液体を高圧の作動蒸気で圧送する液体圧送装置に関するものである。本発明の液体圧送装置は、各種蒸気使用装置で発生した復水をボイラーや廃熱利用箇所に送る装置として特に適するものである。   The present invention relates to a liquid pumping device that pumps liquid such as hot water or fuel with high-pressure working steam. The liquid pressure feeding device of the present invention is particularly suitable as a device for sending condensate generated in various steam using devices to a boiler or a waste heat utilization site.

従来の液体圧送装置としては、例えば特開平8−145290号公報に示されているものが用いられていた。これは、図2に示すように、本体1と蓋2で密閉容器を構成して、密閉容器内にフロート3とフロート弁4とスナップ機構部5を配置すると共に、蓋2に作動蒸気の給気口6と排気口7及び圧送液体の流入口8と圧送口9を設けたものであり、流入口8が密閉容器への液体の流れだけを許容する流入側逆止弁20を介して圧送液体発生源(図示せず)に連通する流入管21に接続され、圧送口9が液体圧送先への液体の流れだけを許容する圧送側逆止弁22を介して液体圧送先(図示せず)に連通する圧送管25に接続され、給気口6が高圧の作動蒸気源(図示せず)に連通する給気管26に接続され、排気口7が圧送液体発生源側(図示せず)に連通する排気管23に接続される。給気管26で発生した復水を排出する排水管27を給気管26から分岐させて圧送管25に接続する。排水管27に復水を排出するスチームトラップ28を配置すると共にスチームトラップ28の下流に圧送管25への復水の流れだけを許容する排出側逆止弁29を配置する。   As a conventional liquid pumping apparatus, for example, the one shown in Japanese Patent Laid-Open No. 8-145290 has been used. As shown in FIG. 2, the main body 1 and the lid 2 constitute a sealed container, and the float 3, the float valve 4 and the snap mechanism portion 5 are arranged in the sealed container, and the working steam is supplied to the lid 2. The inlet 6 and the outlet 7 and the inlet 8 and the outlet 9 of the pumping liquid are provided, and the inlet 8 is pumped via an inflow check valve 20 that allows only the liquid to flow into the sealed container. A liquid pumping destination (not shown) is connected to an inflow pipe 21 communicating with a liquid generating source (not shown), and the pumping port 9 allows only the flow of liquid to the liquid pumping destination through a pumping-side check valve 22. ) Is connected to a pressure feed pipe 25 communicating with the pressure supply pipe 26, the air supply port 6 is connected to a supply pipe 26 communicating with a high-pressure working steam source (not shown), and the exhaust port 7 is connected to the pressure feed liquid generation source side (not shown). Is connected to an exhaust pipe 23 communicating with. A drain pipe 27 for discharging the condensate generated in the air supply pipe 26 is branched from the air supply pipe 26 and connected to the pressure feed pipe 25. A steam trap 28 that discharges condensate is disposed in the drain pipe 27, and a discharge-side check valve 29 that allows only the flow of condensate to the pressure feed pipe 25 is disposed downstream of the steam trap 28.

フロート3は支点10を回転中心として上下に浮上降下して、ダブル弁機構のフロート弁4を上下に移動させて圧送口9を連通遮断すると共に、第1レバー11を支点12を中心として上下に変位させるものである。同じく支点12を中心として回転自在に第2レバー13を配置し、この第2レバー13の端部と第1レバー11の端部の間に圧縮状態のコイルバネ14を取り付ける。第2レバー13の上部に操作棒15を連結する。操作棒15の上部には、排気口7を開閉する球状の排気弁体16を取り付けると共に、操作棒15の中段部に操作レバー17を固着する。操作レバー17の上部に上下動自在に給気棒18を配置して、この給気棒18の更に上方に球状の給気弁体19を自由状態で配置する。   The float 3 floats up and down around the fulcrum 10 as the center of rotation, moves the float valve 4 of the double valve mechanism up and down to cut off the communication of the pressure feed port 9, and moves the first lever 11 up and down around the fulcrum 12. It is to be displaced. Similarly, a second lever 13 is disposed so as to be rotatable about the fulcrum 12, and a compressed coil spring 14 is attached between the end of the second lever 13 and the end of the first lever 11. The operation rod 15 is connected to the upper part of the second lever 13. A spherical exhaust valve body 16 that opens and closes the exhaust port 7 is attached to the upper portion of the operation rod 15, and an operation lever 17 is fixed to the middle portion of the operation rod 15. An air supply rod 18 is arranged above the operation lever 17 so as to be movable up and down, and a spherical air supply valve body 19 is arranged in a free state further above the air supply rod 18.

