JP2876279B2 - Condensate recovery equipment - Google Patents

Condensate recovery equipment

Info

Publication number
JP2876279B2
JP2876279B2 JP30978893A JP30978893A JP2876279B2 JP 2876279 B2 JP2876279 B2 JP 2876279B2 JP 30978893 A JP30978893 A JP 30978893A JP 30978893 A JP30978893 A JP 30978893A JP 2876279 B2 JP2876279 B2 JP 2876279B2
Authority
JP
Japan
Prior art keywords
condensate
steam
pipe
pump means
pressure
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.)
Expired - Fee Related
Application number
JP30978893A
Other languages
Japanese (ja)
Other versions
JPH07139705A (en
Inventor
昌邦 大西
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 JP30978893A priority Critical patent/JP2876279B2/en
Publication of JPH07139705A publication Critical patent/JPH07139705A/en
Application granted granted Critical
Publication of JP2876279B2 publication Critical patent/JP2876279B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は蒸気使用装置で発生した
復水をボイラや廃熱利用装置に圧送する復水回収装置に
関する。蒸気使用装置で凝縮した復水はスチ―ムトラッ
プで排出されるが、この復水は通常高温であり多くの熱
エネルギを有しているために、従来からこの復水をボイ
ラや廃熱利用装置に回収することが行なわれてきた。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a condensate recovery device for feeding condensate generated in a steam-using device to a boiler or a waste heat utilizing device. The condensate condensed by the steam-using device is discharged by a steam trap. This condensate is usually high in temperature and has a lot of heat energy. Has been collected.

【0002】[0002]

【従来の技術】従来の復水回収装置は例えば特開昭50
−65205号公報に示されている。これは、復水受け
容器にレベルスイッチを取り付け、このレベルスイッチ
とエゼクタへの蒸気通路に配置した電気操作弁とを接続
することにより、復水受け容器に所定量の復水が溜ると
エゼクタが駆動して復水を回収先へ導くものである。
2. Description of the Related Art A conventional condensate recovery apparatus is disclosed in
-65205. This is done by attaching a level switch to the condensate receiving container and connecting this level switch to an electrically operated valve arranged in the vapor passage to the ejector, so that when a predetermined amount of condensate accumulates in the condensate receiving container, the ejector It is driven to guide the condensate to the recovery destination.

【0003】[0003]

【発明が解決しようとする課題】上記従来のものは、ス
チ―ムエゼクタを用いているが、蒸気使用装置で発生し
た復水を吸引することができず、蒸気使用装置に復水を
滞留してしまう問題があった。蒸気使用圧力が低くて大
気圧とほとんど差が無い場合や、蒸気使用装置と復水受
け容器の間に立下げ部を設けることができないような場
合には、蒸気使用装置で発生した復水が復水受け容器に
流下することができず滞留してしまうのである。
The above-mentioned conventional apparatus uses a steam ejector. However, the condensate generated in the steam-using device cannot be sucked, and the condensed water stays in the steam-using device. There was a problem. If the steam usage pressure is low and there is almost no difference from the atmospheric pressure, or if it is not possible to provide a falling section between the steam usage device and the condensate receiving container, the condensate generated by the steam usage device It cannot flow down to the condensate receiving container and stays there.

【0004】また上記従来のものは電気操作弁を用いて
いることにより、化学プラント等のような爆発性の雰囲
気の場所ではその使用が制限されてしまう問題があっ
た。
Further, since the above-mentioned conventional one uses an electric operation valve, there is a problem that its use is restricted in an explosive atmosphere such as a chemical plant.

【0005】従って本発明の技術的課題は、電気部を使
用することなく、蒸気使用装置で発生した復水を吸引す
ることができるようにすることである。
Therefore, a technical object of the present invention is to make it possible to suck in condensate generated in a steam-using device without using an electric part.

