JPH09112808A - Condensation recovery device - Google Patents
Condensation recovery deviceInfo
- Publication number
- JPH09112808A JPH09112808A JP29194795A JP29194795A JPH09112808A JP H09112808 A JPH09112808 A JP H09112808A JP 29194795 A JP29194795 A JP 29194795A JP 29194795 A JP29194795 A JP 29194795A JP H09112808 A JPH09112808 A JP H09112808A
- Authority
- JP
- Japan
- Prior art keywords
- water supply
- condensate
- temperature
- pump
- supply tank
- 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.)
- Granted
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 26
- 230000005494 condensation Effects 0.000 title abstract 2
- 238000009833 condensation Methods 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 61
- 239000000498 cooling water Substances 0.000 claims abstract description 8
- 238000002347 injection Methods 0.000 claims abstract description 6
- 239000007924 injection Substances 0.000 claims abstract description 6
- 239000012530 fluid Substances 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 7
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 230000005855 radiation Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000000740 bleeding effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、蒸気使用機器等で発生
した凝縮水としての復水をボイラ―等へ回収する復水回
収装置に関する。蒸気使用機器で発生する復水は一般に
スチ―ムトラップを介して排出される。排出される復水
は通常高圧蒸気の復水であり、まだ高温の熱エネルギ―
を有しており、この熱エネルギ―の有効利用を図るため
に復水の回収が行なわれている。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a condensate recovery system for recovering condensate as condensed water generated in steam-using equipment to a boiler or the like. Condensate generated in equipment using steam is generally discharged through a steam trap. The discharged condensate is usually high-pressure steam condensate, which is still hot thermal energy.
The condensate is collected in order to make effective use of this thermal energy.
【0002】[0002]
【従来の技術】従来の復水回収装置を図2により説明す
る。ボイラ―1で発生した高圧蒸気を蒸気使用機器2が
消費することにより凝縮水としての復水が発生し、その
復水はスチ―ムトラップ3を経てヘッダ―4に至る。ヘ
ッダ―4の上部を一次圧力調整弁13と管路14を介し
て給水タンク11と連通することにより、ヘッダ―4内
圧力が所定以上に上昇すると一次圧力調整弁13が開弁
してその圧力を抜くことで圧力勾配を形成して蒸気使用
機器2内に復水を滞留しないものである。ヘッダ―4は
エゼクタ5と接続されて循環路6を介して循環ポンプ7
と連通する。循環ポンプ7とエゼクタ5と循環路6とで
復水回収ポンプを構成する。循環路6が分岐して復水回
収管路8と接続され、更に一部が弁9を介してボイラ―
1と接続すると共に、弁10を介して給水タンク11と
も接続するものである。2. Description of the Related Art A conventional condensate recovery system will be described with reference to FIG. Condensate as condensed water is generated by the steam-using device 2 consuming the high-pressure steam generated in the boiler 1, and the condensed water reaches the header 4 through the steam trap 3. By communicating the upper part of the header 4 with the water supply tank 11 through the primary pressure regulating valve 13 and the pipe line 14, when the internal pressure of the header 4 rises above a predetermined level, the primary pressure regulating valve 13 opens and its pressure increases. Is removed to form a pressure gradient so that the condensate does not stay in the steam-using device 2. The header-4 is connected to the ejector 5 and the circulation pump 7 is connected through the circulation path 6.
Communicate with The circulation pump 7, the ejector 5, and the circulation path 6 constitute a condensate recovery pump. The circulation path 6 is branched to be connected to the condensate water recovery pipeline 8, and a part of the circulation path 6 is connected via a valve 9 to the boiler.
1 is connected to the water supply tank 11 through the valve 10.
【0003】循環ポンプ7により復水を循環させること
によってエゼクタ5に吸引力を発生させ、ヘッダ―4か
らの復水を吸引すると共に、吸引した復水をボイラ―1
あるいは給水タンク11へ回収し、給水タンク11内の
復水は更に給水ポンプ12でもってボイラ―1へ回収す
ることにより、熱エネルギ―の有効利用を図るものであ
る。By circulating the condensate with the circulation pump 7, a suction force is generated in the ejector 5 to suck the condensate from the header 4 and to suck the condensate into the boiler-1.
