JP4509301B2 - Condensate discharge device - Google Patents

Condensate discharge device Download PDF

Info

Publication number
JP4509301B2
JP4509301B2 JP2000141616A JP2000141616A JP4509301B2 JP 4509301 B2 JP4509301 B2 JP 4509301B2 JP 2000141616 A JP2000141616 A JP 2000141616A JP 2000141616 A JP2000141616 A JP 2000141616A JP 4509301 B2 JP4509301 B2 JP 4509301B2
Authority
JP
Japan
Prior art keywords
steam
valve
ejector
pressure
condensate
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
JP2000141616A
Other languages
Japanese (ja)
Other versions
JP2001324092A (en
Inventor
智明 横野
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 JP2000141616A priority Critical patent/JP4509301B2/en
Publication of JP2001324092A publication Critical patent/JP2001324092A/en
Application granted granted Critical
Publication of JP4509301B2 publication Critical patent/JP4509301B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Jet Pumps And Other Pumps (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、蒸気使用装置内で蒸気が凝縮して生じた復水を蒸気使用装置から排出するものに関し、特に供給される蒸気量が少なくなって蒸気使用装置内部の圧力が低下しても復水を確実に排出することのできる復水排出装置に関する。通常、蒸気使用装置では蒸気による加熱効率を良くするために、蒸気が加熱を行なうことによって生じた復水は、速やかに装置外へ排出されている。
【0002】
【従来の技術】
従来の復水排出装置としては、例えば特公昭51−31998号公報に示されたものがあった。これは、フィンチューブ型熱交換器の出口ヘッダに、負圧時に開き正圧時に閉じる逆止弁と、低温時に開き高温時に閉じる熱動弁の、組合せ弁を設けることにより、出口ヘッダ内部が負圧になるとこの組合せ弁から外気を導入して正圧にすることによって、スチームトラップの入口と出口の差圧を確保して、蒸気を使用する加熱装置から凝縮水としての復水を速やかに外部に排出することができるものである。
【0003】
【発明が解決しようとする課題】
上記従来の復水排出装置では、未だ尚、加熱装置内の復水を外部へ速やかに排出することができない問題があった。これは、出口ヘッダ内部が負圧になってスチームトラップの入出口の差圧が無くなり復水が排出不能になると、組合せ弁が開弁して外気を導入して出口ヘッダ内部を大気圧状態に戻してやることによって、スチームトラップの入出口の差圧を確保して復水を排出しようとするものであり、例えばスチームトラップの出口側の圧力がほぼ大気圧状態である場合は、組合せ弁から外気を導入しても、スチームトラップの入口側と出口側の圧力差がほとんど確保できず、従ってスチームトラップから復水を外部に速やかに排出することができないのである。
【0004】
従って本発明の課題は、蒸気使用装置等で発生した復水を、スチームトラップを介して確実に外部に排出することにより、復水を滞留することのない復水排出装置を得ることである。
【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、蒸気使用装置に弁を介して蒸気供給管を接続すると共に、蒸気使用装置で蒸気の凝縮した復水を排出するためのスチームトラップを取り付けたものにおいて、蒸気供給管に取り付けた弁の開度を検出する弁開度検出手段を設け、スチームトラップの出口側をエゼクタの吸引室と接続し、当該エゼクタの入口側を流体源と連通すると共に、当該流体源とエゼクタの入口側との間を連通遮断する弁手段を配置し、当該弁手段と上記弁開度検出手段を接続して、弁開度検出手段で検出した蒸気供給管の弁開度に応じて、エゼクタ入口側の弁手段を連通遮断するものである。
【0006】
【発明の実施の形態】
蒸気供給管に取り付けた弁の開度を弁開度検出手段で検出して、この弁開度が所定の値まで小さくなるかあるいは全閉になった場合に、エゼクタ入口側の弁手段が開弁してエゼクタに流体源から高圧の流体が供給され、エゼクタの吸引室で真空吸引力を発生する。この吸引力によってスチームトラップ出口側の圧力が低下し、スチームトラップの入口側と出口側の圧力差が確保され、スチームトラップを介して復水が排出される。スチームトラップから排出された復水はエゼクタの吸引室を経て外部に排除される。
【0007】
例えば、蒸気使用装置内の圧力が大気圧程度まで低下した場合でも、エゼクタで大気圧以下の真空状態とすることによって、スチームトラップの入出口間の差圧を確保することができ、スチームトラップを介して速やかに復水を排出することができる。
【0008】
【実施例】
本実施例においては蒸気使用装置1としてフィンチューブ型熱交換器を用いた例を示す。熱交換器1に加熱用の蒸気を供給する蒸気供給管2を、供給量を任意に調節する弁としての圧力調節弁3とバルブ13を介して接続する。圧力調節弁3の内部には図示しない弁開度検出手段としてのポテンショメータやロータリーエンコーダ等を内蔵する。熱交換器1の下方にはスチームトラップ4を取り付ける。スチームトラップ4は、熱交換器1内で発生した蒸気の凝縮水としての復水や蒸気に混入している不凝縮性の気体であるエアー等を自動的に外部へ排出するものである。
【0009】
フィンチューブ型熱交換器1は、両側方に入口ヘッダ5と出口ヘッダ6を備えて、蒸気供給管2から供給される所定圧力の蒸気が入口ヘッダ5から図示しない分割された多数の熱交換器1内部に供給されて、通過する空気等の被熱交換物と熱交換するものである。熱交換した蒸気は凝縮して復水となり、出口ヘッダ6に至る。
【0010】
出口ヘッダ6の下部にはスチームトラップ4を接続する。スチームトラップ4の出口側は管路8を介してエゼクタ9の吸引室10と接続する。エゼクタ9は、本実施例においてはスチームを駆動源として吸引室10で真空吸引力を発生することのできるスチームエゼクタを用いた例を示す。
【0011】
スチームエゼクタ9の入口側に、蒸気供給管2の一部を分岐した蒸気分岐管11を接続する。蒸気分岐管11から供給される高圧の蒸気がエゼクタ9の駆動流体源となる。蒸気供給管2とエゼクタ9の間に弁手段としての電動弁12と逆止弁16を設けて両者の間を連通遮断する。スチームエゼクタ9の出口側は、ディフューザ14と排出管15を設けて、スチームトラップ4から流下する復水を所定箇所へ排出することができるようにする。
【0012】
電動弁12及び圧力調節弁3はそれぞれコントローラ7と電気接続する。圧力調節弁3に内蔵した弁開度検出手段で圧力調節弁3の弁開度を検出して、コントローラ7に予め設定しておいた弁開度よりも小さくなると電動弁12を開弁するものである。
【0013】
フィンチューブ型熱交換器1で熱交換して生じた復水は、圧力調節弁3の開度が比較的大きく供給される蒸気の量が多くて熱交換器1内の圧力の方がスチームトラップ4の出口管路8側の圧力よりも高い場合にはスチームトラップ4へ自然に流下し、更にスチームエゼクタ9の吸引室10とディフューザ14を通って排出管15から系外へ排出される。このように圧力調節弁3の弁開度が比較的大きい場合は、電動弁12は閉弁している。
【0014】
熱交換器1内の圧力は、圧力調節弁3から供給される蒸気の量が充分に多い場合は大気圧以上の高圧を維持しているが、圧力調節弁3の弁開度が小さくなって蒸気の供給量が少なくなると、供給される蒸気量よりも熱交換器1内で凝縮する蒸気量の方が多くなって大気圧以下の負圧状態となることもある。例えば、調節弁3の開度が約25%以下くらいに小さくなると熱交換器1内が負圧になるケースが多々ある。このように、圧力調節弁3の弁開度が小さくなって熱交換器1内の圧力が低くなることを、圧力調節弁3に内蔵した弁開度検出手段が検知して、電動弁12を開弁することによりエゼクタ9に高圧蒸気が供給されて吸引室10で真空吸引力を生じる。
