JP2010116899A - Ejector device - Google Patents

Ejector device Download PDF

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JP2010116899A
JP2010116899A JP2008292229A JP2008292229A JP2010116899A JP 2010116899 A JP2010116899 A JP 2010116899A JP 2008292229 A JP2008292229 A JP 2008292229A JP 2008292229 A JP2008292229 A JP 2008292229A JP 2010116899 A JP2010116899 A JP 2010116899A
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ejector
steam
suction chamber
evaporation tank
condensate
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JP2008292229A
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JP5295726B2 (en
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Tomoyuki Shiraishi
知行 白石
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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 an ejector device preventing suction of air into a steam ejector and heat transfer failure. <P>SOLUTION: A steam supply pipe 8 is connected to a suction chamber 2 of the steam ejector 1. The suction chamber 2 of the steam ejector 1 is connected to a re-evaporation tank 13. An air sump part 7 is formed on an upper part of the re-evaporation tank 13, and is connected to a suction chamber 16 of a water ejector 3. A gas discharge means 10 is interposed between the water ejector 3 and re-evaporation tank 13. Condensate collected in a bottom of the re-evaporation tank 13 is supplied to the water ejector 3 by a liquid pressure-feeding member 17, and suction force is generated in the suction chamber 16 of the water ejector 3, and the air collected in the air sump part 7 of the re-evaporation tank 13 is sucked through the gas discharge means 10. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、駆動蒸気をノズルから高速で噴出させて、その流体の速度エネルギにより吸込室に吸引力を発生する蒸気エゼクタを組み合わせたエゼクタ装置に関する。   The present invention relates to an ejector device in which drive steam is ejected from a nozzle at high speed and a steam ejector that generates suction force in a suction chamber by the velocity energy of the fluid is combined.

エゼクタ装置は、ノズルを内蔵した吸込室の入口側に蒸気管を接続し、ディフューザの出口側に出口管を接続するとともに、蒸気エゼクタの吸込室を再蒸発タンクの上部と接続することによって、再蒸発タンクで再蒸発した蒸気を有効に活用することができるものである。   In the ejector device, a steam pipe is connected to the inlet side of the suction chamber containing the nozzle, an outlet pipe is connected to the outlet side of the diffuser, and the suction chamber of the steam ejector is connected to the upper part of the re-evaporation tank. The steam re-evaporated in the evaporation tank can be used effectively.

このエゼクタ装置においては、再蒸発タンクに混入した空気が、蒸気エゼクタに再蒸発蒸気とともに吸引されて、出口管から別途の蒸気使用箇所へ供給されてしまい、この別途の蒸気使用箇所で伝熱不良を起こす問題があった。空気が蒸気の伝熱を阻害してしまうためである。
特開2007−332859
In this ejector device, the air mixed in the re-evaporation tank is sucked into the steam ejector together with the re-evaporated vapor and supplied from the outlet pipe to a separate steam use location. There was a problem that caused. This is because air hinders the heat transfer of steam.
JP2007-332859A

解決しようとする課題は、蒸気エゼクタに空気が吸引されることがなく、伝熱不良を発生することのないエゼクタ装置を提供することである。   The problem to be solved is to provide an ejector device in which air is not sucked into the steam ejector and heat transfer failure does not occur.

本発明は、流体を絞る細孔からなるノズル部と、当該ノズル部の周囲に形成した吸込室と、当該吸込室及び上記ノズル部と連通したディフューザとからなる蒸気エゼクタと、当該蒸気エゼクタの吸込室を再蒸発タンクと接続したものにおいて、再蒸発タンクの上部を水エゼクタの吸込室と、気体排出手段を介在して接続したものである。   The present invention relates to a nozzle part composed of pores for constricting fluid, a suction chamber formed around the nozzle part, a steam ejector comprising the suction chamber and the diffuser communicating with the nozzle part, and a suction of the steam ejector In the case where the chamber is connected to the reevaporation tank, the upper part of the reevaporation tank is connected to the suction chamber of the water ejector via the gas discharge means.