Alternatively, the water is collected in the water supply tank 11, and the condensate in the water supply tank 11 is further collected in the boiler 1 by the water supply pump 12 so that the heat energy is effectively used.
【0004】[0004]
【本発明が解決しようとする課題】上記従来のもので
は、多量の高温復水を回収した場合に、給水タンク11
内の液温が過度に上昇して、給水タンク11から大量の
復水が再蒸発蒸気として大気中へ蒸発してしまい熱エネ
ルギ―の損失を生じる問題、あるいは、流体温度が高く
て給水ポンプ12がキャビテ―ションを起こしてポンプ
が騒音を発生したり振動したりあるいは腐食損傷してし
まう問題があった。In the above-mentioned conventional apparatus, when a large amount of high-temperature condensate is collected, the water supply tank 11
The liquid temperature inside rises excessively and a large amount of condensate from the water supply tank 11 evaporates into the atmosphere as re-evaporated vapor, causing a loss of thermal energy, or the fluid temperature is high and the water supply pump 12 There was a problem that the cavitation caused the pump to generate noise, vibrate, or corrode.
【0005】給水タンク11は通常大気開放状態で設置
されるために、高温復水が溜ると大量の再蒸発蒸気が発
生するのである。また、給水ポンプ12は流体の温度が
通常80度C以上程度になると、ポンプ内で蒸気泡が発
生してキャビテ―ションを発生するのである。Since the water supply tank 11 is usually installed in a state of being open to the atmosphere, a large amount of re-evaporated steam is generated when high-temperature condensate is accumulated. Further, when the temperature of the fluid in the water supply pump 12 is usually about 80 ° C. or higher, vapor bubbles are generated in the pump to cause cavitation.
【0006】従って本発明の技術的課題は、高温復水を
多量に回収する場合においても、給水タンクからの再蒸
発蒸気の発生を少なくして熱エネルギ―の損失を押える
と共に、給水ポンプでキャビテ―ションを生じることの
ない復水回収装置を得ることである。Therefore, a technical problem of the present invention is that even when a large amount of high-temperature condensate is recovered, the generation of re-evaporated steam from the water supply tank is reduced to suppress the heat energy loss, and the water supply pump is used to cavitation. -To obtain a condensate recovery system that does not cause bleeding.
【0007】[0007]
【課題を解決する為の手段】本発明の復水回収装置の構
成は次の通りである。蒸気使用機器で発生した復水を復
水回収ポンプにより、ボイラ―あるいは給水タンク等の
復水回収先へ圧送するものにおいて、給水タンクに冷却
水を供給する冷却水供給管と、給水タンク内の液温を検
出する温度検出手段を設けて、当該給水タンク内の液温
を所定温度に維持すると共に、給水タンク内の流体を復
水回収ポンプの復水流入側に注入するタンク流体注入手
段を設けたものである。The constitution of the condensate recovery apparatus of the present invention is as follows. Condensate generated from steam-using equipment is pumped to a condensate recovery destination such as a boiler or a water supply tank by a condensate recovery pump, and a cooling water supply pipe for supplying cooling water to the water supply tank and the inside of the water supply tank A temperature detecting means for detecting the liquid temperature is provided to maintain the liquid temperature in the water supply tank at a predetermined temperature, and a tank fluid injecting means for injecting the fluid in the water supply tank to the condensate inflow side of the condensate recovery pump. It is provided.
【0008】[0008]
【作用】温度検出手段と冷却水供給管により給水タンク
内の流体温度を所定温度、例えば60度Cから70度C
程度に維持することにより、給水タンクからの復水の再
蒸発を押えると共に、給水ポンプでキャビテ―ションを
生じることもない。With the temperature detecting means and the cooling water supply pipe, the temperature of the fluid in the water supply tank is set to a predetermined temperature, for example, 60 to 70 degrees C
By maintaining the level to a certain extent, re-evaporation of the condensate from the water supply tank can be suppressed, and cavitation does not occur in the water supply pump.
