JPH11201393A - Condensate discharging device - Google Patents
Condensate discharging deviceInfo
- Publication number
- JPH11201393A JPH11201393A JP1782598A JP1782598A JPH11201393A JP H11201393 A JPH11201393 A JP H11201393A JP 1782598 A JP1782598 A JP 1782598A JP 1782598 A JP1782598 A JP 1782598A JP H11201393 A JPH11201393 A JP H11201393A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- pressure
- condensate
- differential pressure
- steam trap
- 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.)
- Pending
Links
- 238000007599 discharging Methods 0.000 title claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 26
- 230000001105 regulatory effect Effects 0.000 abstract 3
- 239000012530 fluid Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000005086 pumping Methods 0.000 description 9
- 230000007423 decrease Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
- Control Of Fluid Pressure (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は蒸気使用装置内に滞
留する不凝縮性の気体としてのエア―や、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、装置内部に滞留するエア―や、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。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for discharging air as non-condensable gas staying in a steam-using device and condensate generated by condensing steam from the steam-using device. Normally, in a steam-using apparatus, in order to improve the heating efficiency by steam, air stagnating inside the apparatus and condensate generated by heating the steam are quickly discharged out of the apparatus.
【0002】[0002]
【従来の技術】従来から初期エア―や復水を排出するも
のとして、所謂スチ―ムトラップが用いられていた。ス
チ―ムトラップは各種型式のものが用いられているが、
蒸気と復水の比重差を利用して復水が流入してくればフ
ロ―トが浮上して弁口を開口することにより復水を系外
へ排出するものや、バイメタルやベロ―ズ等の温度応動
素子を組み込んで蒸気よりも所定温度低くなった復水や
エア―を排出するもの等が使用されている。2. Description of the Related Art Conventionally, a so-called steam trap has been used to discharge initial air and condensate. Various types of steam traps are used,
If condensate flows in using the specific gravity difference between steam and condensate, float floats up and opens the valve port to discharge condensate out of the system, bimetal, bellows, etc. A device which incorporates a temperature responsive element and discharges condensate or air having a predetermined temperature lower than that of steam is used.
【0003】[0003]
【発明が解決しようとする課題】従来から用いられてい
るスチ―ムトラップは、スチ―ムトラップの入口側と出
口側の圧力差が小さくなると、復水を確実に排出するこ
とができずに、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、蒸気使用装置における負荷量が変動して
蒸気使用装置内の圧力が低下して出口側と圧力差が無く
なるような場合、あるいは、蒸気使用装置の出口側が何
等かの要因によって入口側の圧力よりも高くなってしま
った場合には、蒸気使用装置で発生した復水がスチ―ム
トラップに確実に流下することができず滞留してしまう
のである。A conventional steam trap cannot reliably discharge condensed water when the pressure difference between the inlet side and the outlet side of the steam trap becomes small, so that steam cannot be discharged. There was a problem that the condensed water stayed in the used equipment. When the steam use pressure is low and there is almost no difference from the atmospheric pressure, or when the load in the steam use device fluctuates and the pressure in the steam use device drops and there is no pressure difference from the outlet side, or If the pressure on the outlet side of the used equipment becomes higher than the pressure on the inlet side for some reason, the condensate generated in the steam using equipment cannot flow down to the steam trap without fail and stays. It is.
【0004】従って本発明の課題は、蒸気使用装置等で
発生した復水を確実に排出することができるようにし
て、復水を滞留することがない復水排出装置を得ること
である。[0004] It is therefore an object of the present invention to provide a condensate discharge device that can reliably discharge condensate generated in a steam-using device or the like and that does not accumulate condensate.
【0005】[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、蒸気使用装置に不凝縮性の
気体や凝縮した復水を排出するスチ―ムトラップを取り
付けたものにおいて、スチ―ムトラップの入口側と出口
側の圧力差により開閉弁する差圧弁をスチ―ムトラップ
と並列に配置して、当該差圧弁の入口側をスチ―ムトラ
ップの入口側と連通し出口側を液体圧送手段と接続した
ものである。The means of the present invention taken to solve the above-mentioned problems are the ones in which a steam trap is attached to a steam-using device to discharge a non-condensable gas or condensed condensate. A differential pressure valve that opens and closes due to the pressure difference between the inlet side and the outlet side of the steam trap is arranged in parallel with the steam trap, the inlet side of the differential pressure valve communicates with the inlet side of the steam trap, and the outlet side is liquid. It is connected to the pumping means.
