JP2013170707A - Condensate recovery device - Google Patents
Condensate recovery device Download PDFInfo
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- JP2013170707A JP2013170707A JP2012032919A JP2012032919A JP2013170707A JP 2013170707 A JP2013170707 A JP 2013170707A JP 2012032919 A JP2012032919 A JP 2012032919A JP 2012032919 A JP2012032919 A JP 2012032919A JP 2013170707 A JP2013170707 A JP 2013170707A
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本発明は、蒸気使用機器で発生した蒸気の凝縮水としての復水を、ボイラーや給水タンクや排出口等の所定の復水回収先へ回収する復水回収装置に関する。 The present invention relates to a condensate recovery apparatus that recovers condensate as condensate of steam generated in a steam-using device to a predetermined condensate recovery destination such as a boiler, a water supply tank, and a discharge port.
従来の復水回収装置は、蒸気使用機器の復水出口側を蒸気トラップと復水集合タンクを介して復水圧送部材に接続し、この復水圧送部材の高圧操作流体排出口に圧力制御弁を取り付けたもので、熱エネルギー損失を少なくすることができるものである。 A conventional condensate recovery apparatus connects a condensate outlet side of a steam-using device to a condensate pumping member via a steam trap and a condensate collecting tank, and a pressure control valve is connected to a high-pressure operation fluid discharge port of the condensate pumping member. It is possible to reduce heat energy loss.
この復水回収装置においては、蒸気使用機器で使用される蒸気圧力が低くなると、蒸気使用機器で発生した復水を確実に排出することができなくなる問題があった。これは、復水圧送部材の高圧操作流体排出口に取り付けた圧力制御弁によって、復水圧送部材の内部を大気圧以下の真空状態とすることができず、蒸気使用機器で使用される蒸気圧力が極端に低くなると、蒸気使用機器の復水を蒸気トラップを介して外部へ排出することができなくなるのである。 In this condensate recovery apparatus, there is a problem that if the steam pressure used in the steam-using device is low, the condensate generated in the steam-using device cannot be discharged reliably. This is because the pressure control valve attached to the high-pressure operating fluid discharge port of the condensate pumping member cannot bring the inside of the condensate pumping member into a vacuum state below atmospheric pressure, and the steam pressure used in steam-using equipment When the temperature becomes extremely low, the condensate of the steam-using device cannot be discharged outside through the steam trap.
解決しようとする課題は、スチームトラップの出口を大気圧以下の真空状態とすることができるようにして、蒸気使用機器で使用される蒸気圧力が極端に低くなっても復水を確実に外部へ排出することのできる復水回収装置を提供すること。 The problem to be solved is that the outlet of the steam trap can be set to a vacuum state below atmospheric pressure, so that the condensate can be reliably discharged to the outside even if the steam pressure used in the steam-using equipment becomes extremely low. To provide a condensate recovery device that can be discharged.
本発明は、蒸気使用機器で発生した復水を所定の復水回収先へ回収するものにおいて、蒸気使用機器の出口側にスチームトラップを接続して、当該スチームトラップの出口をエゼクタの吸込室に接続し、当該エゼクタのノズル部を駆動流体供給管と接続して、当該駆動流体供給管に差圧弁を配置し、当該差圧弁の一次圧検出管路の端部を、蒸気使用機器の内部と、又は、蒸気使用機器へ蒸気を供給する蒸気供給管と接続すると共に、差圧弁の二次圧検出管路の端部を、スチームトラップの出口側とエゼクタの吸込室の間に接続したものである。 The present invention collects condensate generated in steam-using equipment to a predetermined condensate collection destination, and connects a steam trap to the outlet side of the steam-using equipment and connects the outlet of the steam trap to the suction chamber of the ejector. Connect, connect the nozzle part of the ejector to the driving fluid supply pipe, place a differential pressure valve in the driving fluid supply pipe, and connect the end of the primary pressure detection pipe line of the differential pressure valve to the inside of the steam-using device. Or, it is connected to the steam supply pipe that supplies steam to the equipment that uses steam, and the end of the secondary pressure detection pipe of the differential pressure valve is connected between the outlet side of the steam trap and the suction chamber of the ejector. is there.
本発明の復水回収装置は、スチームトラップの出口をエゼクタの吸込室に接続し、このエゼクタへの駆動流体供給管に差圧弁を配置し、この差圧弁の一次圧検出管路の端部を、蒸気使用機器の内部と、又は、蒸気使用機器へ蒸気を供給する蒸気供給管と接続すると共に、差圧弁の二次圧検出管路の端部を、スチームトラップの出口側とエゼクタの吸込室の間に接続したことによって、蒸気使用機器の内部の蒸気圧力が、又は、蒸気供給管の蒸気圧力が、所定値まで低下すると差圧弁が開弁して、駆動流体供給管からエゼクタに駆動流体、例えば高圧蒸気とか高圧水、が供給されてエゼクタの吸込室で吸引力を発生することで、スチームトラップの出口を大気圧以下の真空状態とすることができる。 In the condensate recovery apparatus of the present invention, the outlet of the steam trap is connected to the suction chamber of the ejector, a differential pressure valve is arranged in the drive fluid supply pipe to the ejector, and the end of the primary pressure detection pipe line of the differential pressure valve is connected , Connected to the inside of the steam-using equipment or to the steam supply pipe for supplying steam to the steam-using equipment, and connected the end of the secondary pressure detection pipe of the differential pressure valve to the outlet side of the steam trap and the suction chamber of the ejector When the steam pressure inside the steam using device or the steam pressure in the steam supply pipe drops to a predetermined value, the differential pressure valve opens and the drive fluid is supplied from the drive fluid supply pipe to the ejector. For example, by supplying high-pressure steam or high-pressure water and generating a suction force in the suction chamber of the ejector, the outlet of the steam trap can be brought into a vacuum state below atmospheric pressure.
本発明の復水回収装置は、エゼクタを用いるものであるが、このエゼクタとしては、駆動流体を高圧蒸気とする蒸気エゼクタや、駆動流体を高圧水とする水エゼクタなど従来公知のエゼクタを用いることができる。 The condensate recovery apparatus of the present invention uses an ejector. As this ejector, a conventionally known ejector such as a steam ejector that uses high-pressure steam as a driving fluid or a water ejector that uses high-pressure water as a driving fluid is used. Can do.
図1は本発明の1実施例の構成図であって、蒸気使用機器1と、蒸気使用機器1の出口側に接続したスチームトラップ2と、スチームトラップ2の出口と接続したエゼクタ3の吸込室4と、エゼクタ3のノズル部と接続した駆動流体供給管5、及び、駆動流体供給管5に配置した差圧弁6とで復水回収装置を構成する。 FIG. 1 is a block diagram of an embodiment of the present invention, in which a steam-using device 1, a steam trap 2 connected to the outlet side of the steam-using device 1, and a suction chamber of an ejector 3 connected to the outlet of the steam trap 2 are shown. 4, the driving fluid supply pipe 5 connected to the nozzle portion of the ejector 3, and the differential pressure valve 6 disposed in the driving fluid supply pipe 5 constitute a condensate recovery device.
蒸気使用機器1には蒸気供給管7を接続する。蒸気供給管7は、蒸気使用機器1の内部で螺旋状に形成され、その出口端部にスチームトラップ2を接続する。スチームトラップ2は、蒸気使用機器1の内部の螺旋状部で熱を奪われた蒸気が凝縮した復水だけを、エゼクタ3の吸込室4側へ流下させ、蒸気を流下することはないものである。 A steam supply pipe 7 is connected to the steam using device 1. The steam supply pipe 7 is formed in a spiral shape inside the steam using device 1, and the steam trap 2 is connected to an outlet end portion thereof. The steam trap 2 causes only the condensate condensed with the steam deprived of heat in the spiral part inside the steam-using device 1 to flow down to the suction chamber 4 side of the ejector 3 and does not flow down the steam. is there.
エゼクタ3に差圧弁6を介在して駆動流体供給管5を接続する。本実施例においては、駆動流体として高圧蒸気を用いた例を示す。差圧弁6は、一次圧と二次圧との差圧に応じて自動的に開閉弁するものであり、その一次圧検出管路8を、蒸気供給管7と接続し、二次圧検出管路10の端部を、スチームトラップ2の出口側とエゼクタ3の吸込室4の間に接続する。なお、蒸気使用機器1で蒸気の直接加熱を行う場合は、一次圧検出管路8を蒸気使用機器1の内部と接続する。エゼクタ3の下部出口側には蒸気使用機器1で発生した復水を所定の復水回収先へ回収する復水回収管9を接続する。 A drive fluid supply pipe 5 is connected to the ejector 3 via a differential pressure valve 6. In the present embodiment, an example in which high-pressure steam is used as a driving fluid is shown. The differential pressure valve 6 automatically opens and closes according to the differential pressure between the primary pressure and the secondary pressure, and the primary pressure detection pipe line 8 is connected to the steam supply pipe 7 to connect the secondary pressure detection pipe. The end of the passage 10 is connected between the outlet side of the steam trap 2 and the suction chamber 4 of the ejector 3. When the steam is directly heated by the steam using device 1, the primary pressure detection pipe line 8 is connected to the inside of the steam using device 1. Connected to the lower outlet side of the ejector 3 is a condensate recovery pipe 9 for recovering the condensate generated in the steam using device 1 to a predetermined condensate recovery destination.
蒸気供給管7から蒸気使用機器1へ加熱用の高圧蒸気を供給することによって、蒸気使用機器1内の図示しない被加熱物が蒸気加熱される。加熱によって熱を奪われた蒸気は凝縮して復水となり、スチームトラップ2とエゼクタ3を経て復水回収管9から所定の復水回収先へと流下する。このように蒸気供給管7から供給される蒸気の圧力が高い場合は、差圧弁6は閉弁しており、エゼクタ3が駆動流体供給管5からの駆動流体によって駆動される必要もなく、復水は回収される。 By supplying high-pressure steam for heating from the steam supply pipe 7 to the steam using device 1, an object to be heated (not shown) in the steam using device 1 is steam heated. Steam deprived of heat by heating is condensed into condensate, and flows down from the condensate recovery pipe 9 to a predetermined condensate recovery destination via the steam trap 2 and the ejector 3. Thus, when the pressure of the steam supplied from the steam supply pipe 7 is high, the differential pressure valve 6 is closed, and the ejector 3 does not need to be driven by the drive fluid from the drive fluid supply pipe 5, so Water is recovered.