【0015】
エゼクタ9で発生する真空吸引力を、供給する蒸気の圧力や量を調節して熱交換器1内の圧力よりも低い値とすることによって、熱交換器1内とエゼクタ9の間、即ち、スチームトラップ4の入口側と出口側の間に、所定の圧力差を作り出すことができ、出口ヘッダ6内の復水をスチームトラップ4を介して速やかに排出することができる。トラップ4を通過した復水はエゼクタ9で高圧蒸気と混合されて排出管15から所定箇所へ至る。
【0016】
本実施例においては、蒸気使用装置としてフィンチューブ型熱交換器を用いた例を示したが、その他のエアハンドリングユニットとか熱風乾燥機、温水製造装置等の比較的低温で蒸気加熱するものに用いることができる。また、本実施例においては、エゼクタ9としてスチームエゼクタを用いた例を示したが、エゼクタ9の駆動源はスチームに限ることなく、例えば高圧の圧縮空気であるとか、あるいは、高圧水等を用いることができる。
【0017】
【発明の効果】
上記のように本発明によれば、圧力調節弁の弁開度が絞られてスチームトラップの入口側の圧力が低下し出口側との差圧が小さくなった場合に、弁手段が開弁してエゼクタの吸引力でもってスチームトラップの入出口間の差圧を作り出すことができ、蒸気使用装置で発生した復水を速やかに且つ確実に系外へ排出することができる。
【図面の簡単な説明】
【図1】本発明の復水排出装置の実施例を示す構成図である。
【符号の説明】
1 蒸気使用装置
2 蒸気供給管
3 圧力調節弁
4 スチームトラップ
9 エゼクタ
10 吸引室
11 分岐管
12 電動弁
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for discharging condensate produced by condensation of steam in a steam using apparatus from the steam using apparatus, and particularly, even if the amount of supplied steam decreases and the pressure inside the steam using apparatus decreases. The present invention relates to a condensate discharge device capable of reliably discharging water. Usually, in a steam using apparatus, in order to improve the heating efficiency by steam, the condensate generated by heating the steam is quickly discharged out of the apparatus.
[0002]
[Prior art]
As a conventional condensate discharging apparatus, for example, there is one disclosed in Japanese Patent Publication No. 51-31998. This is because the outlet header of the finned tube heat exchanger is provided with a combination of a check valve that opens at negative pressure and closes at positive pressure, and a thermal valve that opens at low temperature and closes at high temperature. When the pressure reaches, the outside air is introduced from this combination valve to a positive pressure to ensure a differential pressure between the inlet and outlet of the steam trap, and the condensate as condensate is quickly removed from the heating device using steam. Can be discharged.
[0003]
[Problems to be solved by the invention]
In the conventional condensate discharging apparatus, there is still a problem that the condensate in the heating apparatus cannot be quickly discharged to the outside. This is because when the pressure inside the outlet header becomes negative and the differential pressure at the inlet and outlet of the steam trap disappears and the condensate cannot be discharged, the combination valve opens and introduces outside air to bring the outlet header to atmospheric pressure. By returning it, it is intended to discharge the condensate while ensuring the differential pressure at the inlet and outlet of the steam trap.For example, when the pressure on the outlet side of the steam trap is almost atmospheric, the outside air from the combination valve However, the pressure difference between the inlet side and the outlet side of the steam trap can hardly be ensured, and therefore the condensate cannot be quickly discharged from the steam trap to the outside.
[0004]
Accordingly, an object of the present invention is to obtain a condensate discharge device that does not retain condensate by reliably discharging the condensate generated by a steam using device or the like to the outside through a steam trap.
[0005]
[Means for Solving the Problems]
The means of the present invention devised to solve the above-mentioned problem is that a steam supply pipe is connected to the steam using device via a valve, and a steam trap for discharging condensate condensed with steam in the steam using device is provided. In the attached one, a valve opening degree detecting means for detecting the opening degree of the valve attached to the steam supply pipe is provided, the outlet side of the steam trap is connected to the suction chamber of the ejector, and the inlet side of the ejector is communicated with the fluid source. In addition, a valve means for disconnecting communication between the fluid source and the inlet side of the ejector is disposed, and the steam supply pipe detected by the valve opening degree detecting means is connected by connecting the valve means and the valve opening degree detecting means. The valve means on the ejector inlet side is cut off in accordance with the valve opening degree.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