【0006】[0006]
【発明の実施の形態】差圧弁をスチ―ムトラップと並列
に配置して、差圧弁の入口側をスチ―ムトラップの入口
側と連通し出口側を液体圧送手段と接続したことによ
り、スチ―ムトラップの入口側と出口側の圧力差が小さ
くなって所定の差圧になると差圧弁が開弁して、スチ―
ムトラップの入口側と液体圧送手段が連通し、排出する
ことができずに滞留していたスチ―ムトラップの入口側
の復水は液体圧送装置内へ流下して系外へ排出される。BEST MODE FOR CARRYING OUT THE INVENTION A steam trap is provided by arranging a differential pressure valve in parallel with a steam trap, and connecting the inlet side of the differential pressure valve with the inlet side of the steam trap and connecting the outlet side to a liquid pressure feeding means. When the pressure difference between the inlet side and the outlet side becomes smaller and reaches a predetermined differential pressure, the differential pressure valve opens,
The inlet side of the steam trap communicates with the liquid pumping means, and the condensed water at the inlet side of the steam trap, which could not be discharged and stayed, flows down into the liquid pumping device and is discharged out of the system.
【0007】スチ―ムトラップの入口側と出口側の差圧
が通常の場合、即ち、入口側が充分に出口側よりも高い
場合は、差圧弁は閉弁して液体圧送手段と連通すること
はなく、スチ―ムトラップは従来通りその差圧に応じて
自力で復水を出口側から排出することができる。When the pressure difference between the inlet side and the outlet side of the steam trap is normal, that is, when the inlet side is sufficiently higher than the outlet side, the differential pressure valve closes and does not communicate with the liquid pumping means. The steam trap can discharge the condensed water from the outlet side by itself according to the pressure difference as before.
【0008】[0008]
【実施例】蒸気使用装置1に熱交換用の蒸気を供給する
蒸気供給管2を圧力調節弁3を介して接続する。蒸気使
用装置1の下方にはスチ―ムトラップ4を取り付ける。
スチ―ムトラップ4は、蒸気使用装置1内で生じた蒸気
の凝縮水としての復水や不凝縮性の気体であるエア―等
を自動的に外部へ排出するものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A steam supply pipe 2 for supplying steam for heat exchange to a steam using apparatus 1 is connected via a pressure control valve 3. A steam trap 4 is attached below the steam-using device 1.
The steam trap 4 automatically condenses steam generated in the steam-using device 1 as condensed water or automatically discharges air, which is a non-condensable gas, to the outside.
【0009】スチ―ムトラップ4と並列に差圧弁7を配
置してその入口を管路17によりスチ―ムトラップ4の
入口と連通する。差圧弁7の出口側には管路25を介し
て液体圧送手段26を接続する。差圧弁7は、入口9と
出口10を区画する弁体11を上下動自在に配置し、弁
体11と接続した弁棒12にコイルバネ13とダイヤフ
ラム14を取り付けて、ダイヤフラム14で区画した上
差圧室15を連通路20によりスチ―ムトラップ4の入
口側と連通すると共に、下差圧室16を同じく連通路2
1によりスチ―ムトラップ4の出口側と連通する。A differential pressure valve 7 is arranged in parallel with the steam trap 4, and its inlet communicates with the inlet of the steam trap 4 via a pipe 17. The liquid pressure feeding means 26 is connected to the outlet side of the differential pressure valve 7 via a pipe 25. The differential pressure valve 7 has a valve body 11 that defines an inlet 9 and an outlet 10 movably arranged up and down. A coil spring 13 and a diaphragm 14 are attached to a valve rod 12 connected to the valve body 11, and an upper differential defined by the diaphragm 14. The pressure chamber 15 communicates with the inlet side of the steam trap 4 through the communication passage 20, and the lower differential pressure chamber 16 also communicates with the communication passage 2.
1 communicates with the outlet side of the steam trap 4.
【0010】差圧弁7は、スチ―ムトラップ4の入口側
と出口側の差圧がダイヤフラム14で検出されて、その
差圧が所定値よりも小さくなるとダイヤフラム14が上
方へ変位して弁体11も上方へ変位し、入口9と出口1
0を連通して、管路17,25を介してスチ―ムトラッ
プ4の入口側と液体圧送手段26とを連通するものであ
る。The differential pressure valve 7 detects the differential pressure between the inlet side and the outlet side of the steam trap 4 by the diaphragm 14, and when the differential pressure becomes smaller than a predetermined value, the diaphragm 14 is displaced upward and the valve body 11 is displaced upward. Is also displaced upward, the entrance 9 and the exit 1
0, and connects the inlet side of the steam trap 4 and the liquid pressure feeding means 26 via the pipes 17 and 25.
