JP2009300011A - Waste heat recovery device of steam - Google Patents

Waste heat recovery device of steam Download PDF

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JP2009300011A
JP2009300011A JP2008155859A JP2008155859A JP2009300011A JP 2009300011 A JP2009300011 A JP 2009300011A JP 2008155859 A JP2008155859 A JP 2008155859A JP 2008155859 A JP2008155859 A JP 2008155859A JP 2009300011 A JP2009300011 A JP 2009300011A
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steam
ejector
tank
waste heat
screw compressor
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JP2008155859A
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JP5274900B2 (en
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Takayuki Morii
高之 森井
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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 waste heat recovery device of steam, quickly sucking steam even if the intake steam amount varies from a very small amount to a large amount. <P>SOLUTION: A condensed water supply pipe 2 is connected to a reevaporation tank 1. The top face of the reevaporation tank 1 is connected to a suction chamber 5 of a steam ejector 3. A drive steam pipe 7 is connected to the suction chamber 5. A screw compressor 4 is connected to the outlet side of the steam ejector 3. A steam supply pipe 8 is connected to the outlet side of the screw compressor 4. The rotational frequency of the screw compressor 4 is increased or decreased to quickly suck steam reevaporated in the reevaporation tank 1 in a very small amount up to a large amount. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、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蒸気の廃熱回収装置に関する。  TECHNICAL FIELD The present invention relates to a steam waste heat recovery apparatus that re-evaporates high-temperature condensate condensed with steam in a re-evaporation tank and reuses it as steam.

従来の、蒸気の廃熱回収装置は、再蒸発タンクに復水供給管を接続して、この再蒸発タンク内で復水の再蒸発した蒸気を吸入する蒸気エゼクタに連通管を介在して再蒸発タンクと接続し、この連通管に圧力制御弁を取り付けると共に、再蒸発タンクの所定下方に液体圧送部材を配置したもので、再蒸発タンク内の再蒸発蒸気を蒸気エゼクタで吸入して、所定の蒸気使用箇所へ供給することによって、蒸気の廃熱回収を図ることができるものである。  In the conventional steam waste heat recovery system, a condensate supply pipe is connected to a re-evaporation tank, and a steam ejector that sucks the re-evaporated steam of the condensate in the re-evaporation tank is connected via a communication pipe. Connected to the evaporating tank, a pressure control valve is attached to this communication pipe, and a liquid pumping member is arranged below the re-evaporating tank. The re-evaporated vapor in the re-evaporating tank is sucked with a steam ejector It is possible to recover the waste heat of the steam by supplying it to the place where the steam is used.

上記従来の、蒸気の廃熱回収装置では、吸入蒸気量が変動した場合に、例えば再蒸発タンクで多量の再蒸発蒸気が発生した場合に、1台の蒸気エゼクタでは吸入することができなくなる問題があった。
特開2004−278871号公報
In the above-mentioned conventional waste heat recovery apparatus for steam, when a large amount of re-evaporated steam is generated in a re-evaporation tank, for example, when a large amount of re-evaporated steam is generated, a single steam ejector cannot be inhaled. was there.
JP 2004-278871 A

解決しようとする課題は、吸入蒸気量が少量から多量まで変動しても、速やかに吸入することができる蒸気の廃熱回収装置を得ることである。   The problem to be solved is to obtain a waste heat recovery device for steam that can be quickly sucked even if the amount of sucked steam varies from a small amount to a large amount.

本発明は、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から再蒸発した蒸気を吸引する蒸気エゼクタを接続したものにおいて、蒸気エゼクタの出口側にスクリュー式コンプレッサを接続したものである。   In the present invention, a condensate supply pipe is connected to a re-evaporation tank, and a steam ejector for sucking vapor re-evaporated from the condensate in the re-evaporation tank is connected. Is connected.

本発明は、蒸気エゼクタの出口側にスクリュー式コンプレッサを接続したことによって、吸入蒸気量が多量に発生した場合はスクリュー式コンプレッサの回転数を上げて多量の蒸気を吸入し、一方、吸入蒸気量が少量の場合はスクリュー式コンプレッサの回転数を下げることにより、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。   According to the present invention, when a screw compressor is connected to the outlet side of the steam ejector, when a large amount of intake steam is generated, the screw compressor is increased in number of rotations to suck in a large amount of steam. In the case of a small amount, the re-evaporated vapor that fluctuates from a small amount to a large amount can be rapidly sucked by lowering the rotational speed of the screw compressor.

本発明は、スクリュー式コンプレッサを用いるものであるが、このスクリュー式コンプレッサとしては、回転数を変化させることで吸入容量を自在にコントロールできるものが好適である。   The present invention uses a screw compressor, and as the screw compressor, one that can freely control the suction capacity by changing the rotation speed is suitable.

図1において、再蒸発タンク1と復水供給管2と蒸気エゼクタ3、及び、スクリュー式コンプレッサ4とで蒸気の廃熱回収装置を構成する。   In FIG. 1, a re-evaporation tank 1, a condensate supply pipe 2, a steam ejector 3, and a screw compressor 4 constitute a waste heat recovery device for steam.

蒸気エゼクタ3は、吸引室5とディフューザ6で構成し、吸引室5の内部にノズルを内蔵して、駆動蒸気管7と接続する。駆動蒸気管7の上流側は図示しない高圧蒸気源と接続する。   The steam ejector 3 includes a suction chamber 5 and a diffuser 6. A nozzle is built in the suction chamber 5 and is connected to a driving steam pipe 7. The upstream side of the driving steam pipe 7 is connected to a high-pressure steam source (not shown).

蒸気エゼクタ3の出口側にスクリュー式コンプレッサ4を接続する。スクリュー式コンプレッサ4は、内部にスクリュー式のロータと、このロータを回転する回転部、及び、この回転数をコントロールする制御部とで構成する。スクリュー式コンプレッサ4の出口側に、このスクリュー式コンプレッサ4で所定の圧力まで昇圧された再蒸発蒸気を、図示しない蒸気使用箇所へ供給するための蒸気供給管8を接続する。   A screw type compressor 4 is connected to the outlet side of the steam ejector 3. The screw-type compressor 4 includes a screw-type rotor, a rotating unit that rotates the rotor, and a control unit that controls the number of rotations. Connected to the outlet side of the screw compressor 4 is a steam supply pipe 8 for supplying re-evaporated steam, which has been pressurized to a predetermined pressure by the screw compressor 4, to a steam use location (not shown).

蒸気エゼクタ3の吸引室5を再蒸発タンク1の上部と管路9で接続する。管路9には、再蒸発タンク1から吸引室5側への蒸気の流下のみを許容し、反対方向の流体の流下を阻止する逆止弁10を取り付ける。   The suction chamber 5 of the steam ejector 3 is connected to the upper part of the reevaporation tank 1 by a pipe 9. A check valve 10 that allows only the flow of steam from the reevaporation tank 1 to the suction chamber 5 side and prevents the flow of fluid in the opposite direction is attached to the conduit 9.

再蒸発タンク1の左側面に復水供給管2を接続する。復水供給管2の左側端部は、高温状態の復水源と接続することによって、再蒸発タンク1内へ高温状態の復水を供給する。再蒸発タンク1内で高温復水から再蒸発した蒸気が、蒸気エゼクタ3に吸引され、更に、スクリュー式コンプレッサ4で昇圧されて、蒸気供給管8から所定の蒸気使用箇所へ供給されるものである。 A condensate supply pipe 2 is connected to the left side surface of the reevaporation tank 1. The left end of the condensate supply pipe 2 is connected to a high temperature condensate source to supply high temperature condensate into the reevaporation tank 1. Steam re-evaporated from the high-temperature condensate in the re-evaporation tank 1 is sucked into the steam ejector 3, further pressurized by the screw compressor 4, and supplied from the steam supply pipe 8 to a predetermined steam use location. is there.

再蒸発タンク1の下面に連通管11を介在してエゼクタ式真空ポンプ12の水エゼクタ13と接続する。エゼクタ式真空ポンプ12は、水エゼクタ13と、冷却水タンク14と、循環ポンプ15及びこれらを連結する連結循環路16とで構成する。冷却水タンク14には、タンク14内へ冷却水を補給する冷却水補給管17を接続する。また、連結循環路16の一部を分岐して、余剰水を排出するための余剰水排出管18を接続する。 The bottom surface of the reevaporation tank 1 is connected to a water ejector 13 of an ejector type vacuum pump 12 through a communication pipe 11. The ejector type vacuum pump 12 includes a water ejector 13, a cooling water tank 14, a circulation pump 15, and a connection circuit 16 connecting them. A cooling water supply pipe 17 for supplying cooling water into the tank 14 is connected to the cooling water tank 14. Moreover, a part of the connection circuit 16 is branched, and the surplus water discharge pipe 18 for discharging surplus water is connected.