図2は、密閉容器内の液位が低くフロート3が底部に位置する状態を示している。フロート弁4は閉弁して密閉容器内と圧送口9を遮断し、給気弁体19が給気口6を閉口すると共に排気弁体16が排気口7を開口している。密閉容器内の作動蒸気が排気口7から排気管23を通して圧送液体発生源側に排気されると共に圧送液体発生源側の液体が流入管21から流入側逆止弁20を介して流入口8から密閉容器内に流入される。密閉容器内の液位上昇に伴ってフロート3が上昇してフロート弁4が開弁する。密閉容器内の液位が所定高位に達すると、スナップ機構部5がスナップ移動して給気弁体19が給気口6を開口すると共に排気弁体16が排気口7を閉口し、給気管26を通して給気口6から密閉容器内に供給される作動蒸気によって、密閉容器内の液体が圧送口9から圧送側逆止弁22を介して圧送管25を通して液体圧送先へ圧送される。液体の圧送に伴ってフロート3が降下し、密閉容器内の液位が所定低位に達すると、フロート弁4が閉弁し、スナップ機構部5が反対側にスナップ移動して給気弁体19が給気口6を閉口すると共に排気弁体16が排気口7を開口する。   FIG. 2 shows a state where the liquid level in the sealed container is low and the float 3 is located at the bottom. The float valve 4 is closed to shut off the inside of the sealed container and the pressure feed port 9, the air supply valve body 19 closes the air supply port 6, and the exhaust valve body 16 opens the exhaust port 7. The working vapor in the hermetic container is exhausted from the exhaust port 7 through the exhaust pipe 23 to the pumping liquid generation source side, and the liquid at the pumping liquid generation source side is discharged from the inlet pipe 21 through the inlet check valve 20 from the inlet 8. It flows into the sealed container. As the liquid level in the sealed container rises, the float 3 rises and the float valve 4 opens. When the liquid level in the sealed container reaches a predetermined high level, the snap mechanism portion 5 snaps and the air supply valve body 19 opens the air supply port 6 and the exhaust valve body 16 closes the exhaust port 7, and the air supply pipe The liquid in the sealed container is pumped from the pumping port 9 to the liquid pumping destination through the pumping side check valve 22 to the liquid pumping destination by the working vapor supplied from the air supply port 6 into the sealed container through 26. When the float 3 descends as the liquid is pumped and the liquid level in the sealed container reaches a predetermined low level, the float valve 4 closes, and the snap mechanism 5 snaps to the opposite side to supply the air supply valve body 19. Closes the air supply port 6 and the exhaust valve body 16 opens the exhaust port 7.

上記従来の液体圧送装置では、排水管27を流れる復水のフラッシュ蒸気が圧送管25を流れる液体と混合するときに騒音や振動を発生する問題点があった。
特開平8−145290
The conventional liquid pumping apparatus has a problem that noise and vibration are generated when the condensate flush vapor flowing through the drain pipe 27 is mixed with the liquid flowing through the pump pipe 25.
JP-A-8-145290

従って本発明の課題は、排水管を流れる復水のフラッシュ蒸気が圧送管を流れる液体と混合するときに騒音や振動を発生することのない液体圧送装置を提供することである。   Accordingly, an object of the present invention is to provide a liquid pumping device that does not generate noise or vibration when the condensate flush vapor flowing through the drain pipe is mixed with the liquid flowing through the pump pipe.

上記の課題を解決するために講じた本発明の技術的手段は、密閉容器に作動蒸気の給気口と排気口及び圧送液体の流入口と圧送口が設けられ、流入口が密閉容器への液体の流れだけを許容する流入側逆止弁を介して圧送液体発生源に連通する流入管に接続され、圧送口が液体圧送先への液体の流れだけを許容する圧送側逆止弁を介して液体圧送先に連通する圧送管に接続され、給気口が高圧の作動蒸気源に連通する給気管に接続され、排気口が圧送液体発生源側に連通する排気管に接続され、密閉容器内の液位が所定高位に達すると給気口が開口されると共に排気口が閉口されて密閉容器内に作動蒸気が供給されることにより、密閉容器内の液体が圧送口から液体圧送先へ圧送され、密閉容器内の液位が所定低位に達すると給気口が閉口されると共に排気口が開口されて密閉容器内の液位が所定高位に達するまで密閉容器内の作動蒸気が排気口から圧送液体発生源側に排気されると共に圧送液体発生源側の液体が流入口から密閉容器内に流入される液体圧送装置であって、給気管で発生した復水を排出する排水管を給気管から分岐させて圧送管に接続し、排水管に復水を排出するスチームトラップを配置すると共にスチームトラップの下流に圧送管への復水の流れだけを許容する排出側逆止弁を配置したものにおいて、排水管と圧送管の接続部に排水管を流れる復水のフラッシュ蒸気と圧送管を流れる液体との混合室を形成し、排水管の終端にフラッシュ蒸気を混合室に噴射させるノズル部と、ノズル部から噴射されるフラッシュ蒸気により液体を吸込む吸込口を設けたことを特徴とする液体圧送装置にある。   The technical means of the present invention devised to solve the above-described problems is that a closed container is provided with a supply port and an exhaust port for working steam and an inlet and a pumping port for pressurized liquid, and the inlet is connected to the sealed container. Via an inflow side check valve that allows only the flow of liquid, it is connected to an inflow pipe that communicates with the source of pressure liquid supply, and through a pressure side check valve that allows only the flow of liquid to the liquid pumping destination. Connected to a pumping pipe communicating with the liquid pumping destination, an air supply port connected to an air supply pipe communicating with a high-pressure working steam source, an exhaust port connected to an exhaust pipe communicating with the pumping liquid generating source side, and a sealed container When the liquid level in the inside reaches a predetermined high level, the air supply port is opened and the exhaust port is closed, and the working vapor is supplied into the sealed container, so that the liquid in the sealed container is transferred from the pressure feed port to the liquid pressure destination. When the liquid level in the sealed container reaches a predetermined low level, the air supply port is closed. At the same time, until the exhaust port is opened and the liquid level in the sealed container reaches a predetermined high level, the working vapor in the sealed container is exhausted from the exhaust port to the pressurized liquid generation source side, and the liquid on the pressurized liquid generation source side is discharged from the inflow port. A liquid pressure feeding device that flows into a sealed container, a drain pipe that discharges the condensate generated in the air supply pipe is branched from the air supply pipe, connected to the pressure feed pipe, and a steam trap that discharges the condensate to the drain pipe And a discharge check valve that allows only the condensate flow to the pressure feed pipe downstream of the steam trap, and the condensate flush steam that flows through the drain pipe at the connection between the drain pipe and the pressure feed pipe. A mixing chamber with the liquid flowing through the pressure feed pipe is formed, and a nozzle part for injecting flash vapor into the mixing chamber at the end of the drain pipe, and a suction port for sucking liquid with the flash vapor injected from the nozzle part are provided. A liquid pumping device for.

本発明の液体圧送装置は、排水管と圧送管とが接続される混合室でノズル部から噴射されるフラッシュ蒸気に液体が吸込口から吸込まれて速やかに均一に混合されるので騒音や振動を発生することがないという優れた効果を生じる。   The liquid pumping device according to the present invention is capable of generating noise and vibration because the liquid is sucked from the suction port into the flash vapor ejected from the nozzle portion in the mixing chamber to which the drain pipe and the pumping pipe are connected, and quickly and uniformly mixed. This produces an excellent effect that it does not occur.

本発明の液体圧送装置は、排水管と圧送管の接続部に排水管を流れる復水のフラッシュ蒸気と圧送管を流れる液体との混合室を形成し、排水管の終端にフラッシュ蒸気を混合室に噴射させるノズル部と、ノズル部から噴射されるフラッシュ蒸気により液体を吸込む吸込口を設けたものである。そのため、排水管と圧送管とが接続される混合室でノズル部から噴射されるフラッシュ蒸気に液体が吸込口から吸込まれて速やかに均一に混合される。そのため、排水管を流れる復水のフラッシュ蒸気が圧送管を流れる液体と混合するときに騒音や振動を発生することがない。   The liquid pumping device of the present invention forms a mixing chamber of the condensate flush vapor flowing through the drainage pipe and the liquid flowing through the pumping pipe at the connection between the drainage pipe and the pumping pipe, and the flash steam mixing chamber at the end of the drainage pipe And a suction port through which liquid is sucked by flash vapor ejected from the nozzle portion. Therefore, in the mixing chamber where the drain pipe and the pressure feed pipe are connected, the liquid is sucked from the suction port into the flash vapor sprayed from the nozzle portion, and quickly and uniformly mixed. Therefore, no noise or vibration is generated when the condensate flush steam flowing through the drain pipe is mixed with the liquid flowing through the pressure feed pipe.