【0011】蒸気供給管2の一部を分岐して蒸気分岐管
5を設け、バルブ6を介して液体圧送手段26の蒸気導
入口27と接続する。液体圧送手段26は、本実施例に
おいては蒸気導入口27から導入される高圧の蒸気によ
り、内部に溜った液体としての復水を所定箇所へ圧送す
るものを用いた例を示す。液体圧送手段26としてはそ
の他に、復水を溜め置くタンクと、タンク内の液位に応
じて駆動または停止する循環ポンプを組み合わせたもの
を用いることもできる。A part of the steam supply pipe 2 is branched to provide a steam branch pipe 5, which is connected via a valve 6 to a steam inlet 27 of a liquid pressure feeding means 26. In the present embodiment, the liquid pumping means 26 is an example in which a liquid condensed as a liquid stored therein is pumped to a predetermined location by high-pressure steam introduced from the steam inlet 27. Alternatively, as the liquid pressure feeding means 26, a combination of a tank for storing condensed water and a circulation pump for driving or stopping according to the liquid level in the tank can be used.
【0012】液体圧送手段26には、復水流入口28と
復水圧送口29、及び、蒸気導入口27の側部に大気連
通口30を設けて、復水流入口28と差圧弁7を管路2
5と逆止弁22を介して連通し、復水圧送口29に逆止
弁23を介して圧送管路24を連通する。The liquid pressure feeding means 26 is provided with a condensate inlet 28 and a condensate pressure feed port 29, and an air communication port 30 on the side of the steam inlet 27, and connects the condensate inlet 28 and the differential pressure valve 7 to a pipeline. 2
5 through a check valve 22, and a condensate feed line 29 through a check valve 23 to a condensate pressure feed port 29.
【0013】液体圧送手段26は、図示はしていない
が、復水流入口28から流下してきた復水が内部で所定
量溜ると液位検知手段が作動して蒸気導入口27を開口
すると同時に大気連通口30が閉口して、導入された高
圧の蒸気でもって溜っている復水を、復水圧送口29か
ら圧送管路24を介して所定箇所へ圧送するものであ
る。The liquid pressure feeding means 26 is not shown, but when the condensed water flowing down from the condensate inlet 28 accumulates in a predetermined amount inside, the liquid level detecting means operates to open the vapor inlet 27 and at the same time to open the atmosphere. The communication port 30 is closed, and the condensed water retained by the introduced high-pressure steam is pressure-fed from the condensed water pressure feeding port 29 to a predetermined location via the pressure feeding pipe 24.
【0014】蒸気使用装置1で熱交換して生じた復水
は、スチ―ムトラップ4の入口側の圧力が出口側の圧力
よりも所定値だけ高い場合には差圧弁7が閉弁している
と共に、スチ―ムトラップ4へ流下し、更にスチ―ムト
ラップ4から系外へ自動的に排出される。Condensate generated by heat exchange in the steam-using device 1 is closed when the pressure on the inlet side of the steam trap 4 is higher than the pressure on the outlet side by a predetermined value. At the same time, it flows down to the steam trap 4 and is automatically discharged from the steam trap 4 to the outside of the system.
【0015】スチ―ムトラップ4の出口側の圧力が高く
なるか、あるいは蒸気使用装置1側の圧力が低くなっ
て、スチ―ムトラップ4の入口側と出口側の圧力圧が小
さくなるかあるいは逆転して入口側より出口側の方が圧
力が高くなると、差圧弁7が開弁してスチ―ムトラップ
4の入口側と液体圧送手段26が管路17,25で連通
されて、スチ―ムトラップ4の入口側に滞留していた蒸
気使用装置1の復水は液体圧送手段26に流下すること
により、蒸気使用装置1内に復水を滞留することがな
い。The pressure on the outlet side of the steam trap 4 increases or the pressure on the steam-using device 1 side decreases, and the pressure pressure on the inlet side and the outlet side of the steam trap 4 decreases or reverses. When the pressure on the outlet side becomes higher than that on the inlet side, the differential pressure valve 7 is opened, and the inlet side of the steam trap 4 and the liquid pressure feeding means 26 are communicated through the pipes 17 and 25, and the steam trap 4 The condensed water of the steam-using device 1 that has stayed at the inlet side flows down to the liquid pumping means 26, so that the condensed water does not stay in the steam-using device 1.
【0016】液体圧送手段26に流下してきた復水は、
本体内に溜って所定液位に達すると蒸気導入口27が開
口し大気連通口30が閉口して、蒸気分岐管5から供給
される高圧蒸気によって圧送管路24から所定箇所へ圧
送される。圧送されて本体内の液位が低下すると蒸気導
入口27が閉口し大気連通口30が開口して、液体圧送
手段26の内部は大気圧状態となる。The condensate flowing down to the liquid pumping means 26 is:
When the liquid accumulates in the main body and reaches a predetermined liquid level, the steam introduction port 27 is opened and the air communication port 30 is closed, and the high pressure steam supplied from the steam branch pipe 5 is fed from the pressure feed pipe 24 to a predetermined location. When the liquid level in the main body is reduced by the pressure feeding, the vapor introduction port 27 is closed and the air communication port 30 is opened, and the inside of the liquid pressure feeding means 26 is brought into the atmospheric pressure state.
【0017】[0017]
【発明の効果】上記のように本発明によれば、スチ―ム
トラップの入口側と出口側の差圧が所定差圧よりも小さ
くなった場合だけ、差圧弁が開弁して液体圧送手段を介
して復水を排出することができ、蒸気使用装置で発生し
た復水を確実に系外へ排出することができる。As described above, according to the present invention, only when the differential pressure between the inlet side and the outlet side of the steam trap becomes smaller than the predetermined differential pressure, the differential pressure valve opens and the liquid pumping means is provided. The condensate can be discharged through the system, and the condensate generated in the steam-using device can be surely discharged out of the system.
【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。FIG. 1 is a configuration diagram showing an embodiment of a condensate discharge device of the present invention.
1 蒸気使用装置 2 蒸気供給管 4 スチ―ムトラップ 7 差圧弁 11 弁体 14 ダイヤフラム 15 上差圧室 16 下差圧室 17,25 管路 20,21 連通路 22,23 逆止弁 24 圧送管路 26 液体圧送手段 27 蒸気導入口 28 復水流入口 29 復水圧送口 30 大気連通口 DESCRIPTION OF SYMBOLS 1 Steam use apparatus 2 Steam supply pipe 4 Steam trap 7 Differential pressure valve 11 Valve element 14 Diaphragm 15 Upper differential pressure chamber 16 Lower differential pressure chamber 17, 25 Pipe 20, 20, Communication passage 22, 23 Check valve 24 Pressure feed pipe 26 Liquid pumping means 27 Vapor inlet 28 Condensate inlet 29 Condensate inlet 30 Atmosphere communication port
Claims (1)
た復水を排出するスチ―ムトラップを取り付けたものに
おいて、スチ―ムトラップの入口側と出口側の圧力差に
より開閉弁する差圧弁をスチ―ムトラップと並列に配置
して、当該差圧弁の入口側をスチ―ムトラップの入口側
と連通し出口側を液体圧送手段と接続したことを特徴と
する復水排出装置。1. A steam pressure-reducing valve which is provided with a steam trap for discharging a non-condensable gas or condensed condensate in a steam-using device, wherein the valve is opened and closed by a pressure difference between an inlet side and an outlet side of the steam trap. A condensate discharge device, which is disposed in parallel with a steam trap, wherein the inlet side of the differential pressure valve communicates with the inlet side of the steam trap and the outlet side is connected to a liquid pressure feeding means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1782598A JPH11201393A (en) | 1998-01-14 | 1998-01-14 | Condensate discharging device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1782598A JPH11201393A (en) | 1998-01-14 | 1998-01-14 | Condensate discharging device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11201393A true JPH11201393A (en) | 1999-07-30 |
Family
ID=11954511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1782598A Pending JPH11201393A (en) | 1998-01-14 | 1998-01-14 | Condensate discharging device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11201393A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104964166A (en) * | 2015-07-13 | 2015-10-07 | 武汉都市环保工程技术股份有限公司 | Steam pipeline drain recovery system |
-
1998
- 1998-01-14 JP JP1782598A patent/JPH11201393A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104964166A (en) * | 2015-07-13 | 2015-10-07 | 武汉都市环保工程技术股份有限公司 | Steam pipeline drain recovery system |
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