【0009】所定温度の給水タンク内流体を復水回収ポ
ンプの復水流入側に注入することにより、蒸気使用機器
及びスチ―ムトラップと、復水回収ポンプの間に温度差
に応じた圧力勾配を形成することができ、蒸気使用機器
とスチ―ムトラップから排出された復水をこの圧力勾配
によって、スム―ズに滞留することなく復水回収ポンプ
に吸引することができる。By injecting the fluid in the water supply tank of a predetermined temperature into the condensate inflow side of the condensate recovery pump, a pressure gradient according to the temperature difference is generated between the steam-using device and the steam trap and the condensate recovery pump. This pressure gradient allows the condensate discharged from the steam-using device and the steam trap to be sucked into the condensate recovery pump without staying in the smoose.
【0010】[0010]
【実施例】図1により本発明の実施例を詳細に説明す
る。本実施例においては図2に示す従来技術と同一部材
には同一符号を付す。Embodiments of the present invention will be described in detail with reference to FIG. In this embodiment, the same members as those of the conventional technique shown in FIG.
【0011】蒸気使用機器2の出口側にスチ―ムトラッ
プ3を介してヘッダ―4を接続する。ヘッダ―4とエゼ
クタ5を接続し、エゼクタ5は循環路6を介して循環ポ
ンプ7と接続する。エゼクタ5と循環路6と循環ポンプ
7とで復水回収ポンプを構成する。循環路6を分岐して
復水回収管路8を接続し、弁9を介してボイラ―1と接
続すると共に、弁10を介して給水タンク11の上部に
接続する。給水タンク11は上部が大気へ開放されてい
るものである。給水タンク11とボイラ―1の間に給水
ポンプ12を配置する。給水ポンプ12はボイラ―1内
の水位が低水位まで低下した場合に駆動して給水タンク
11内の低温復水をボイラ―1へ供給するものである。A header 4 is connected to the outlet side of the steam-using device 2 via a steam trap 3. The header 4 and the ejector 5 are connected to each other, and the ejector 5 is connected to the circulation pump 7 via the circulation path 6. The ejector 5, the circulation path 6, and the circulation pump 7 constitute a condensate water recovery pump. The circulation line 6 is branched to connect the condensate water recovery pipe line 8 to the boiler 1 via the valve 9 and to the upper part of the water supply tank 11 via the valve 10. The upper portion of the water supply tank 11 is open to the atmosphere. A water supply pump 12 is arranged between the water supply tank 11 and the boiler 1. The water supply pump 12 is driven when the water level in the boiler 1 is lowered to a low water level, and supplies the low temperature condensate in the water supply tank 11 to the boiler 1.
【0012】給水タンク11の上部に自動調節弁15を
介して冷却水供給管16を連通する。給水タンク11の
下部にはタンク内の流体温度を検出する温度検出手段と
しての温度センサ―17を取り付ける。温度センサ―1
7と自動調節弁15はそれぞれ温度コントロ―ラ18と
接続して、給水タンク11内の液温を所定温度範囲に制
御する。A cooling water supply pipe 16 is connected to the upper portion of the water supply tank 11 via an automatic control valve 15. At the lower part of the water supply tank 11, a temperature sensor 17 as temperature detecting means for detecting the temperature of the fluid in the tank is attached. Temperature sensor-1
7 and the automatic control valve 15 are respectively connected to the temperature controller 18 to control the liquid temperature in the water supply tank 11 within a predetermined temperature range.
【0013】給水タンク11の下部から管路19と注入
ポンプ20と自動弁21を介してヘッダ―4の上部と接
続する。これらの管路19と注入ポンプ20と自動弁2
1とでタンク流体注入手段を構成する。本実施例におい
ては、給水タンク11内の流体をヘッダ―4の上部に注
入する例を示したが、ヘッダ―を用いることなく、スチ
―ムトラップ3からエゼクタ5の間の管路に注入した
り、あるいは、ヘッダ―4に替えて密閉タンクを配置し
てその中に注入することもできる。The lower part of the water supply tank 11 is connected to the upper part of the header 4 through the conduit 19, the injection pump 20 and the automatic valve 21. These lines 19, infusion pump 20, and automatic valve 2
1 and the tank fluid injection means. In this embodiment, an example in which the fluid in the water supply tank 11 is injected into the upper portion of the header-4 has been shown, but without using the header, it is possible to inject it into the conduit between the steam trap 3 and the ejector 5. Alternatively, instead of the header 4, a closed tank may be arranged and injected into it.