図1を参照して本発明の実施例を説明する。本発明の液体圧送装置24は、内部構造が図2に示した従来例のものと同じであるので外観図で示し、同じ構成要素には同じ参照番号を付して説明する。液体圧送装置24は、本体1と蓋2で密閉容器を構成し、蓋2に作動蒸気の給気口6と排気口7及び圧送液体の流入口8と圧送口9を設ける。流入口8は密閉容器への液体の流れだけを許容する流入側逆止弁20を介して圧送液体発生源に連通する流入管21に接続する。圧送口9は液体圧送先への液体の流れだけを許容する圧送側逆止弁22を介して液体圧送先に連通する圧送管25に接続する。給気口6は高圧の作動蒸気源に連通する給気管26に接続する。排気口7は圧送液体発生源側に連通する排気管23に接続する。給気管26で発生した復水を排出する排水管27を給気管26から分岐させて圧送管25に接続する。排水管27に復水を排出するスチームトラップ28を配置すると共にスチームトラップ28の下流に圧送管25への復水の流れだけを許容する排出側逆止弁29を配置する。排水管27と圧送管25の接続部に排水管27を流れる復水のフラッシュ蒸気と圧送管25を流れる液体との混合室30をT継手31に形成し、排水管27の終端にフラッシュ蒸気を混合室30に噴射させるノズル部32を設けたノズル部材33をT継手31にねじ結合し、ノズル部32から噴射されるフラッシュ蒸気により液体を吸込む吸込口34を設けた吸込部材35をノズル部材33にねじ結合する。   An embodiment of the present invention will be described with reference to FIG. Since the liquid pumping device 24 of the present invention has the same internal structure as that of the conventional example shown in FIG. 2, it is shown in an external view, and the same constituent elements are denoted by the same reference numerals. The liquid pumping device 24 forms a sealed container with the main body 1 and the lid 2, and the lid 2 is provided with a supply port 6 and an exhaust port 7 for working steam, and an inlet 8 and a pumping port 9 for pumping liquid. The inflow port 8 is connected to an inflow pipe 21 that communicates with a pumped liquid generation source via an inflow side check valve 20 that allows only the flow of liquid to the sealed container. The pressure feed port 9 is connected to a pressure feed pipe 25 communicating with the liquid pressure feed destination via a pressure feed side check valve 22 that allows only the flow of liquid to the liquid pressure feed destination. The air supply port 6 is connected to an air supply pipe 26 communicating with a high-pressure working steam source. The exhaust port 7 is connected to an exhaust pipe 23 that communicates with the pumped liquid generation source side. A drain pipe 27 for discharging the condensate generated in the air supply pipe 26 is branched from the air supply pipe 26 and connected to the pressure feed pipe 25. A steam trap 28 that discharges condensate is disposed in the drain pipe 27, and a discharge-side check valve 29 that allows only the flow of condensate to the pressure feed pipe 25 is disposed downstream of the steam trap 28. A mixing chamber 30 of the condensate flush steam flowing through the drain pipe 27 and the liquid flowing through the pressure feed pipe 25 is formed in a T-joint 31 at the connection between the drain pipe 27 and the pressure feed pipe 25, and flush steam is supplied to the end of the drain pipe 27. A nozzle member 33 provided with a nozzle portion 32 to be injected into the mixing chamber 30 is screw-coupled to the T joint 31, and a suction member 35 provided with a suction port 34 for sucking liquid by flash vapor injected from the nozzle portion 32 is used as the nozzle member 33. Screw on to.