【0006】[0006]

【課題を解決するための手段】上記の技術的課題を解決
するために講じた本発明の技術的手段は、蒸気使用装置
で発生した復水をボイラ―等へ回収するものにおいて、
蒸気使用装置の復水出口側をスチ―ムエゼクタの吸込み
口と接続し、該スチ―ムエゼクタの出口側を流体圧送式
のポンプ手段と接続し、該ポンプ手段の出口側を復水回
収先と接続して、該ポンプ手段に高圧流体管を連通する
と共に上記スチ―ムエゼクタにスチ―ム管を連通したも
のである。
Means for Solving the Problems The technical means of the present invention taken to solve the above technical problem is to recover condensate generated in a steam-using device to a boiler or the like.
The condensing outlet side of the steam-using device is connected to the suction port of the steam ejector, the outlet side of the steam ejector is connected to pump means of a fluid pressure type, and the outlet side of the pump means is connected to the condensate recovery destination. A high-pressure fluid pipe is connected to the pump means, and a steam pipe is connected to the steam ejector.

【0007】[0007]

【作用】上記の技術的手段の作用は下記の通りである。
スチ―ムエゼクタにスチ―ム管から蒸気が供給され、吸
込み口で吸引力を生じて蒸気使用装置で発生した復水を
吸引する。吸引された復水は出口側から流体圧送式のポ
ンプ手段に至る。ポンプ手段には高圧流体管が連通され
ており、ポンプ手段内部に溜った復水はこの高圧流体に
より復水回収先へ圧送される。
The operation of the above technical means is as follows.
Steam is supplied to the steam ejector from the steam pipe, and a suction force is generated at the suction port to suck the condensate generated by the steam-using device. The suctioned condensate flows from the outlet side to a fluid pressure type pump means. A high-pressure fluid pipe is connected to the pump means, and condensate collected inside the pump means is pressure-fed to the condensate recovery destination by the high-pressure fluid.

【0008】[0008]

【実施例】上記の技術的手段の具体例を示す実施例を説
明する(図1及び図2参照)。本実施例においては、流
体圧送式のポンプ手段へ供給する高圧流体に蒸気を用い
た例を説明する。蒸気使用装置20の復水排出管21と
スチ―ムトラップ22を介して接続するスチ―ムエゼク
タ1と、流体圧送式のポンプ手段2と、スチ―ムエゼク
タ1に蒸気を供給するスチ―ム管3と、同じくポンプ手
段2に蒸気を供給する高圧流体管5とで復水回収装置を
構成する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment showing a specific example of the above technical means will be described (see FIGS. 1 and 2). In the present embodiment, an example will be described in which steam is used as a high-pressure fluid supplied to a fluid pumping type pump means. A steam ejector 1 connected to a condensate discharge pipe 21 of a steam using device 20 via a steam trap 22, a pump means 2 of a fluid pressure feeding type, and a steam pipe 3 for supplying steam to the steam ejector 1. A high-pressure fluid pipe 5 for supplying steam to the pump means 2 also constitutes a condensate recovery device.

【0009】スチ―ムエゼクタ1は、吸込み口6の内部
に配置した図示しないノズルと、その出口側に連設した
ディフュ―ザ7とで構成する。吸込み口6を復水排出管
21と接続する。蒸気供給管23から分岐したスチ―ム
管3をノズルと接続して、蒸気を流下させることによ
り、吸込み口6部に吸引力を生じるものである。ディフ
ュ―ザ7は気水を分離するセパレ―タ8と接続する。セ
パレ―タ8の上部には分離された蒸気を図示しない別途
の低圧蒸気使用装置へ供給する低圧蒸気管9を設けると
共に、下部には分離された復水を溜置く復水タンク10
と接続する管11を設ける。復水タンク10は管12と
逆止弁13を介して流体圧送式のポンプ手段2と連通す
る。ポンプ手段2の出口は同じく管14と逆止弁15と
を介して図示しない復水回収先と接続する。
The steam ejector 1 comprises a nozzle (not shown) disposed inside the suction port 6 and a diffuser 7 connected to the outlet side. The suction port 6 is connected to the condensate discharge pipe 21. The steam pipe 3 branched from the steam supply pipe 23 is connected to a nozzle to cause the steam to flow down, thereby generating a suction force at the suction port 6. The diffuser 7 is connected to a separator 8 for separating air and water. A low-pressure steam pipe 9 for supplying the separated steam to a separate low-pressure steam-using device (not shown) is provided at the upper part of the separator 8 and a condensate tank 10 for storing the separated condensate at the lower part.
A tube 11 is provided for connection to The condensate tank 10 communicates with the pump means 2 of a fluid pressure type via a pipe 12 and a check valve 13. The outlet of the pump means 2 is connected to a condensate collection destination (not shown) via the pipe 14 and the check valve 15.

【0010】図2に流体圧送式のポンプ手段2を示す。
ポンプ手段2は、本体31に蓋体32をボルト(図示せ
ず)で取り付けて内部に復水溜り室33を形成する。本
体31の上部に復水溜り室33に連通する復水の流入口
34を形成し、同じく下部には復水を回収先へ還元する
還元口35を形成する。流入口34と還元口35はそれ
ぞれ図1における管12と管14とを接続する。蓋体3
2に高圧流体管5と接続する導入口38と、この導入口
38の奥側に図示しない高圧流体循環口39を形成す
る。導入口38は吸気弁50を介して復水溜り室33に
連通し、循環口39は給気弁50の奥側にほぼ平行に配
置した図示しない排気弁51を介して復水溜り室33と
連通する。吸気弁50と排気弁51はスライド棒53と
結合していることにより、スライド棒53が上方へ変位
すると給気弁50が開弁して排気弁51が閉弁し、スラ
イド棒53が下方へ変位すると給気弁50が閉弁して排
気弁51が開弁する構成のものである。スライド棒53
の両側側方にはストイド棒53の上下動を支持するスラ
イドリング55を設ける。
FIG. 2 shows a pump means 2 of a fluid pressure type.
The pump means 2 has a lid 32 attached to the main body 31 with bolts (not shown) to form a condensate sump chamber 33 inside. An inflow port 34 for condensate water is formed in the upper part of the main body 31 to communicate with the condensate sump chamber 33, and a return port 35 for reducing the condensate water to a recovery destination is formed in the lower part. The inflow port 34 and the reduction port 35 connect the pipe 12 and the pipe 14 in FIG. 1, respectively. Lid 3
2, an inlet 38 connected to the high-pressure fluid pipe 5 and a high-pressure fluid circulation port 39 (not shown) are formed at the back of the inlet 38. The inlet 38 communicates with the condensate sump chamber 33 via an intake valve 50, and the circulation port 39 communicates with the condensate sump chamber 33 via an exhaust valve 51 (not shown) arranged substantially parallel to the back side of the air supply valve 50. Communicate. Since the intake valve 50 and the exhaust valve 51 are connected to the slide rod 53, when the slide rod 53 is displaced upward, the supply valve 50 is opened, the exhaust valve 51 is closed, and the slide rod 53 is moved downward. When displaced, the air supply valve 50 is closed and the exhaust valve 51 is opened. Slide bar 53
A slide ring 55 for supporting the up-and-down movement of the stoid bar 53 is provided on both sides.

【0011】復水溜り室33内に水位と共に浮上降下す
る密閉のフロ―ト56を収容する。フロ―ト56にはレ
バ―57を取り付け、レバ―57に連結部材58と弁体
60の弁棒59をピン結合する。レバ―57はピン61
を中心にしてフロ―ト56の浮上降下と共に回転する。
レバ―57の端部にピン63を介して補助レバ―64を
連設する。補助レバ―64の他端部は蓋体32に取り付
けたピン65により回動自在に取り付ける。連結部材5
8の一端はピン62によりスライド棒53と結合し、他
端はピン66により補助レバ―64と結合する。連結部
材58の中央部には圧縮状態のコイルバネ67を配置す
る。
A closed float 56 which rises and falls with the water level is accommodated in the condensate sump chamber 33. A lever 57 is attached to the float 56, and the connecting member 58 and the valve stem 59 of the valve body 60 are pin-connected to the lever 57. Lever 57 is pin 61
, And rotates with the float 56 floating.
An auxiliary lever 64 is connected to the end of the lever 57 via a pin 63. The other end of the auxiliary lever 64 is rotatably attached by a pin 65 attached to the lid 32. Connecting member 5
One end of 8 is connected to the slide bar 53 by a pin 62, and the other end is connected to an auxiliary lever 64 by a pin 66. A coil spring 67 in a compressed state is arranged at the center of the connecting member 58.

【0012】復水溜り室33内に復水が流入するとフロ
―ト56が上昇し、レバ―57がピン61を中心に回転
する。この場合ピン66は下方向へ変位してコイルバネ
67は更に圧縮される。ピン66が更に下方へ変位して
ピン62の位置よりもわずかに下に位置するとコイルバ
ネ67の圧縮力がピン62に作用して、スライド棒53
を一気に上へ押し上げる。スライド棒53が上方に位置
すると給気弁50が開弁して高圧流体管5から高圧蒸気
が復水溜り室33内に流入すると共に、給気弁50の奥
側に平行に設けた排気弁51が閉弁して高圧蒸気の排出
を防ぐことにより、復水溜り室33内の復水は還元口3
5と管14を経て復水回収先へ圧送される。
When the condensate flows into the condensate chamber 33, the float 56 rises, and the lever 57 rotates about the pin 61. In this case, the pin 66 is displaced downward, and the coil spring 67 is further compressed. When the pin 66 is further displaced downward and is positioned slightly below the position of the pin 62, the compression force of the coil spring 67 acts on the pin 62, and the slide rod 53
At once. When the slide rod 53 is positioned above, the air supply valve 50 is opened, high-pressure steam flows from the high-pressure fluid pipe 5 into the condensate sump chamber 33, and an exhaust valve provided in parallel with the back side of the air supply valve 50. The condensate in the condensate sump chamber 33 is returned to the return port 3 by closing the valve
5 and the pipe 14 are fed to the condensate recovery destination.

【0013】復水が回収されて復水溜り室33内の水位
が低下すると図2に示すようにフロ―ト56が降下し、
給気弁50が閉弁すると共に排気弁51が開弁して復水
溜り室33内の高圧蒸気を外部へ排出する。復水溜り室
33内の蒸気圧力が低下すると流入口34と管12を介
して復水タンク10内の復水が、復水溜り室33内へ流
下してくる。この場合弁体60が上昇して通路を閉じて
いることにより、復水が還元口35から排出されること
はない。
When the condensate is collected and the water level in the condensate sump 33 drops, the float 56 descends as shown in FIG.
The supply valve 50 is closed and the exhaust valve 51 is opened to discharge the high-pressure steam in the condensate sump chamber 33 to the outside. When the steam pressure in the condensate storage chamber 33 decreases, the condensate in the condensate tank 10 flows down into the condensate storage chamber 33 through the inflow port 34 and the pipe 12. In this case, the condensate is not discharged from the return port 35 because the valve body 60 is raised to close the passage.

【0014】図1において、蒸気供給管23から蒸気使
用装置20へ供給された蒸気は、仕事を行なって凝縮し
て復水となる。一方、スチ―ム管3からスチ―ムエゼク
タ1へは蒸気が供給され吸込み口6に吸引力を発生して
いる。この吸引力によって復水は復水排出管21とスチ
―ムトラップ22を介してスチ―ムエゼクタ1に吸引さ
れる。スチ―ムエゼクタ1により蒸気と混合した復水は
セパレ―タ8へ至り、再度蒸気と復水が分離され、蒸気
は低圧蒸気管9から別途の低圧蒸気使用装置へ供給さ
れ、復水は復水タンク10内に至る。ポンプ手段2の復
水溜り室33内の水位が低くフロ―ト56が降下してい
る場合は、復水溜り室33内の圧力はほぼ大気圧となっ
ており、復水タンク10に溜った復水は管12と逆止弁
13を経てポンプ手段2へ流下する。そして、ポンプ手
段2内に所定量の復水が溜るとフロ―ト56が上昇して
復水を回収先へ圧送する。
In FIG. 1, the steam supplied from the steam supply pipe 23 to the steam use device 20 performs work and condenses to be condensed. On the other hand, steam is supplied from the steam pipe 3 to the steam ejector 1 to generate a suction force at the suction port 6. The condensate is sucked by the steam ejector 1 through the condensate discharge pipe 21 and the steam trap 22 by this suction force. The condensed water mixed with the steam by the steam ejector 1 reaches the separator 8 where the steam and the condensed water are separated again. It reaches the inside of the tank 10. When the water level in the condensate sump chamber 33 of the pump means 2 is low and the float 56 is descending, the pressure in the condensate sump chamber 33 is almost equal to the atmospheric pressure and has accumulated in the condensate tank 10. The condensate flows down to the pump means 2 via the pipe 12 and the check valve 13. When a predetermined amount of condensed water accumulates in the pump means 2, the float 56 rises and pumps the condensed water to a recovery destination.