【0014】次に作用を説明する。蒸気使用機器2で発
生した復水はスチ―ムトラップ3を経てヘッダ―4に至
りエゼクタ5に吸引され、一部が循環ポンプ7により循
環路6を循環すると共に、一部の復水は復水回収管路8
と弁9を経てボイラ―1に供給され、再度蒸気となって
蒸気使用機器2へ供給される。Next, the operation will be described. Condensate generated in the steam-using device 2 reaches the header 4 via the steam trap 3 and is sucked by the ejector 5, and a part of the condensate is circulated in the circulation path 6 by the circulation pump 7, and part of the condensate is condensed. Collection line 8
Then, it is supplied to the boiler 1 through the valve 9 and becomes steam again to be supplied to the steam using device 2.
【0015】給水タンク11内の液温は温度センサ―1
7で検出され温度コントロ―ラ18と自動調節弁15に
より所定温度、例えば60度C、に維持される。従っ
て、給水タンク11上部から大量の再蒸発蒸気が放散す
ることがないと共に、給水ポンプ12がキャビテ―ショ
ンを起こすこともない。The liquid temperature in the water supply tank 11 is a temperature sensor-1.
The temperature is detected at 7, and the temperature is maintained at a predetermined temperature, for example, 60 ° C. by the temperature controller 18 and the automatic control valve 15. Therefore, a large amount of re-evaporated vapor is not emitted from the upper part of the water supply tank 11, and the water supply pump 12 does not cause cavitation.
【0016】給水タンク11の所定温度に制御された流
体は、管路19と注入ポンプ20と自動弁21からヘッ
ダ―4に供給され、ヘッダ―4内を所定温度まで降温さ
せる。ヘッダ―4内の温度が所定温度まで低くなること
により、蒸気使用機器2とヘッダ―4の間に温度勾配、
すなわち圧力勾配ができて、蒸気使用機器2内で生じた
復水は滞留することなくスチ―ムトラップ3を経てヘッ
ダ―4内に流下する。The fluid whose temperature is controlled to a predetermined temperature in the water supply tank 11 is supplied from the conduit 19, the injection pump 20 and the automatic valve 21 to the header-4 to lower the temperature inside the header-4 to a predetermined temperature. When the temperature inside the header-4 is lowered to a predetermined temperature, a temperature gradient between the steam using device 2 and the header-4,
That is, a pressure gradient is created, and the condensate generated in the steam using device 2 flows down into the header 4 through the steam trap 3 without staying.
【0017】[0017]
【発明の効果】本発明は次のような効果を奏する。給水
タンク内の流体温度を所定値に維持することにより、給
水タンクからの大量の再蒸発蒸気の放散を防止して熱エ
ネルギ―の損失を防ぐことができ、且つ、給水ポンプで
キャビテ―ションを生じることもない。The present invention has the following effects. By maintaining the fluid temperature in the water supply tank at a specified value, it is possible to prevent the large amount of re-evaporated vapor from escaping from the water supply tank and prevent the loss of heat energy. It never happens.
【0018】所定温度の給水タンクの流体をタンク流体
注入手段によって復水回収ポンプの復水流入側に注入す
ることにより、蒸気使用機器及びスチ―ムトラップと復
水回収ポンプの間に必要な圧力勾配をつくることがで
き、蒸気使用機器で発生した復水をスチ―ムトラップを
介してスム―ズに復水回収ポンプで吸引することがで
き、蒸気使用機器に復水を滞留することがない。By injecting the fluid of the water supply tank having a predetermined temperature into the condensate inflow side of the condensate recovery pump by the tank fluid injecting means, the pressure gradient required between the steam using device and the steam trap and the condensate recovery pump. The condensate generated in the steam-using device can be sucked into the steam smoothly through the steam trap by the condensate recovery pump, and the condensate does not stay in the steam-using device.
【図1】本発明の復水回収装置の実施例の構成図であ
る。FIG. 1 is a configuration diagram of an embodiment of a condensate recovery device of the present invention.
【図2】従来例の復水回収装置の構成図である。FIG. 2 is a configuration diagram of a condensate water recovery device of a conventional example.
1 ボイラ― 2 蒸気使用機器 3 スチ―ムトラップ 4 ヘッダ― 5 エゼクタ 6 循環路 7 循環ポンプ 8 復水回収管路 11 給水タンク 12 給水ポンプ 16 冷却水供給管 17 温度センサ― 18 温度コントロ―ラ 20 注入ポンプ 1 Boiler 2 Steam-using equipment 3 Steam trap 4 Header-5 Ejector 6 Circulation path 7 Circulation pump 8 Condensate recovery pipeline 11 Water tank 12 Water pump 16 Cooling water supply pipe 17 Temperature sensor 18 Temperature controller 20 Injection pump
Claims (1)
ポンプにより、ボイラ―あるいは給水タンク等の復水回
収先へ圧送するものにおいて、給水タンクに冷却水を供
給する冷却水供給管と、給水タンク内の液温を検出する
温度検出手段を設けて、当該給水タンク内の液温を所定
温度に維持すると共に、給水タンク内の流体を復水回収
ポンプの復水流入側に注入するタンク流体注入手段を設
けたことを特徴とする復水回収装置。1. A cooling water supply pipe for supplying cooling water to a water tank, wherein condensed water generated by steam-using equipment is pressure-fed to a condensate recovery destination such as a boiler or a water tank by a condensate recovery pump. , Providing temperature detecting means for detecting the liquid temperature in the water supply tank to maintain the liquid temperature in the water supply tank at a predetermined temperature and inject the fluid in the water supply tank to the condensate inflow side of the condensate recovery pump A condensate recovery device comprising tank fluid injection means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29194795A JP3725221B2 (en) | 1995-10-13 | 1995-10-13 | Condensate recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29194795A JP3725221B2 (en) | 1995-10-13 | 1995-10-13 | Condensate recovery device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09112808A true JPH09112808A (en) | 1997-05-02 |
| JP3725221B2 JP3725221B2 (en) | 2005-12-07 |
Family
ID=17775525
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29194795A Expired - Fee Related JP3725221B2 (en) | 1995-10-13 | 1995-10-13 | Condensate recovery device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3725221B2 (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004278870A (en) * | 2003-03-14 | 2004-10-07 | Tlv Co Ltd | Condensate re-evaporation device |
| JP2010164237A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2010164236A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2010164235A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2010164234A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2011237065A (en) * | 2010-05-07 | 2011-11-24 | Samson Co Ltd | High-temperature drain collection system |
| WO2013024826A1 (en) * | 2011-08-12 | 2013-02-21 | 株式会社ビクター特販 | Heat recovery apparatus and heat recovery system |
| CN103292313A (en) * | 2013-05-30 | 2013-09-11 | 浙江莱美纺织印染科技有限公司 | Closed condensate recycling system |
| CN112229235A (en) * | 2020-10-15 | 2021-01-15 | 天津渤化永利化工股份有限公司 | A condensate recovery device and control method thereof |
-
1995
- 1995-10-13 JP JP29194795A patent/JP3725221B2/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004278870A (en) * | 2003-03-14 | 2004-10-07 | Tlv Co Ltd | Condensate re-evaporation device |
| JP2010164237A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2010164236A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2010164235A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2010164234A (en) * | 2009-01-15 | 2010-07-29 | Tlv Co Ltd | Condensate returning device |
| JP2011237065A (en) * | 2010-05-07 | 2011-11-24 | Samson Co Ltd | High-temperature drain collection system |
| WO2013024826A1 (en) * | 2011-08-12 | 2013-02-21 | 株式会社ビクター特販 | Heat recovery apparatus and heat recovery system |
| JP2013057494A (en) * | 2011-08-12 | 2013-03-28 | Victor Tokuhan Co Ltd | Heat recovery apparatus and heat recovery system |
| US9664379B2 (en) | 2011-08-12 | 2017-05-30 | Victor Tokuhan Co., Ltd. | Heat recovery apparatus and heat recovery system |
| CN103292313A (en) * | 2013-05-30 | 2013-09-11 | 浙江莱美纺织印染科技有限公司 | Closed condensate recycling system |
| CN112229235A (en) * | 2020-10-15 | 2021-01-15 | 天津渤化永利化工股份有限公司 | A condensate recovery device and control method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3725221B2 (en) | 2005-12-07 |
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