密閉容器内の液位が低い状態において、密閉容器内と圧送口9が遮断され、給気口6が閉口されると共に排気口7が開口されている。密閉容器内の作動蒸気が排気口7から排気管23を通して圧送液体発生源側に排気されると共に圧送液体発生源側で発生した復水が流入管21から流入側逆止弁20を介して流入口8から密閉容器内に流入される。密閉容器内の液位上昇に伴って密閉容器内と圧送口9が連通され、密閉容器内の液位が所定高位に達すると、給気口6が開口されると共に排気口7が閉口され、給気管26を通して給気口6から密閉容器内に供給される作動蒸気によって、密閉容器内の復水が圧送口9から圧送側逆止弁22を介して圧送管25から液体圧送先へ圧送される。液体の圧送に伴って密閉容器内の液位が低下し所定低位に達すると、密閉容器内と圧送口9が遮断され、給気口6が閉口されると共に排気口7が開口される。給気管26で発生した復水は排水管27を通して圧送管25に排出されるが、排水管27と圧送管25とが接続される混合室30でノズル部32から噴射されるフラッシュ蒸気に液体が吸込口34から吸込まれて速やかに均一に混合されるので、排水管27を流れる復水のフラッシュ蒸気が圧送管25を流れる液体と混合するときに騒音や振動を発生することがない。   In a state where the liquid level in the sealed container is low, the sealed container and the pressure feeding port 9 are shut off, the air supply port 6 is closed, and the exhaust port 7 is opened. The working steam in the hermetic container is exhausted from the exhaust port 7 through the exhaust pipe 23 to the pressurized liquid generation source side, and condensate generated on the pressurized liquid generation source side flows from the inflow pipe 21 through the inflow check valve 20. It flows into the sealed container from the inlet 8. As the liquid level in the sealed container rises, the inside of the sealed container and the pressure feed port 9 are communicated. When the liquid level in the sealed container reaches a predetermined high level, the air supply port 6 is opened and the exhaust port 7 is closed, The condensate in the sealed container is pumped from the pumping port 9 to the liquid pumping destination through the pumping-side check valve 22 by the working steam supplied from the air supply port 6 into the sealed container through the air supply pipe 26. The When the liquid level in the sealed container decreases and reaches a predetermined low level as the liquid is pumped, the inside of the sealed container and the pumping port 9 are shut off, the air supply port 6 is closed, and the exhaust port 7 is opened. Condensate generated in the air supply pipe 26 is discharged to the pressure feed pipe 25 through the drain pipe 27, but liquid is supplied to the flash vapor ejected from the nozzle portion 32 in the mixing chamber 30 to which the drain pipe 27 and the pressure feed pipe 25 are connected. Since it is sucked in from the suction port 34 and quickly and uniformly mixed, no noise or vibration is generated when the condensate flush vapor flowing in the drain pipe 27 is mixed with the liquid flowing in the pressure feed pipe 25.

本発明の液体圧送装置の構成図。The block diagram of the liquid pumping apparatus of this invention. 従来例を示す液体圧送装置の断面図。Sectional drawing of the liquid pumping apparatus which shows a prior art example.

符号の説明Explanation of symbols

1 本体
2 蓋
6 給気口
7 排気口
8 流入口
9 圧送口
20 流入側逆止弁
21 流入管
22 圧送側逆止弁
23 排気管
24 液体圧送装置
25 圧送管
26 給気管
27 排水管
28 スチームトラップ
29 排出側逆止弁
30 混合室
32 ノズル部
34 吸込口
DESCRIPTION OF SYMBOLS 1 Main body 2 Lid 6 Air supply port 7 Exhaust port 8 Inflow port 9 Pressure feed port 20 Inflow side check valve 21 Inflow pipe 22 Pressure feed side check valve 23 Exhaust pipe 24 Liquid pressure feeder 25 Pressure feed pipe 26 Supply pipe 27 Drain pipe 28 Steam Trap 29 Ejection check valve 30 Mixing chamber 32 Nozzle part 34 Suction port

Claims (1)