When the opening degree of the valve attached to the steam supply pipe is detected by the valve opening degree detecting means, and the valve opening degree is reduced to a predetermined value or fully closed, the valve means on the ejector inlet side is opened. A high-pressure fluid is supplied from the fluid source to the ejector, and a vacuum suction force is generated in the suction chamber of the ejector. This suction force reduces the pressure on the outlet side of the steam trap, ensures a pressure difference between the inlet side and the outlet side of the steam trap, and condensate is discharged through the steam trap. Condensate discharged from the steam trap is discharged outside through the suction chamber of the ejector.
[0007]
For example, even when the pressure in the steam using device drops to about atmospheric pressure, the pressure difference between the inlet and outlet of the steam trap can be secured by setting the vacuum state below the atmospheric pressure with the ejector. The condensate can be discharged quickly via
[0008]
【Example】
In the present embodiment, an example in which a fin tube type heat exchanger is used as the steam using device 1 is shown. A steam supply pipe 2 for supplying steam for heating to the heat exchanger 1 is connected via a pressure control valve 3 and a valve 13 as a valve for arbitrarily adjusting the supply amount. The pressure control valve 3 includes a potentiometer, a rotary encoder, etc. as valve opening degree detection means (not shown). A steam trap 4 is attached below the heat exchanger 1. The steam trap 4 automatically discharges condensate as condensed water of steam generated in the heat exchanger 1 or air that is a non-condensable gas mixed in the steam to the outside.
[0009]
The finned tube heat exchanger 1 includes an inlet header 5 and an outlet header 6 on both sides, and a plurality of heat exchangers in which steam of a predetermined pressure supplied from the steam supply pipe 2 is divided from the inlet header 5 (not shown). 1 is supplied to the inside and exchanges heat with a heat exchange object such as air passing therethrough. The heat-exchanged steam is condensed to condensate and reaches the outlet header 6.
[0010]
A steam trap 4 is connected to the lower part of the outlet header 6. The outlet side of the steam trap 4 is connected to the suction chamber 10 of the ejector 9 via a pipe line 8. In this embodiment, the ejector 9 is an example using a steam ejector that can generate a vacuum suction force in the suction chamber 10 using steam as a drive source.
[0011]
A steam branch pipe 11 that branches a part of the steam supply pipe 2 is connected to the inlet side of the steam ejector 9. High-pressure steam supplied from the steam branch pipe 11 serves as a drive fluid source for the ejector 9. An electric valve 12 and a check valve 16 are provided as valve means between the steam supply pipe 2 and the ejector 9 to cut off communication between them. A diffuser 14 and a discharge pipe 15 are provided on the outlet side of the steam ejector 9 so that the condensate flowing down from the steam trap 4 can be discharged to a predetermined location.
[0012]
The motor-operated valve 12 and the pressure control valve 3 are electrically connected to the controller 7 respectively. The valve opening degree detecting means built in the pressure control valve 3 detects the valve opening degree of the pressure control valve 3 and opens the motor-operated valve 12 when the valve opening degree set in advance in the controller 7 becomes smaller. It is.