蒸気エゼクタ3は、駆動蒸気管7から供給される高圧蒸気によって吸引室5で所定の吸引力を発生するものであるが、再蒸発タンク1内での再蒸発蒸気の量が多い場合は、スクリュー式コンプレッサ4の回転数を高めて吸入容量を多くすることによって多量の再蒸発蒸気を吸入することができ、一方、再蒸発タンク1内での再蒸発蒸気の量が少ない場合は、スクリュー式コンプレッサ4の回転数を低くして吸入容量を少なくすることで対応することができる。 The steam ejector 3 generates a predetermined suction force in the suction chamber 5 by the high-pressure steam supplied from the drive steam pipe 7. If the amount of the re-evaporated steam in the re-evaporation tank 1 is large, A large amount of re-evaporated steam can be sucked by increasing the number of revolutions of the compressor 4 and increasing the suction capacity. On the other hand, when the amount of re-evaporated steam in the re-evaporator tank 1 is small, a screw compressor This can be dealt with by lowering the rotational speed of 4 to reduce the suction volume.

再蒸発タンク1の底部にたまった再蒸発しきれなかった復水は、エゼクタ式真空ポンプ12の水エゼクタ13に吸引され、冷却水タンク14へと至る。   Condensate that cannot be completely evaporated again at the bottom of the re-evaporation tank 1 is sucked into the water ejector 13 of the ejector vacuum pump 12 and reaches the cooling water tank 14.

本発明に係る蒸気の廃熱回収装置の実施例を示す構成図。BRIEF DESCRIPTION OF THE DRAWINGS The block diagram which shows the Example of the waste heat recovery apparatus of the steam which concerns on this invention.

符号の説明Explanation of symbols

1 再蒸発タンク
2 復水供給管
3 蒸気エゼクタ
4 スクリュー式コンプレッサ
7 駆動蒸気管
8 蒸気供給管
12 エゼクタ式真空ポンプ
13 水エゼクタ
14 冷却水タンク
15 循環ポンプ
16 連結循環路
DESCRIPTION OF SYMBOLS 1 Re-evaporation tank 2 Condensate supply pipe 3 Steam ejector 4 Screw type compressor 7 Drive steam pipe 8 Steam supply pipe 12 Ejector type vacuum pump 13 Water ejector 14 Cooling water tank 15 Circulation pump 16 Connection circuit

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から再蒸発した蒸気を吸引する蒸気エゼクタを接続したものにおいて、蒸気エゼクタの出口側にスクリュー式コンプレッサを接続したことを特徴とする蒸気の廃熱回収装置。
A condensate supply pipe is connected to the re-evaporation tank and a steam ejector that sucks re-evaporated steam from the condensate in the re-evaporation tank is connected, and a screw type compressor is connected to the outlet side of the steam ejector. A waste heat recovery device for steam.
JP2008155859A 2008-06-13 2008-06-13 Steam waste heat recovery system Active JP5274900B2 (en)

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JP5274900B2 JP5274900B2 (en) 2013-08-28

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018009728A (en) * 2016-07-13 2018-01-18 株式会社テイエルブイ Waste heat recovery device
JP2020128845A (en) * 2019-02-08 2020-08-27 株式会社テイエルブイ Drain recovery device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0565808A (en) * 1991-09-04 1993-03-19 Fuji Electric Co Ltd Steam turbine plant supplying heat
JP2004278871A (en) * 2003-03-14 2004-10-07 Tlv Co Ltd Condensate re-evaporation device
JP2007247973A (en) * 2006-03-16 2007-09-27 Tlv Co Ltd Condensate recovery device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0565808A (en) * 1991-09-04 1993-03-19 Fuji Electric Co Ltd Steam turbine plant supplying heat
JP2004278871A (en) * 2003-03-14 2004-10-07 Tlv Co Ltd Condensate re-evaporation device
JP2007247973A (en) * 2006-03-16 2007-09-27 Tlv Co Ltd Condensate recovery device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018009728A (en) * 2016-07-13 2018-01-18 株式会社テイエルブイ Waste heat recovery device
JP2020128845A (en) * 2019-02-08 2020-08-27 株式会社テイエルブイ Drain recovery device
JP7189792B2 (en) 2019-02-08 2022-12-14 株式会社テイエルブイ Drain recovery device

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