本発明のエゼクタ装置は、再蒸発タンクの上部を水エゼクタの吸込室と接続したことにより、再蒸発タンク内へ混入した空気は、この水エゼクタに吸引されるために、蒸気エゼクタに吸引されることがなく、したがって、蒸気使用箇所で伝熱不良を発生することのないエゼクタ装置とすることができる。   In the ejector device according to the present invention, since the upper part of the reevaporation tank is connected to the suction chamber of the water ejector, the air mixed into the reevaporation tank is sucked into the water ejector and is therefore sucked into the steam ejector. Therefore, it is possible to provide an ejector device that does not cause poor heat transfer at the location where steam is used.

本発明のエゼクタとしては従来から使用されているものを用いることができ、ノズルと、吸込口を設けた吸込室、及び、ディフューザ部とで構成されるエゼクタを用いることができ、駆動流体に蒸気を用いる蒸気エゼクタと、駆動流体に水を用いる水エゼクタを用いる。   As the ejector of the present invention, a conventionally used ejector can be used, and an ejector comprising a nozzle, a suction chamber provided with a suction port, and a diffuser part can be used, and the drive fluid is vaporized. A steam ejector that uses water and a water ejector that uses water as the driving fluid are used.

図1において、蒸気エゼクタ1と、ノズル部を内蔵した吸込室2と、ディフューザ4と、ディフューザ4の出口側部に接続した出口管5と、再蒸発タンク13、及び、水エゼクタ3とでエゼクタ装置を構成する。   In FIG. 1, an ejector includes a steam ejector 1, a suction chamber 2 containing a nozzle portion, a diffuser 4, an outlet pipe 5 connected to an outlet side portion of the diffuser 4, a re-evaporation tank 13, and a water ejector 3. Configure the device.

蒸気エゼクタ1の吸込室2の入口側に駆動用の蒸気供給管8を接続する。蒸気供給管8には、供給する蒸気圧力を制御するための圧力制御弁6を介在する。蒸気エゼクタ1は、ノズル部を内蔵した吸込室2とディフューザ4とで構成する。吸込室2の下端には、吸込室2で吸引する再蒸発蒸気の流入する吸込通路12を設けて、再蒸発タンク13の上部と接続する。   A driving steam supply pipe 8 is connected to the inlet side of the suction chamber 2 of the steam ejector 1. A pressure control valve 6 for controlling the supplied steam pressure is interposed in the steam supply pipe 8. The steam ejector 1 is composed of a suction chamber 2 and a diffuser 4 each having a nozzle portion. A suction passage 12 into which re-evaporated vapor sucked in the suction chamber 2 flows is provided at the lower end of the suction chamber 2 and is connected to the upper portion of the re-evaporation tank 13.

再蒸発タンク13は横長円筒状で、左側上部に高温復水流入管14を接続する。再蒸発タンク13の右側上部に空気溜部7を形成して、その空気溜部7の上端に空気吸込通路9の一端を接続する。空気吸込通路9の途中に、気体排出手段10を取り付ける。気体排出手段10は、従来より用いられている自動空気抜弁、あるいは、手動で開閉弁することによって気体を排除することのできる手動弁を取り付けることができる。この気体排出手段10は、通路9内を流下してきた流体中に混入している空気を、系外へ排出することができるものである。   The reevaporation tank 13 has a horizontally long cylindrical shape, and a high-temperature condensate inflow pipe 14 is connected to the upper left portion. An air reservoir 7 is formed on the upper right side of the reevaporation tank 13, and one end of the air suction passage 9 is connected to the upper end of the air reservoir 7. A gas discharge means 10 is attached in the middle of the air suction passage 9. The gas discharge means 10 can be equipped with an automatic air vent valve conventionally used, or a manual valve that can exclude gas by manually opening and closing the valve. This gas discharge means 10 can discharge the air mixed in the fluid flowing down in the passage 9 out of the system.

気体排出手段10の出口側を、水エゼクタ3の吸込室16と接続する。水エゼクタ3の吸込室16の入口側を、後述する液体圧送部材17の液体圧送管路18と接続する。また、再蒸発タンク13の下端中央部に復水排出管15を接続する。   The outlet side of the gas discharge means 10 is connected to the suction chamber 16 of the water ejector 3. The inlet side of the suction chamber 16 of the water ejector 3 is connected to a liquid pumping line 18 of the liquid pumping member 17 described later. In addition, a condensate discharge pipe 15 is connected to the center of the lower end of the reevaporation tank 13.

液体圧送部材17は、復水流入口19と復水流出口20、及び、高圧操作用蒸気導入口21と蒸気排出口22を有し、復水流入口19に逆止弁23を介して復水排出管15を接続する。逆止弁23は、復水排出管15から液体圧送部材17内への復水の流下を許容し、反対方向の流れは阻止するものである。   The liquid pumping member 17 has a condensate inlet 19 and a condensate outlet 20, a high-pressure operation steam inlet 21 and a steam outlet 22, and a condensate discharge pipe is connected to the condensate inlet 19 via a check valve 23. 15 is connected. The check valve 23 allows the condensate to flow from the condensate discharge pipe 15 into the liquid pumping member 17 and prevents the flow in the opposite direction.

同様に、復水流出口20に逆止弁24を介して液体圧送管路18を接続する。この逆止弁24は、液体圧送部材17内から液体圧送管路18への復水の流下を許容し、反対方向の流れは阻止する機能を有する。高圧操作用蒸気導入口21に蒸気供給管8を分岐した高圧蒸気管25を接続する。蒸気排出口22を再蒸発タンク13の左側面上部と連通する。 Similarly, the liquid pumping line 18 is connected to the condensate outlet 20 via a check valve 24. The check valve 24 has a function of allowing the condensate to flow from the liquid pumping member 17 to the liquid pumping pipeline 18 and blocking the flow in the opposite direction. A high-pressure steam pipe 25 branched from the steam supply pipe 8 is connected to the high-pressure operation steam inlet 21. The vapor discharge port 22 communicates with the upper left side surface of the reevaporation tank 13.

液体圧送部材17は、内部に配置した図示しないフロートが下方部に位置する場合に、高圧操作用蒸気導入口21を閉口し、一方、蒸気排出口22を開口して、再蒸発タンク13から復水を、復水排出管15と逆止弁23と復水流入口19を通して液体圧送部材17内に流下させる。 The liquid pumping member 17 closes the high-pressure operation steam inlet 21 and opens the steam outlet 22 when the float (not shown) disposed therein is located in the lower part, and then recovers from the re-evaporation tank 13. Water is caused to flow down into the liquid pumping member 17 through the condensate discharge pipe 15, the check valve 23, and the condensate inlet 19.

液体圧送部材17内に復水が溜まって図示しないフロートが所定上方部に位置すると、蒸気排出口22を閉口すると共に、高圧操作用蒸気導入口21を開口して、高圧蒸気管25から高圧圧送用蒸気を内部に流入させることにより、内部に溜まった復水を、復水流出口20と逆止弁24と液体圧送管路18を通して、水エゼクタ3へ圧送供給する。 When condensate accumulates in the liquid pumping member 17 and a float (not shown) is positioned at a predetermined upper portion, the steam discharge port 22 is closed and the high-pressure operation steam introducing port 21 is opened, so that high-pressure pumping from the high-pressure steam pipe 25 is performed. By causing the steam for use to flow into the interior, the condensate accumulated therein is fed to the water ejector 3 through the condensate outlet 20, the check valve 24 and the liquid pressure feed line 18.

復水が圧送されて液体圧送部材17内の液位が低下すると、再度、高圧操作用蒸気導入口21を閉口し、蒸気排出口22を開口することにより、再蒸発タンク13から復水を内部へ流下させる。このような作動サイクルを繰り返すことにより、液体圧送部材17は、再蒸発タンク13の復水を、水エゼクタ3へ断続的に供給することができる。   When the condensate is pumped and the liquid level in the liquid pumping member 17 is lowered, the high pressure operation steam inlet 21 is closed again, and the steam outlet 22 is opened, so that the condensate is discharged from the reevaporation tank 13 to the inside. Flow down. By repeating such an operation cycle, the liquid pumping member 17 can intermittently supply the condensate in the reevaporation tank 13 to the water ejector 3.

再蒸発タンク13の内部で、高温復水流入管14から流入してきた高温復水が再蒸発して再び蒸気となり、吸込通路12から蒸気エゼクタ1の吸込室2へ吸引される。再蒸発してある程度温度の低下した復水は、再蒸発タンク13の底部に溜まる。   Inside the re-evaporation tank 13, the high-temperature condensate flowing in from the high-temperature condensate inflow pipe 14 is re-evaporated and becomes steam again, and is sucked into the suction chamber 2 of the steam ejector 1 from the suction passage 12. Condensate whose temperature has decreased to some extent due to re-evaporation accumulates at the bottom of the re-evaporation tank 13.

再蒸発タンク13の底部に溜まった復水が、液体圧送部材17によって水エゼクタ3へ供給され、水エゼクタ3の吸込室16に吸引力を発生して、再蒸発タンク13の空気溜部7に溜まっていた空気を、気体排出手段10を介して吸引することにより、再蒸発タンク13内の空気が、蒸気エゼクタ1に吸引されることがない。  Condensate collected at the bottom of the re-evaporation tank 13 is supplied to the water ejector 3 by the liquid pumping member 17, generating a suction force in the suction chamber 16 of the water ejector 3, and entering the air reservoir 7 of the re-evaporation tank 13. By sucking the accumulated air through the gas discharge means 10, the air in the re-evaporation tank 13 is not sucked into the steam ejector 1.

本発明のエゼクタ装置の実施例を示す構成図。The block diagram which shows the Example of the ejector apparatus of this invention.

符号の説明Explanation of symbols

1 蒸気エゼクタ
2 吸込室
3 水エゼクタ
4 ディフューザ
5 出口管
7 空気溜部
8 蒸気供給管
10 気体排出手段
12 吸込通路
13 再蒸発タンク
14 高温復水流入管
15 復水排出管
17 液体圧送部材
18 液体圧送管路
DESCRIPTION OF SYMBOLS 1 Steam ejector 2 Suction chamber 3 Water ejector 4 Diffuser 5 Outlet pipe 7 Outlet pipe 8 Air supply part 10 Steam supply pipe 10 Gas discharge means 12 Suction passage 13 Re-evaporation tank 14 High temperature condensate inflow pipe 15 Condensate discharge pipe 17 Liquid pressure feed member 18 Liquid pressure feed Pipeline

Claims (1)

流体を絞る細孔からなるノズル部と、当該ノズル部の周囲に形成した吸込室と、当該吸込室及び上記ノズル部と連通したディフューザとからなる蒸気エゼクタと、当該蒸気エゼクタの吸込室を再蒸発タンクと接続したものにおいて、再蒸発タンクの上部を水エゼクタの吸込室と、気体排出手段を介在して接続したことを特徴とするエゼクタ装置。
Re-evaporating the nozzle part composed of a pore for narrowing the fluid, a suction chamber formed around the nozzle part, a steam ejector comprising the suction chamber and the diffuser communicating with the nozzle part, and the suction chamber of the steam ejector What is connected to a tank, The ejector apparatus characterized by connecting the upper part of the re-evaporation tank with the suction chamber of the water ejector via the gas discharge means.
JP2008292229A 2008-11-14 2008-11-14 Ejector device Active JP5295726B2 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102434501A (en) * 2011-11-08 2012-05-02 吴艳坤 Energy-saving three-fluid joint jet vacuum device
JP2012145006A (en) * 2011-01-11 2012-08-02 Sasakura Engineering Co Ltd Thermo compressor and seawater desalination system provided with the same

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6291705A (en) * 1985-10-15 1987-04-27 株式会社テイエルブイ Condensate recovery pump device
JPH09196305A (en) * 1996-01-12 1997-07-29 Tlv Co Ltd Condensation recovery device
JP2000170698A (en) * 1998-12-09 2000-06-20 Samson Co Ltd Ejector type vacuum generator capable of providing high vacuum
JP2000354541A (en) * 1999-06-15 2000-12-26 Tlv Co Ltd Steam heating device
JP2007332859A (en) * 2006-06-15 2007-12-27 Tlv Co Ltd Steam ejector

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6291705A (en) * 1985-10-15 1987-04-27 株式会社テイエルブイ Condensate recovery pump device
JPH09196305A (en) * 1996-01-12 1997-07-29 Tlv Co Ltd Condensation recovery device
JP2000170698A (en) * 1998-12-09 2000-06-20 Samson Co Ltd Ejector type vacuum generator capable of providing high vacuum
JP2000354541A (en) * 1999-06-15 2000-12-26 Tlv Co Ltd Steam heating device
JP2007332859A (en) * 2006-06-15 2007-12-27 Tlv Co Ltd Steam ejector

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012145006A (en) * 2011-01-11 2012-08-02 Sasakura Engineering Co Ltd Thermo compressor and seawater desalination system provided with the same
CN102434501A (en) * 2011-11-08 2012-05-02 吴艳坤 Energy-saving three-fluid joint jet vacuum device

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