[0013]
Condensate produced by heat exchange in the finned tube heat exchanger 1 has a relatively large opening amount of the pressure control valve 3 and a large amount of steam is supplied, and the pressure in the heat exchanger 1 is steam trapped. If the pressure is higher than the pressure on the outlet line 8 side of the steam outlet 4, it naturally flows down to the steam trap 4, and is further discharged from the discharge pipe 15 through the suction chamber 10 and the diffuser 14 of the steam ejector 9. Thus, when the valve opening degree of the pressure control valve 3 is relatively large, the motor-operated valve 12 is closed.
[0014]
When the amount of steam supplied from the pressure control valve 3 is sufficiently large, the pressure in the heat exchanger 1 is maintained at a high pressure equal to or higher than the atmospheric pressure, but the valve opening degree of the pressure control valve 3 is reduced. When the supply amount of steam decreases, the amount of steam condensed in the heat exchanger 1 may increase more than the amount of supplied steam, resulting in a negative pressure state below atmospheric pressure. For example, there are many cases where the inside of the heat exchanger 1 becomes negative pressure when the opening degree of the control valve 3 is reduced to about 25% or less. Thus, the valve opening degree detection means built in the pressure control valve 3 detects that the valve opening degree of the pressure control valve 3 becomes small and the pressure in the heat exchanger 1 becomes low, and the electric valve 12 is turned on. By opening the valve, high-pressure steam is supplied to the ejector 9 and a vacuum suction force is generated in the suction chamber 10.
[0015]
The vacuum suction force generated in the ejector 9 is adjusted to a value lower than the pressure in the heat exchanger 1 by adjusting the pressure and amount of the supplied steam, that is, between the heat exchanger 1 and the ejector 9, that is, A predetermined pressure difference can be created between the inlet side and the outlet side of the steam trap 4, and the condensate in the outlet header 6 can be quickly discharged through the steam trap 4. Condensate that has passed through the trap 4 is mixed with high-pressure steam by an ejector 9 and reaches a predetermined location from a discharge pipe 15.
[0016]
In this embodiment, an example using a fin tube type heat exchanger as a steam using device has been shown. However, it is used for other air handling units, hot air dryers, hot water producing devices, etc. that are steam heated at a relatively low temperature. be able to. In the present embodiment, an example in which a steam ejector is used as the ejector 9 is shown. However, the drive source of the ejector 9 is not limited to steam, and for example, high-pressure compressed air or high-pressure water is used. be able to.
[0017]
【The invention's effect】
As described above, according to the present invention, when the valve opening degree of the pressure control valve is reduced and the pressure on the inlet side of the steam trap decreases and the differential pressure with respect to the outlet side decreases, the valve means opens. Thus, the differential pressure between the inlet and outlet of the steam trap can be created by the suction force of the ejector, and the condensate generated in the steam using device can be quickly and reliably discharged out of the system.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of a condensate discharging apparatus according to the present invention.
[Explanation of symbols]
1 Steam Use Device 2 Steam Supply Pipe 3 Pressure Control Valve 4 Steam Trap 9 Ejector 10 Suction Chamber 11 Branch Pipe 12 Motorized Valve