一方、蒸気供給管7から供給される蒸気の圧力が低い場合、たとえば供給蒸気圧力が大気圧程度あるいは大気圧以下の真空状態である場合は、蒸気使用機器1内で発生した復水は圧力差が無いためにスチームトラップ2から排出されることがなく、蒸気使用機器1内で滞留してしまう。 On the other hand, when the pressure of the steam supplied from the steam supply pipe 7 is low, for example, when the supply steam pressure is in a vacuum state of about atmospheric pressure or less than atmospheric pressure, the condensate generated in the steam-using device 1 has a pressure difference. Therefore, the steam trap 2 is not discharged and stays in the steam using device 1.
このように蒸気供給管7から供給される蒸気の圧力が低く、スチームトラップ2出口側の圧力が高くなっていることを、差圧弁6の一次圧検出管路8と二次圧検出管路10を介して差圧弁6が検知すると差圧弁6が自動的に開弁して、駆動流体供給管5から高圧の蒸気をエゼクタ3へ供給し、吸込室4で吸引力を発生することで、スチームトラップ2を介して蒸気使用機器1内に滞留していた復水を吸引して、復水回収管9から所定箇所へ復水を回収することができる。 The primary pressure detection line 8 and the secondary pressure detection line 10 of the differential pressure valve 6 indicate that the pressure of the steam supplied from the steam supply pipe 7 is low and the pressure on the outlet side of the steam trap 2 is high. When the differential pressure valve 6 detects the pressure, the differential pressure valve 6 automatically opens, supplies high pressure steam from the drive fluid supply pipe 5 to the ejector 3, and generates a suction force in the suction chamber 4. The condensed water staying in the steam using device 1 can be sucked through the trap 2 and the condensed water can be recovered from the condensed water recovery pipe 9 to a predetermined location.
本発明は、蒸気使用機器で使用される蒸気の圧力が低い場合であっても、確実に復水を回収することのできる復水回収装置として利用することができる。 INDUSTRIAL APPLICABILITY The present invention can be used as a condensate recovery apparatus that can reliably recover condensate even when the pressure of steam used in steam-using equipment is low.
1 蒸気使用機器
2 スチームトラップ
3 エゼクタ
4 吸込室
5 駆動流体供給管
6 差圧弁
7 蒸気供給管
8 一次圧検出管路
9 復水回収管
10 二次圧検出管路
DESCRIPTION OF SYMBOLS 1 Steam use equipment 2 Steam trap 3 Ejector 4 Suction chamber 5 Drive fluid supply pipe 6 Differential pressure valve 7 Steam supply pipe 8 Primary pressure detection pipe 9 Condensate recovery pipe 10 Secondary pressure detection pipe
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JP2012032919A JP2013170707A (en) | 2012-02-17 | 2012-02-17 | Condensate recovery device |
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JP2012032919A JP2013170707A (en) | 2012-02-17 | 2012-02-17 | Condensate recovery device |
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JP2013170707A true JP2013170707A (en) | 2013-09-02 |
JP2013170707A5 JP2013170707A5 (en) | 2015-03-05 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106247788A (en) * | 2016-09-09 | 2016-12-21 | 开平市天美洗涤有限公司 | A kind of water circuit system drying workshop steam circulation |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0571699A (en) * | 1991-09-13 | 1993-03-23 | Tlv Co Ltd | Condensate recovery device |
JPH0544563B2 (en) * | 1988-04-07 | 1993-07-06 | Tlv Co Ltd | |
US5611673A (en) * | 1994-07-19 | 1997-03-18 | Shin-Ei Kabushiki Kaisha | Vacuum jet pump for recovering a mixed fluid of gas and liquid condensates from steam-using apparatus |
JP2008170126A (en) * | 2007-01-15 | 2008-07-24 | Tlv Co Ltd | Condensate collecting apparatus |
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2012
- 2012-02-17 JP JP2012032919A patent/JP2013170707A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0544563B2 (en) * | 1988-04-07 | 1993-07-06 | Tlv Co Ltd | |
JPH0571699A (en) * | 1991-09-13 | 1993-03-23 | Tlv Co Ltd | Condensate recovery device |
US5611673A (en) * | 1994-07-19 | 1997-03-18 | Shin-Ei Kabushiki Kaisha | Vacuum jet pump for recovering a mixed fluid of gas and liquid condensates from steam-using apparatus |
JP2008170126A (en) * | 2007-01-15 | 2008-07-24 | Tlv Co Ltd | Condensate collecting apparatus |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106247788A (en) * | 2016-09-09 | 2016-12-21 | 开平市天美洗涤有限公司 | A kind of water circuit system drying workshop steam circulation |
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