JP2008150995A - Steam ejector - Google Patents

Steam ejector Download PDF

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Publication number
JP2008150995A
JP2008150995A JP2006338474A JP2006338474A JP2008150995A JP 2008150995 A JP2008150995 A JP 2008150995A JP 2006338474 A JP2006338474 A JP 2006338474A JP 2006338474 A JP2006338474 A JP 2006338474A JP 2008150995 A JP2008150995 A JP 2008150995A
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steam
pressure
reducing valve
pipe
pressure reducing
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JP2006338474A
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Naoki Matsukawa
直樹 松川
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TLV Co Ltd
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TLV Co Ltd
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Priority to JP2006338474A priority Critical patent/JP2008150995A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an easily installable and inexpensive steam ejector without requiring electricity and a high pressure air source. <P>SOLUTION: Suction chambers 17 and 18 of the steam ejectors 2 and 4 are connected to a steam pipe 8 via a pressure reducing valve 1. A re-evaporation tank 13 and the suction chambers 17 and 18 are connected by a suction passage 12. A three-way switching valve 26 is interposed between the suction passage 12 and the suction chamber 17. An outlet pipe 11 is connected to diffusers 19 and 20 of the ejectors 2 and 4. The right end of a pipe 5 is connected to the middle of the outlet pipe 11, and the other end is connected to a secondary side pressure detecting port 3 of the pressure reducing valve 1. Steam pressure detected in the pipe 5 is maintained under predetermined constant pressure by the pressure reducing valve 1 as a self-actuated pressure regulating valve, and since a driving source such as electricity and high pressure air is not required, the inexpensive and simple steam ejector can be provided. <P>COPYRIGHT: (C)2008,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に関する。   The present invention relates to a steam ejector that ejects drive steam from a nozzle at high speed and generates suction force in a suction chamber by velocity energy of the fluid.

蒸気エゼクタは、ノズルを内蔵した吸引室の入口側に圧力調節弁を接続し、ディフューザの出口側に圧力センサを取り付けて、この圧力センサの検出値に応じて圧力調節弁の弁開度を駆動制御することによって、吸引室で発生する吸引力を制御することができるものである。   The steam ejector is connected to a pressure control valve on the inlet side of a suction chamber with a built-in nozzle, and a pressure sensor is attached to the outlet side of the diffuser, and the valve opening of the pressure control valve is driven according to the detected value of this pressure sensor. By controlling, the suction force generated in the suction chamber can be controlled.

この蒸気エゼクタにおいては、圧力センサと圧力調節弁を電気的に接続する電気回線、及び、他力式圧力調節弁としての圧力調節弁を駆動するための電気や高圧空気源等を必要とするために、エゼクタ装置そのものが高価なものとなってしまうと共に、装置の設置にも多くの労力やコストを要する問題があった。
特開2003−269400号公報
This steam ejector requires an electric circuit that electrically connects the pressure sensor and the pressure control valve, and electricity and a high-pressure air source for driving the pressure control valve as the other force type pressure control valve. In addition, the ejector device itself becomes expensive, and there is a problem that much labor and cost are required for installation of the device.
JP 2003-269400 A

解決しようとする課題は、電気や高圧空気源等を必要とすることがなく、設置も簡単で安価な蒸気エゼクタを提供することである。   The problem to be solved is to provide a steam ejector that does not require electricity, a high-pressure air source, or the like, is easy to install, and is inexpensive.

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ものにおいて、ノズル部の入口側に減圧弁を接続して、当該減圧弁の二次側圧力検出口を、ディフューザ内の出口側部、又は、ディフューザの出口側部と接続し、吸込室を再蒸発タンクと接続すると共に、この蒸気エゼクタを少なくとも2台配置して、当該蒸気エゼクタの吸込室の入口側もしくはディフューザの出口側に流路の切換弁を取り付けて、当該切換弁の切換操作によって、少なくとも2台の蒸気エゼクタの接続位置を並列状態に、又は、直列状態に切り換えるものである。   The present invention comprises a nozzle part composed of pores for restricting fluid, a suction chamber formed around the nozzle part, and a diffuser communicating with the suction chamber and the nozzle part. Connect the pressure reducing valve, connect the secondary pressure detection port of the pressure reducing valve to the outlet side of the diffuser or the outlet side of the diffuser, connect the suction chamber to the reevaporation tank, and At least two ejectors are arranged, a switching valve for the flow path is attached to the inlet side of the suction chamber of the steam ejector or the outlet side of the diffuser, and the connection position of at least two steam ejectors by switching operation of the switching valve Are switched to a parallel state or a serial state.

本発明の蒸気エゼクタは、ノズル部の入口側に減圧弁を接続して、この減圧弁の二次側圧力検出口を、ディフューザ内の出口側部、又は、ディフューザの出口側部と接続したことにより、減圧弁は自力式圧力調整弁であって駆動源としての電気や高圧空気を必要としないと共に、圧力センサも不要となって、安価で簡便な蒸気エゼクタとすることができる。   In the steam ejector of the present invention, the pressure reducing valve is connected to the inlet side of the nozzle portion, and the secondary pressure detection port of the pressure reducing valve is connected to the outlet side portion in the diffuser or the outlet side portion of the diffuser. Therefore, the pressure reducing valve is a self-acting pressure regulating valve, which does not require electricity or high-pressure air as a driving source, does not require a pressure sensor, and can be an inexpensive and simple steam ejector.

また、本発明は、少なくとも2台の蒸気エゼクタと流路の切換弁を取り付けて、この切換弁を切換操作することによって、少なくとも2台の蒸気エゼクタの接続位置を、並列状態又は直列状態に切り換えることができ、吸入蒸気量が多量に発生した場合は蒸気エゼクタを並列状態に、一方、吸入蒸気量が少量の場合は蒸気エゼクタを直列状態にすることにより、少量から多量まで変動する再蒸発蒸気を速やかに吸入することができる。   Further, according to the present invention, at least two steam ejectors and a flow path switching valve are attached, and the switching positions of the switching valves are switched to switch the connection position of at least two steam ejectors to a parallel state or a serial state. Re-evaporated steam that varies from a small amount to a large amount can be achieved by placing the steam ejector in parallel when a large amount of intake steam is generated, and by connecting the steam ejector in series when the amount of intake steam is small. Can be inhaled quickly.

本発明は、自力式圧力調整弁としての減圧弁を用いるものであり、この減圧弁としては、感圧部材としてのダイヤフラムやベローズやピストン等の一面に二次側圧力検出口から減圧弁の二次圧を印加させ、感圧部材の他面にはコイルバネ等の所定弾性力を印加させて、コイルバネの所定弾性力よりも減圧弁の二次圧が低下すると、減圧弁の主弁が開弁して減圧弁の一次側の高圧蒸気を二次側へ流下させることによって、減圧弁の二次側の圧力を所定値に維持することができるものが好ましい。   The present invention uses a pressure reducing valve as a self-acting pressure regulating valve. As this pressure reducing valve, a pressure reducing member such as a diaphragm, a bellows, or a piston is provided on a surface of a secondary side pressure detecting port. When the secondary pressure is applied and a predetermined elastic force such as a coil spring is applied to the other surface of the pressure-sensitive member and the secondary pressure of the pressure reducing valve is lower than the predetermined elastic force of the coil spring, the main valve of the pressure reducing valve opens. Then, it is preferable that the pressure on the secondary side of the pressure reducing valve can be maintained at a predetermined value by causing the high pressure steam on the primary side of the pressure reducing valve to flow down to the secondary side.

図1において、減圧弁1と、2台の蒸気エゼクタ2,4と、2台の蒸気エゼクタ2,4の出口側部と減圧弁1の二次側圧力検出口3とを接続する管路5、及び、再蒸発タンク13とで蒸気エゼクタを構成する。   In FIG. 1, a pipe line 5 that connects the pressure reducing valve 1, the two steam ejectors 2, 4, the outlet side portions of the two steam ejectors 2, 4 and the secondary pressure detection port 3 of the pressure reducing valve 1. A vapor ejector is constituted by the re-evaporation tank 13.

減圧弁1は、自力式圧力調整弁としての減圧弁であり、二次側圧力検出口3に管路5から蒸気エゼクタ2,4の出口側の圧力が印加され、図示しないダイヤフラム等の感圧部材の一面にその圧力が印加されることにより、蒸気エゼクタ2,4の出口側圧力を所定値に維持することができるものである。   The pressure reducing valve 1 is a pressure reducing valve as a self-acting pressure adjusting valve, and the pressure on the outlet side of the steam ejectors 2 and 4 is applied to the secondary side pressure detecting port 3 from the pipe line 5, and a pressure sensing such as a diaphragm (not shown). By applying the pressure to one surface of the member, the outlet side pressure of the steam ejectors 2 and 4 can be maintained at a predetermined value.

減圧弁1の入口側には高圧蒸気源と連通している蒸気管8を接続すると共に、減圧弁1の下部には、気液分離器6と蒸気トラップ7を一体に設ける。気液分離器6で、蒸気管8から減圧弁1内へ流入してきた蒸気の中に混入している液体としての復水を、蒸気から分離して、更に、蒸気トラップ7で分離した復水だけを系外へ排出することができるものである。蒸気トラップ7の下部には、逆止弁9を介在した連通管10を接続する。   A steam pipe 8 communicating with a high-pressure steam source is connected to the inlet side of the pressure reducing valve 1, and a gas-liquid separator 6 and a steam trap 7 are integrally provided below the pressure reducing valve 1. In the gas-liquid separator 6, the condensate as a liquid mixed in the steam flowing into the pressure reducing valve 1 from the steam pipe 8 is separated from the steam, and further the condensate separated by the steam trap 7. Can be discharged outside the system. A communication pipe 10 with a check valve 9 interposed is connected to the lower part of the steam trap 7.

蒸気エゼクタ2,4は、それぞれ、ノズル部を内蔵した吸込室17,18と、ディフューザ19,20とで構成する。本実施例においては、蒸気エゼクタ2,4のディフューザ19,20から離れた位置に管路5の右端を接続した例を示したが、管路5の右端はディフューザ19,20から離れることなくディフューザ19,20内の出口側に接続することもできる。管路5の右端部は、出口管11から図示しない蒸気使用装置等へ供給されるプロセス蒸気圧力を検出できる位置に接続することが好ましい。吸込室17,18の下端には、吸込室17,18で吸引する流体の流入する吸込通路12を設ける。   The steam ejectors 2 and 4 are constituted by suction chambers 17 and 18 having a nozzle portion and diffusers 19 and 20, respectively. In the present embodiment, an example is shown in which the right end of the pipe line 5 is connected to a position away from the diffusers 19 and 20 of the steam ejectors 2 and 4, but the right end of the pipe line 5 does not leave the diffusers 19 and 20. It can also be connected to the outlet side in 19,20. The right end of the pipe 5 is preferably connected to a position where the process steam pressure supplied from the outlet pipe 11 to a not-shown steam using device or the like can be detected. At the lower ends of the suction chambers 17 and 18, a suction passage 12 into which the fluid sucked in the suction chambers 17 and 18 flows is provided.

吸込通路12の下端を再蒸発タンク13と接続する。吸込通路12と吸込室17の間には三方切換弁26を介在する。蒸気エゼクタ4の出口側は、三方切換弁26と、分岐した二方切換弁27及び逆止弁28とそれぞれ連通する。 The lower end of the suction passage 12 is connected to the reevaporation tank 13. A three-way switching valve 26 is interposed between the suction passage 12 and the suction chamber 17. The outlet side of the steam ejector 4 communicates with the three-way switching valve 26 and the branched two-way switching valve 27 and check valve 28.

蒸気エゼクタ2,4は、蒸気管8から供給される高圧蒸気によって吸込室17,18で所定の吸引力を発生するものであり、再蒸発タンク13内で復水から再蒸発した蒸気を、吸込通路12から吸引することができるものである。 The steam ejectors 2 and 4 generate a predetermined suction force in the suction chambers 17 and 18 by the high-pressure steam supplied from the steam pipe 8, and suck the steam re-evaporated from the condensate in the re-evaporation tank 13. It is possible to suck from the passage 12.

再蒸発タンク13は縦長円筒状で、左側面中央部に高温復水流入管14を接続すると共に、右側面下部に復水排出管15を接続する。復水排出管15には蒸気トラップ16を介在する。また、減圧弁1の蒸気トラップ7の下部に取り付けた連通管10の下端は、再蒸発タンク13の上部と接続する。  The re-evaporation tank 13 has a vertically long cylindrical shape, and a high-temperature condensate inflow pipe 14 is connected to the central portion on the left side and a condensate discharge pipe 15 is connected to the lower side of the right side. A steam trap 16 is interposed in the condensate discharge pipe 15. Further, the lower end of the communication pipe 10 attached to the lower part of the steam trap 7 of the pressure reducing valve 1 is connected to the upper part of the reevaporation tank 13.

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からエゼクタ2,4の吸込室17,18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、蒸気トラップ16を通って復水排出管15から系外へ排出される。   Inside the reevaporation 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 from the suction passage 12 into the suction chambers 17 and 18 of the ejectors 2 and 4. Condensate whose temperature has decreased to some extent after re-evaporation passes through the steam trap 16 and is discharged from the condensate discharge pipe 15 to the outside of the system.

蒸気管8から供給される高圧蒸気は、減圧弁1で所定圧力まで減圧されてエゼクタ2,4の吸込室17,18に内蔵されたノズル部へ供給され、このノズル部で駆動蒸気は絞られて高速流となることによって、吸引力を発生して吸込通路12から再蒸発蒸気を吸引する。吸引された再蒸発蒸気は駆動蒸気と混合されてディフューザ19,20を通って出口管11から蒸気使用装置等へ供給される。   The high-pressure steam supplied from the steam pipe 8 is decompressed to a predetermined pressure by the pressure reducing valve 1 and supplied to the nozzle part built in the suction chambers 17 and 18 of the ejectors 2 and 4, and the driving steam is throttled by this nozzle part. As a result of the high-speed flow, a suction force is generated and the re-evaporated vapor is sucked from the suction passage 12. The sucked re-evaporated steam is mixed with the driving steam and supplied to the steam using device or the like from the outlet pipe 11 through the diffusers 19 and 20.

蒸気エゼクタ2,4の吸込通路12から吸入する再蒸発蒸気量が多い場合は、二方切換弁27を開弁すると共に、三方切換弁26を操作して、吸込通路12と吸込室17を連通することによって、2つの蒸気エゼクタ2,4の接続位置が並列状態となり、双方の蒸気エゼクタ2,4で吸込通路12を介して多量の再蒸発蒸気を吸入することができる。   When the amount of re-evaporated steam sucked from the suction passage 12 of the steam ejectors 2 and 4 is large, the two-way switching valve 27 is opened and the three-way switching valve 26 is operated to connect the suction passage 12 and the suction chamber 17. By doing so, the connection positions of the two steam ejectors 2 and 4 are in a parallel state, and a large amount of re-evaporated steam can be sucked through the suction passage 12 by both of the steam ejectors 2 and 4.

吸込通路12から吸入する再蒸発蒸気量が少ない場合は、二方切換弁27を閉弁すると共に、三方切換弁26を操作して、蒸気エゼクタ4の出口側と蒸気エゼクタ2の吸込室17を連通することによって、2つの蒸気エゼクタ2,4の接続位置が直列状態となり、吸込通路12から蒸気エゼクタ4の吸込室18へ吸入された蒸気が、三方切換弁26を通って他方の蒸気エゼクタ2の吸込室17へ吸入され、出口管11の下流側へ排出される。 When the amount of re-evaporated steam sucked from the suction passage 12 is small, the two-way switching valve 27 is closed and the three-way switching valve 26 is operated to connect the outlet side of the steam ejector 4 and the suction chamber 17 of the steam ejector 2. By connecting, the connection positions of the two steam ejectors 2 and 4 are in series, and the steam sucked from the suction passage 12 into the suction chamber 18 of the steam ejector 4 passes through the three-way switching valve 26 and the other steam ejector 2. Are sucked into the suction chamber 17 and discharged to the downstream side of the outlet pipe 11.

出口管11を通過する蒸気圧力は、管路5を通って減圧弁1の二次側圧力検出口3へ伝達されることによって、減圧弁1のコイルバネ等で設定された設定圧力と等しい圧力値に維持される。   The vapor pressure passing through the outlet pipe 11 is transmitted to the secondary side pressure detection port 3 of the pressure reducing valve 1 through the pipe line 5, thereby being equal to the set pressure set by the coil spring or the like of the pressure reducing valve 1. Maintained.

減圧弁1の下部に気液分離器6と蒸気トラップ7を設けたことによって、蒸気エゼクタ2,4の吸込室17,18に内蔵されたノズル部へ供給される蒸気は、復水が混入していない乾き度の高い蒸気であり、エゼクタ2,4の吸込室17,18での吸引力を最高水準に維持することができる。   By providing the gas-liquid separator 6 and the steam trap 7 at the lower part of the pressure reducing valve 1, the condensate is mixed into the steam supplied to the nozzle portions built in the suction chambers 17 and 18 of the steam ejectors 2 and 4. It is a steam with high dryness, and the suction force in the suction chambers 17 and 18 of the ejectors 2 and 4 can be maintained at the highest level.

減圧弁1の下部の気液分離器6で分離された高温復水は、蒸気トラップ7から再蒸発タンク13へ流下して再蒸発し、エゼクタ2,4の吸込室17,18に吸引されることによって、その保有する熱エネルギーを有効に回収することができる。   The high-temperature condensate separated by the gas-liquid separator 6 below the pressure reducing valve 1 flows down from the steam trap 7 to the re-evaporation tank 13 and re-evaporates, and is sucked into the suction chambers 17 and 18 of the ejectors 2 and 4. As a result, the stored thermal energy can be effectively recovered.

本発明の蒸気エゼクタの実施例を示す構成図。The block diagram which shows the Example of the steam ejector of this invention.

符号の説明Explanation of symbols

1 減圧弁
2 蒸気エゼクタ
3 二次側圧力検出口
4 蒸気エゼクタ
5 管路
6 気液分離器
7 蒸気トラップ
8 蒸気管
11 出口管
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
16 蒸気トラップ
17,18 吸込室
19,20 ディフューザ
26 三方切換弁
27 二方切換弁
DESCRIPTION OF SYMBOLS 1 Pressure reducing valve 2 Steam ejector 3 Secondary side pressure detection port 4 Steam ejector 5 Pipe line 6 Gas-liquid separator 7 Steam trap 8 Steam pipe 11 Outlet pipe 12 Suction passage 13 Re-evaporation tank 14 High temperature condensate inflow pipe 15 Condensate discharge pipe 16 Steam traps 17 and 18 Suction chambers 19 and 20 Diffuser 26 Three-way switching valve 27 Two-way switching valve

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ものにおいて、ノズル部の入口側に減圧弁を接続して、当該減圧弁の二次側圧力検出口を、ディフューザ内の出口側部、又は、ディフューザの出口側部と接続し、吸込室を再蒸発タンクと接続すると共に、この蒸気エゼクタを少なくとも2台配置して、当該蒸気エゼクタの吸込室の入口側もしくはディフューザの出口側に流路の切換弁を取り付けて、当該切換弁の切換操作によって、少なくとも2台の蒸気エゼクタの接続位置を並列状態に、又は、直列状態に切り換えることを特徴とする蒸気エゼクタ。
A pressure reducing valve is connected to the inlet side of the nozzle part in a nozzle part composed of a fine hole for restricting fluid, a suction chamber formed around the nozzle part, and a diffuser communicating with the suction chamber and the nozzle part. Then, the secondary pressure detection port of the pressure reducing valve is connected to the outlet side part in the diffuser or the outlet side part of the diffuser, the suction chamber is connected to the re-evaporation tank, and the steam ejector is connected to at least 2 Place a stand and install a flow path switching valve on the inlet side of the suction chamber of the steam ejector or on the outlet side of the diffuser. Or the steam ejector characterized by switching to a serial state.
JP2006338474A 2006-12-15 2006-12-15 Steam ejector Pending JP2008150995A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010116901A (en) * 2008-11-14 2010-05-27 Tlv Co Ltd Vacuum pump device
CN101706038B (en) * 2009-11-30 2012-07-04 重庆智得热工工业有限公司 Steam jet waste steam recycling device and steam jet waste steam recycling system
CN104696938A (en) * 2013-12-06 2015-06-10 中国石油化工股份有限公司 Mechanical and thermal combined vapor compression system based on comprehensive utilization of wastewater
CN106247315A (en) * 2016-08-03 2016-12-21 东华工程科技股份有限公司 A kind of steam condensate recycling device

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