【0015】[0015]

【発明の効果】上記のように本発明によれば、スチ―ム
エゼクタと流体圧送式のポンプ手段とを用いたことによ
り、電気部を使用することなく、蒸気使用装置で発生し
た復水を吸引することができる。
As described above, according to the present invention, the condensate generated in the steam-using device is sucked without using the electric part by using the steam ejector and the pumping device of the fluid pressure type. can do.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施例の復水回収装置の構成図であ
る。
FIG. 1 is a configuration diagram of a condensate recovery apparatus according to an embodiment of the present invention.

【図2】本発明の復水回収装置に用いた流体圧送式のポ
ンプ手段の断面図である。
FIG. 2 is a sectional view of a fluid pumping type pump means used in the condensate recovery apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1 スチ―ムエゼクタ 2 流体圧送式のポンプ手段 3 スチ―ム管 5 高圧流体管 6 吸込み口 7 ディフュ―ザ 10 復水タンク 20 蒸気使用装置 33 復水溜り室 50 吸気弁 51 排気弁 56 フロ―ト DESCRIPTION OF SYMBOLS 1 Steam ejector 2 Fluid pumping type pump means 3 Steam pipe 5 High-pressure fluid pipe 6 Suction port 7 Diffuser 10 Condensate tank 20 Steam use device 33 Condensate sump chamber 50 Intake valve 51 Exhaust valve 56 Float

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 蒸気使用装置で発生した復水をボイラ―
等へ回収するものにおいて、蒸気使用装置の復水出口側
をスチ―ムエゼクタの吸込み口と接続し、該スチ―ムエ
ゼクタの出口側を流体圧送式のポンプ手段と接続し、該
ポンプ手段の出口側を復水回収先と接続して、該ポンプ
手段に高圧流体管を連通すると共に上記スチ―ムエゼク
タにスチ―ム管を連通したことを特徴とする復水回収装
置。
1. Condensate generated in a steam-using device is boiled
And the like, in which the condensate outlet side of the steam-using device is connected to the suction port of the steam ejector, the outlet side of the steam ejector is connected to pump means of a fluid pressure type, and the outlet side of the pump means Is connected to a condensate collection destination, a high-pressure fluid pipe is connected to the pump means, and a steam pipe is connected to the steam ejector.
JP30978893A 1993-11-15 1993-11-15 Condensate recovery equipment Expired - Fee Related JP2876279B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30978893A JP2876279B2 (en) 1993-11-15 1993-11-15 Condensate recovery equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30978893A JP2876279B2 (en) 1993-11-15 1993-11-15 Condensate recovery equipment

Publications (2)

Publication Number Publication Date
JPH07139705A JPH07139705A (en) 1995-05-30
JP2876279B2 true JP2876279B2 (en) 1999-03-31

Family

ID=17997254

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30978893A Expired - Fee Related JP2876279B2 (en) 1993-11-15 1993-11-15 Condensate recovery equipment

Country Status (1)

Country Link
JP (1) JP2876279B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018109474A (en) * 2017-01-05 2018-07-12 株式会社テイエルブイ Drain recovery system

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4583610B2 (en) * 2000-01-14 2010-11-17 株式会社テイエルブイ Steam heating device
CN103727523B (en) * 2014-01-21 2015-04-15 山东鲁润热能科技有限公司 Closed type condensate water recovery device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018109474A (en) * 2017-01-05 2018-07-12 株式会社テイエルブイ Drain recovery system

Also Published As

Publication number Publication date
JPH07139705A (en) 1995-05-30

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