密閉容器に作動蒸気の給気口と排気口及び圧送液体の流入口と圧送口が設けられ、流入口が密閉容器への液体の流れだけを許容する流入側逆止弁を介して圧送液体発生源に連通する流入管に接続され、圧送口が液体圧送先への液体の流れだけを許容する圧送側逆止弁を介して液体圧送先に連通する圧送管に接続され、給気口が高圧の作動蒸気源に連通する給気管に接続され、排気口が圧送液体発生源側に連通する排気管に接続され、密閉容器内の液位が所定高位に達すると給気口が開口されると共に排気口が閉口されて密閉容器内に作動蒸気が供給されることにより、密閉容器内の液体が圧送口から液体圧送先へ圧送され、密閉容器内の液位が所定低位に達すると給気口が閉口されると共に排気口が開口されて密閉容器内の液位が所定高位に達するまで密閉容器内の作動蒸気が排気口から圧送液体発生源側に排気されると共に圧送液体発生源側の液体が流入口から密閉容器内に流入される液体圧送装置であって、給気管で発生した復水を排出する排水管を給気管から分岐させて圧送管に接続し、排水管に復水を排出するスチームトラップを配置すると共にスチームトラップの下流に圧送管への復水の流れだけを許容する排出側逆止弁を配置したものにおいて、排水管と圧送管の接続部に排水管を流れる復水のフラッシュ蒸気と圧送管を流れる液体との混合室を形成し、排水管の終端にフラッシュ蒸気を混合室に噴射させるノズル部と、ノズル部から噴射されるフラッシュ蒸気により液体を吸込む吸込口を設けたことを特徴とする液体圧送装置。
Pumped liquid is generated via an inflow check valve that allows only air to flow into the sealed container. Connected to the inflow pipe communicating with the source, the pumping port is connected to the pressure feeding pipe communicating with the liquid pumping destination through the pressure check valve that allows only the liquid flow to the liquid pumping destination, and the air supply port is high pressure The exhaust port is connected to an exhaust pipe that communicates with the working steam source, and the exhaust port is connected to an exhaust pipe that communicates with the pressurized liquid generation source side. When the liquid level in the sealed container reaches a predetermined high level, the intake port is opened. When the exhaust port is closed and working steam is supplied into the sealed container, the liquid in the sealed container is pumped from the pumping port to the liquid pumping destination, and when the liquid level in the sealed container reaches a predetermined low level, the air supply port Is closed and the exhaust port is opened so that the liquid level in the sealed container becomes a predetermined high level. Until the pressure is reached, the working vapor in the sealed container is exhausted from the exhaust port to the pressurized liquid generation source side, and the liquid on the pressurized liquid generation source side flows into the sealed container from the inlet, A drain pipe that discharges the generated condensate is branched from the air supply pipe and connected to the pressure feed pipe. A steam trap that discharges the condensate is placed in the drain pipe, and only the condensate flow to the pressure feed pipe is downstream of the steam trap. In the case where a discharge check valve is arranged to allow the discharge, a mixing chamber of the condensate flush vapor flowing through the drainage pipe and the liquid flowing through the pressure feed pipe is formed at the connection between the drainage pipe and the pressure feed pipe. A liquid pumping device comprising: a nozzle portion for injecting flash vapor into the mixing chamber; and a suction port for sucking liquid by the flash vapor ejected from the nozzle portion.
JP2008185425A 2008-07-16 2008-07-16 Liquid pumping device Active JP4908463B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018194184A (en) * 2017-05-12 2018-12-06 株式会社テイエルブイ Drain recovery system and pipe joint
CN111456973A (en) * 2020-04-23 2020-07-28 自然资源部天津海水淡化与综合利用研究所 Steam jet pump with nozzle heating function
CN115076151A (en) * 2021-03-12 2022-09-20 中核核电运行管理有限公司 Nuclear power steam-driven auxiliary water feeding pump and drainage recovery device of related system

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Publication number Priority date Publication date Assignee Title
JPH109200A (en) * 1996-06-21 1998-01-13 Toshio Awaji Fluid suction and/or fluid force-feed device
JPH10227407A (en) * 1997-02-14 1998-08-25 Tlv Co Ltd Liquid forced feeding device
JPH10227406A (en) * 1997-02-14 1998-08-25 Tlv Co Ltd Liquid forced feeding device
JP2004190822A (en) * 2002-12-13 2004-07-08 Tlv Co Ltd Liquid forced conveyance device
JP2005036737A (en) * 2003-07-15 2005-02-10 Tlv Co Ltd Liquid pumping device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH109200A (en) * 1996-06-21 1998-01-13 Toshio Awaji Fluid suction and/or fluid force-feed device
JPH10227407A (en) * 1997-02-14 1998-08-25 Tlv Co Ltd Liquid forced feeding device
JPH10227406A (en) * 1997-02-14 1998-08-25 Tlv Co Ltd Liquid forced feeding device
JP2004190822A (en) * 2002-12-13 2004-07-08 Tlv Co Ltd Liquid forced conveyance device
JP2005036737A (en) * 2003-07-15 2005-02-10 Tlv Co Ltd Liquid pumping device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018194184A (en) * 2017-05-12 2018-12-06 株式会社テイエルブイ Drain recovery system and pipe joint
CN111456973A (en) * 2020-04-23 2020-07-28 自然资源部天津海水淡化与综合利用研究所 Steam jet pump with nozzle heating function
CN115076151A (en) * 2021-03-12 2022-09-20 中核核电运行管理有限公司 Nuclear power steam-driven auxiliary water feeding pump and drainage recovery device of related system

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