Claims (1)

蒸気使用装置に弁を介して蒸気供給管を接続すると共に、蒸気使用装置で蒸気の凝縮した復水を排出するためのスチームトラップを取り付けたものにおいて、蒸気供給管に取り付けた弁の開度を検出する弁開度検出手段を設け、スチームトラップの出口側をエゼクタの吸引室と接続し、当該エゼクタの入口側を流体源と連通すると共に、当該流体源とエゼクタの入口側との間を連通遮断する弁手段を配置し、当該弁手段と上記弁開度検出手段を接続して、弁開度検出手段で検出した蒸気供給管の弁開度に応じて、エゼクタ入口側の弁手段を連通遮断することを特徴とする復水排出装置。When the steam supply pipe is connected to the steam using device via a valve and a steam trap for discharging the condensed condensate of the steam is attached to the steam using device, the opening degree of the valve attached to the steam supply pipe is A valve opening detection means for detecting is provided, the outlet side of the steam trap is connected to the suction chamber of the ejector, the inlet side of the ejector is communicated with the fluid source, and the fluid source is communicated with the inlet side of the ejector. A valve means for blocking is arranged, and the valve means and the valve opening degree detecting means are connected, and the valve means on the ejector inlet side is communicated according to the valve opening degree of the steam supply pipe detected by the valve opening degree detecting means. Condensate drainage device characterized by blocking.
JP2000141616A 2000-05-15 2000-05-15 Condensate discharge device Expired - Fee Related JP4509301B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000141616A JP4509301B2 (en) 2000-05-15 2000-05-15 Condensate discharge device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000141616A JP4509301B2 (en) 2000-05-15 2000-05-15 Condensate discharge device

Publications (2)

Publication Number Publication Date
JP2001324092A JP2001324092A (en) 2001-11-22
JP4509301B2 true JP4509301B2 (en) 2010-07-21

Family

ID=18648706

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000141616A Expired - Fee Related JP4509301B2 (en) 2000-05-15 2000-05-15 Condensate discharge device

Country Status (1)

Country Link
JP (1) JP4509301B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012193881A (en) * 2011-03-15 2012-10-11 Tlv Co Ltd Condensate recovery device

Also Published As

Publication number Publication date
JP2001324092A (en) 2001-11-22

Similar Documents

Publication Publication Date Title
EP1795844A3 (en) Steam-heating apparatus
CN106642470A (en) Water-cooling type thermostatic and humidity-static air conditioner
JP4509301B2 (en) Condensate discharge device
JP2003232581A (en) Air conditioner
JP4865466B2 (en) Air heater
CN206546051U (en) A kind of used heat defroster of cooling-water machine
JP2001324282A (en) Condensate discharger
JP2001324294A (en) Condensate discharger
JP4387536B2 (en) Steam heating device
JP2001324295A (en) Condensate discharger
JP2004163048A (en) Air heating apparatus
JP2001227877A (en) Heat exchanger
JP4583610B2 (en) Steam heating device
US11841147B2 (en) Heat recovery apparatus and methods of increasing energy efficiency of hybrid heating systems using the apparatus
JP2004138255A (en) Steam heat exchanger
JP2001227879A (en) Heat exchanger
JP3790005B2 (en) Heat exchanger
JP4330730B2 (en) Steam heating device
JP2008070087A (en) Air heater
JP4865465B2 (en) Air heater
CN213480754U (en) Drying equipment
JP3282000B2 (en) Steam heating evaporative cooling system
CN219265014U (en) Steam treatment device
JP4409715B2 (en) Steam heating device
CN218065640U (en) Energy exchange type food drying and dehumidifying device

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20070123

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100401

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100427

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100428

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130514

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 4509301

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees