JP2004278870A - Condensate re-evaporation device - Google Patents

Condensate re-evaporation device Download PDF

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Publication number
JP2004278870A
JP2004278870A JP2003069054A JP2003069054A JP2004278870A JP 2004278870 A JP2004278870 A JP 2004278870A JP 2003069054 A JP2003069054 A JP 2003069054A JP 2003069054 A JP2003069054 A JP 2003069054A JP 2004278870 A JP2004278870 A JP 2004278870A
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JP
Japan
Prior art keywords
condensate
evaporation tank
ejector
evaporation
steam
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2003069054A
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Japanese (ja)
Inventor
Tetsuya Mita
哲也 見田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TLV Co Ltd
Original Assignee
TLV Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TLV Co Ltd filed Critical TLV Co Ltd
Priority to JP2003069054A priority Critical patent/JP2004278870A/en
Publication of JP2004278870A publication Critical patent/JP2004278870A/en
Pending legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a condensate re-evaporation device capable of reliably allowing condensate to flow to the downstream side from a re-evaporation tank irrespective of the inflow of condensate. <P>SOLUTION: The condensate re-evaporation device is constituted by connecting a condensate feed pipe 2 and a communication pipe 8 to an upper part of a re-evaporation tank 1. A pressure sensor 9 and a pressure control valve 4 are fitted to the communication pipe 8 so as to be connected to a suction chamber 12 of an ejector 3, and a steam feed pipe 11 is connected to the ejector 3. In the condensate re-evaporation device, a part of condensate fed from the condensate feed pipe 2 to the re-evaporation tank 1 is re-evaporated, and sucked by the ejector 3 through the communication pipe 8. In this case, the inside of the re-evaporation tank 1 is maintained at a predetermined pressure state by the pressure control valve 4. Condensate in the re-evaporation tank 1 can be discharged to the downstream side from a condensate outlet pipe 5 without any stagnation. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
この発明は、蒸気の凝縮した高温復水を、再蒸発タンク内で再蒸発させて蒸気として再度利用する復水の再蒸発装置に関する。
【0002】
【従来の技術】
【特許文献1】特開平9−196305号公報
これには、蒸気使用機器に蒸気を供給する蒸気供給管にエゼクタを介在し、蒸気使用機器の出口側にスチームトラップを介して再蒸発タンクを接続して、再蒸発タンクの上部をエゼクタと接続した復水回収装置が開示されている。
【0003】
【発明が解決しようとする課題】
上記従来の再蒸発タンクでは、スチームトラップから流入する復水の量が少ない場合に、再蒸発タンクの下流側へ復水が流下しなくなってしまう問題があった。これは、再蒸発タンクへ流入する復水量が少ないと、再蒸発する蒸気も少なくなり、エゼクタの吸引力によって再蒸発タンク内が減圧状態、更には、大気圧以下の負圧状態となってしまい、タンク下流側へ復水が自然流下できないためである。
【0004】
従って、本発明の課題は、流入する復水量に係わりなく再蒸発タンクから下流側へ復水が確実に流下できる復水の再蒸発装置を得ること。
【0005】
【課題を解決するための手段】
上記の課題を解決するために講じた本発明の手段は、再蒸発タンクに復水供給管を接続して、当該再蒸発タンク内で復水の再蒸発した蒸気を吸引するエゼクタを接続したものにおいて、再蒸発タンクとエゼクタの間に圧力制御弁を配置して、当該圧力制御弁によって再蒸発タンク内を所定の圧力状態に維持するものである。
【0006】
【発明の実施の形態】
再蒸発タンクとエゼクタの間に圧力制御弁を配置して、再蒸発タンク内を所定の圧力状態に維持することにより、再蒸発タンク内が減圧状態、あるいは、大気圧以下の負圧状態となることを防止して、再蒸発タンクから下流側へ確実に復水を流下させることができる。
【0007】
【実施例】
図1において、再蒸発タンク1と、再蒸発タンク1に復水を供給する復水供給管2と、エゼクタ3、及び、圧力制御弁4とで復水の再蒸発装置を構成する。
【0008】
再蒸発タンク1は円筒形密閉状で、側面上部に復水供給管2を接続すると共に、側面下部に復水出口管5を接続する。復水供給管2にはバルブ6を介在させて図示しない蒸気使用機器などの復水源と接続する。一方、復水出口管5にはスチームトラップ7を介在させる。スチームトラップ7は、再蒸発タンク1内の復水だけを外部へ排出し、蒸気は排出しないものである。
【0009】
再蒸発タンク1の上面に連結管8を接続して、圧力制御弁4とエゼクタ3を連通する。本実施例における圧力制御弁4は、圧力センサ9とコントローラ10を組み合わせたいわゆる自動圧力調節弁を用いた例を示す。圧力センサ9で連結管8内すなわち再蒸発タンク1内の圧力を検出して、コントローラ10で設定した設定圧力に成るように圧力制御弁4の弁開度を自動的に制御するものである。
【0010】
エゼクタ3には蒸気供給管11を接続すると共に、エゼクタ3の吸引室12に連結管8の端部を接続する。エゼクタ3は、蒸気供給管11から供給される高圧蒸気によって吸引室12で所定の吸引力を発生して、再蒸発タンク1内の再蒸発蒸気を吸引するものである。
【0011】
復水供給管2から再蒸発タンク1内へ供給される復水は、再蒸発タンク1内で再蒸発して連結管8からエゼクタ3へ吸引される。この場合、連結管8に取り付けた圧力制御弁4によって、再蒸発タンク1内の圧力は、供給される復水量に係わりなく所定の圧力状態、すなわち、大気圧以下の負圧状態などの減圧状態にならないように維持される。このように、再蒸発タンク1内が所定の圧力状態に維持されることによって、再蒸発タンク1内の復水は、復水出口管5とスチームトラップ7へと流下して外部へ確実に排出される。
【0012】
エゼクタ3に吸引された再蒸発タンク1内の再蒸発蒸気は、蒸気供給管11からの蒸気と混合されて、蒸気排出管13から図示しない別途の蒸気使用箇所へ配送される。
【0013】
【発明の効果】
上記のように本発明によれば、再蒸発タンクとエゼクタの間に圧力制御弁を取り付けて、再蒸発タンク内を所定の圧力状態に維持することにより、流入してくる復水量に係わりなく再蒸発タンクから下流側へ復水を確実に流下させることができる。
【図面の簡単な説明】
【図1】本発明に係る復水の再蒸発装置の実施例を示す構成図。
【符号の説明】
1 再蒸発タンク
2 復水供給管
3 エゼクタ
4 圧力制御弁
7 スチームトラップ
8 連結管
9 圧力センサ
10 コントローラ
11 蒸気供給管
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a condensate re-evaporation device for re-evaporating high-temperature condensate in which steam is condensed in a re-evaporation tank and reusing the condensed steam as steam.
[0002]
[Prior art]
[Patent Document 1] Japanese Patent Application Laid-Open No. 9-196305 In this, an ejector is interposed in a steam supply pipe for supplying steam to a steam-using device, and a re-evaporation tank is connected to the outlet side of the steam-using device via a steam trap. Then, a condensate recovery device in which the upper part of the re-evaporation tank is connected to an ejector is disclosed.
[0003]
[Problems to be solved by the invention]
In the conventional re-evaporation tank, when the amount of condensate flowing from the steam trap is small, there is a problem that the condensate does not flow down the downstream side of the re-evaporation tank. This is because if the amount of condensate flowing into the re-evaporation tank is small, the amount of re-evaporated steam will also be small, and the suction force of the ejector will cause the inside of the re-evaporation tank to be in a reduced pressure state and a negative pressure state below atmospheric pressure. This is because condensed water cannot flow naturally to the downstream side of the tank.
[0004]
Accordingly, an object of the present invention is to provide a condensate re-evaporation device that can surely condensate down from the re-evaporation tank to the downstream side regardless of the amount of condensate flowing in.
[0005]
[Means for Solving the Problems]
Means of the present invention taken to solve the above-mentioned problem is that a condensate supply pipe is connected to a re-evaporation tank, and an ejector for suctioning re-evaporated steam of the condensate in the re-evaporation tank is connected. , A pressure control valve is arranged between the re-evaporation tank and the ejector, and the pressure control valve maintains the inside of the re-evaporation tank at a predetermined pressure.
[0006]
BEST MODE FOR CARRYING OUT THE INVENTION
By disposing a pressure control valve between the re-evaporation tank and the ejector and maintaining the inside of the re-evaporation tank at a predetermined pressure state, the inside of the re-evaporation tank becomes a reduced pressure state or a negative pressure state below the atmospheric pressure. This can prevent the condensate from flowing down from the re-evaporation tank to the downstream side.
[0007]
【Example】
In FIG. 1, a re-evaporation tank 1, a condensate supply pipe 2 for supplying condensate to the re-evaporation tank 1, an ejector 3, and a pressure control valve 4 constitute a condensate re-evaporation apparatus.
[0008]
The re-evaporation tank 1 has a cylindrical shape and has a condensate supply pipe 2 connected to the upper side and a condensate outlet pipe 5 connected to the lower side. The condensate supply pipe 2 is connected to a condensate source such as a device using steam (not shown) via a valve 6. On the other hand, a steam trap 7 is interposed in the condensate outlet pipe 5. The steam trap 7 discharges only condensed water in the re-evaporation tank 1 to the outside, and does not discharge steam.
[0009]
The connection pipe 8 is connected to the upper surface of the re-evaporation tank 1 to communicate the pressure control valve 4 with the ejector 3. The pressure control valve 4 in the present embodiment shows an example using a so-called automatic pressure control valve in which a pressure sensor 9 and a controller 10 are combined. The pressure sensor 9 detects the pressure in the connection pipe 8, that is, the pressure in the re-evaporation tank 1, and automatically controls the opening degree of the pressure control valve 4 so as to reach the set pressure set by the controller 10.
[0010]
A steam supply pipe 11 is connected to the ejector 3, and an end of the connecting pipe 8 is connected to a suction chamber 12 of the ejector 3. The ejector 3 generates a predetermined suction force in the suction chamber 12 by the high-pressure steam supplied from the steam supply pipe 11 to suck the re-evaporated steam in the re-evaporation tank 1.
[0011]
Condensed water supplied from the condensate supply pipe 2 into the re-evaporation tank 1 is re-evaporated in the re-evaporation tank 1 and sucked from the connecting pipe 8 to the ejector 3. In this case, the pressure in the re-evaporation tank 1 is controlled by the pressure control valve 4 attached to the connecting pipe 8 to a predetermined pressure state, that is, a reduced pressure state such as a negative pressure state below the atmospheric pressure regardless of the supplied condensed water amount. Will be maintained. By maintaining the inside of the re-evaporation tank 1 at a predetermined pressure state, the condensate in the re-evaporation tank 1 flows down to the condensate outlet pipe 5 and the steam trap 7 and is reliably discharged to the outside. Is done.
[0012]
The re-evaporated steam in the re-evaporation tank 1 sucked by the ejector 3 is mixed with the steam from the steam supply pipe 11 and delivered from the steam discharge pipe 13 to a separate steam use location (not shown).
[0013]
【The invention's effect】
As described above, according to the present invention, by installing a pressure control valve between the re-evaporation tank and the ejector and maintaining the inside of the re-evaporation tank at a predetermined pressure state, regardless of the amount of inflowing condensate, Condensed water can flow down reliably from the evaporation tank to the downstream side.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of a condensate re-evaporation apparatus according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Re-evaporation tank 2 Condensate supply pipe 3 Ejector 4 Pressure control valve 7 Steam trap 8 Connecting pipe 9 Pressure sensor 10 Controller 11 Steam supply pipe

Claims (1)

再蒸発タンクに復水供給管を接続して、当該再蒸発タンク内で復水の再蒸発した蒸気を吸引するエゼクタを接続したものにおいて、再蒸発タンクとエゼクタの間に圧力制御弁を配置して、当該圧力制御弁によって再蒸発タンク内を所定の圧力状態に維持することを特徴とする復水の再蒸発装置。A condensate supply pipe is connected to the re-evaporation tank, and an ejector for suctioning the re-evaporated vapor in the re-evaporation tank is connected, and a pressure control valve is arranged between the re-evaporation tank and the ejector. And a pressure control valve for maintaining the inside of the re-evaporation tank at a predetermined pressure state.
JP2003069054A 2003-03-14 2003-03-14 Condensate re-evaporation device Pending JP2004278870A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003069054A JP2004278870A (en) 2003-03-14 2003-03-14 Condensate re-evaporation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003069054A JP2004278870A (en) 2003-03-14 2003-03-14 Condensate re-evaporation device

Publications (1)

Publication Number Publication Date
JP2004278870A true JP2004278870A (en) 2004-10-07

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JP2003069054A Pending JP2004278870A (en) 2003-03-14 2003-03-14 Condensate re-evaporation device

Country Status (1)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011069479A (en) * 2009-09-28 2011-04-07 Tlv Co Ltd Check valve and steam supply system using the same
JP2014089001A (en) * 2012-10-30 2014-05-15 Miura Co Ltd Steam recovery system
JP2015190726A (en) * 2014-03-28 2015-11-02 三浦工業株式会社 Flash steam generating device and boiler system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63213703A (en) * 1987-02-27 1988-09-06 株式会社 テイエルブイ Condensate recovery device
JPH04369302A (en) * 1991-06-14 1992-12-22 Tlv Co Ltd Vacuum steam generating device
JPH06331104A (en) * 1993-05-20 1994-11-29 Hitachi Ltd Steam drain discharging device
JPH09112808A (en) * 1995-10-13 1997-05-02 Tlv Co Ltd Condensation recovery device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63213703A (en) * 1987-02-27 1988-09-06 株式会社 テイエルブイ Condensate recovery device
JPH04369302A (en) * 1991-06-14 1992-12-22 Tlv Co Ltd Vacuum steam generating device
JPH06331104A (en) * 1993-05-20 1994-11-29 Hitachi Ltd Steam drain discharging device
JPH09112808A (en) * 1995-10-13 1997-05-02 Tlv Co Ltd Condensation recovery device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011069479A (en) * 2009-09-28 2011-04-07 Tlv Co Ltd Check valve and steam supply system using the same
JP2014089001A (en) * 2012-10-30 2014-05-15 Miura Co Ltd Steam recovery system
JP2015190726A (en) * 2014-03-28 2015-11-02 三浦工業株式会社 Flash steam generating device and boiler system

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