JPH0320197A - Malfunction detector for steam pipe - Google Patents
Malfunction detector for steam pipeInfo
- Publication number
- JPH0320197A JPH0320197A JP15326489A JP15326489A JPH0320197A JP H0320197 A JPH0320197 A JP H0320197A JP 15326489 A JP15326489 A JP 15326489A JP 15326489 A JP15326489 A JP 15326489A JP H0320197 A JPH0320197 A JP H0320197A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- drain
- orifice
- outlet
- separator
- 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
- 230000007257 malfunction Effects 0.000 title 1
- 239000012530 fluid Substances 0.000 claims abstract description 4
- 230000005856 abnormality Effects 0.000 claims description 8
- 238000001514 detection method Methods 0.000 claims description 7
- 238000004891 communication Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 19
- 230000002159 abnormal effect Effects 0.000 abstract description 7
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000005192 partition Methods 0.000 description 5
- 238000007599 discharging Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Landscapes
- Measuring Volume Flow (AREA)
Abstract
Description
【発明の詳細な説明】
く産業上の利用分野〉
本発明は蒸気管に発生するドレンを蒸気から分離し、分
離したドレン量を測定することにより、蒸気管の異常、
ひいては、ボイラーや、蒸気管がらドレンを排出するス
チームトラップ等の異常を検出する蒸気管の異常検出装
置に関する。[Detailed description of the invention] Industrial application field> The present invention separates condensate generated in steam pipes from steam and measures the amount of separated condensate, thereby detecting abnormalities in steam pipes.
The present invention further relates to a steam pipe abnormality detection device that detects abnormalities in boilers, steam traps that discharge condensate from steam pipes, and the like.
ボイラーで発生した蒸気を各蒸気使用機器に供給する蒸
気管には、ボイラー水のキャリーオーバーによる水滴や
、自然放熱により発生したドレンが混入している。通常
蒸気管にはスチームトラップを接続してドレンを自動的
に排出している。しかし、スチームトラップが排出不良
に至ったり、キャリーオーバーの量が多くなると、蒸気
管には多量のドレンが混入し、ウォーターハンマーを生
じることによる機器の損傷を招いたり、ドレンが蒸気使
用機器に至ることにより蒸気使用機器の生産性の低下を
きたすことがあった。The steam pipes that supply the steam generated in the boiler to each steam-using device are contaminated with water droplets due to carryover of boiler water and condensate generated due to natural heat radiation. Usually, a steam trap is connected to the steam pipe to automatically discharge the condensate. However, if the steam trap fails to discharge or the amount of carryover increases, a large amount of condensate will get mixed into the steam pipe, causing water hammer and damaging equipment, or the condensate will reach steam-using equipment. This sometimes caused a decrease in the productivity of steam-using equipment.
く従来の技術〉
蒸気管の一定間隔ごとにスチームトラップを設けてドレ
ンを自動的に排出したり、蒸気使用機器の入口に蒸気と
ドレンを分離する気水分離器を配してドレンを強制的に
排除することが一般的に行なわれている。Conventional technology> Steam traps are installed at regular intervals in steam pipes to automatically discharge condensate, or steam and water separators are placed at the inlets of steam-using equipment to force condensate out. It is common practice to exclude
く本発明が解決しようとする課題〉
気水分離器の分離能力には自ずと限界があり、蒸気管の
異常による限界を越えたドレンが流入してきても、上記
のものではその異常状態を検出することかできず、ドレ
ンが蒸気使用機器に流入し続けてしまう問題があった。Problems to be Solved by the Present Invention The separation ability of a steam-water separator naturally has a limit, and even if drain exceeding the limit flows in due to an abnormality in the steam pipe, the above-mentioned device cannot detect the abnormal state. There was a problem in that the condensate continued to flow into the steam-using equipment.
ドレンが多量に発生する要因は、上述のキャリーオーバ
ーやスチームトラップの排出不良の他に蒸気管の保温不
良等がある。Factors that cause a large amount of condensate to occur include the above-mentioned carryover and poor discharge of steam traps, as well as poor heat retention of steam pipes.
本発明の技術的課題は、蒸気管の分離したドレン量を測
定することにより、蒸気管の異常、すなわち、ボイラー
のキャリーオーバーやスチームトラップの排出不良、及
び、蒸気管の保温不良等を検知して、分離器で分離しき
れないドレンが蒸気使用機器へ流入し続けたり、ウォー
ターハンマーが発生することを防止することである。The technical problem of the present invention is to detect abnormalities in steam pipes, such as boiler carryover, steam trap discharge failure, and steam pipe heat retention failure, by measuring the amount of drain separated in steam pipes. This is to prevent condensate that cannot be separated by the separator from continuing to flow into steam-using equipment and from causing water hammer.
く課題を解決するための手段〉
蒸気管に蒸気とドレンを分離する気水分離器を配し、該
気水分離器に分離後の蒸気とドレンを排出する蒸気出口
とドレン出口を設け、ドレン出口に連通してオリフィス
を取付け、該オリフィスの前後に圧力検出手段を設けて
差圧を検知することによりオリフイスを通過する流体量
を測定する流量測定部を設けたものである。Means for Solving the Problems> A steam separator for separating steam and condensate is arranged in the steam pipe, and the steam separator is provided with a steam outlet and a drain outlet for discharging the separated steam and condensate, and An orifice is installed in communication with the outlet, and a flow rate measuring section is provided that measures the amount of fluid passing through the orifice by providing pressure detection means before and after the orifice to detect the differential pressure.
く作用〉
ドレン出口に連通してオリフィスと圧力検出手段からな
る流量測定部を設けたことにより、気水分離器で分離ざ
れたドレン量を測定することができる。従って、蒸気管
にドレンが多量に混入している異常状態を検知すること
ができる。Effects> By providing a flow rate measurement section consisting of an orifice and pressure detection means in communication with the drain outlet, the amount of drain separated by the steam/water separator can be measured. Therefore, an abnormal state in which a large amount of condensate is mixed in the steam pipe can be detected.
く発明の効果〉
蒸気管の異常状態を検知することができ、異常状態の要
因である、キャリーオーバーやスチームトラップの排出
不良や蒸気管の保温不良を修正することにより、蒸気使
用機器にドレンが流入することを防止して蒸気使用機器
の生産性の低下を防ぐことができると共に、ウォーター
ハンマーを防止することもできる。Effects of the Invention> Abnormal conditions in steam pipes can be detected, and condensate can be prevented from flowing into steam-using equipment by correcting the causes of the abnormal conditions, such as carryover, poor steam trap discharge, and poor heat retention of steam pipes. By preventing steam from flowing in, it is possible to prevent a decrease in the productivity of steam-using equipment, and also to prevent water hammer.
また、分離したドレン量をオリフィスと圧力検出手段と
で測定するという簡単な手段により、ボイラーの運転状
態やスチームトラップの作動状態をも監視することがで
きる。In addition, the operational state of the boiler and the operational state of the steam trap can also be monitored by a simple method of measuring the amount of separated drain using an orifice and a pressure detection means.
く実施例〉
上記の技術的手段の具体例を示す実施例を説明する。〈
第1図参照〉
ボイラー1で発生した蒸気を蒸気使用機器2へ供給する
蒸気管3に気水分離器4を取付ける。気水分離器4には
、蒸気出口7とドレン出口8を設けて、蒸気出口7は蒸
気使用機器2と連通し、ドレン出口8は圧力検出手段と
しての圧力センサー5aを介してオリフィス9と連通す
る。オリフイス9の出口側にも圧力センサー5bを取付
ける。Embodiment> An embodiment illustrating a specific example of the above technical means will be described. <
See Figure 1> A steam separator 4 is attached to a steam pipe 3 that supplies steam generated in the boiler 1 to the steam-using equipment 2. The steam separator 4 is provided with a steam outlet 7 and a drain outlet 8, the steam outlet 7 communicates with the steam using equipment 2, and the drain outlet 8 communicates with an orifice 9 via a pressure sensor 5a as a pressure detection means. do. A pressure sensor 5b is also attached to the outlet side of the orifice 9.
圧力センサー5a,5bとオリフイス9で流量測定部を
構戒する。オリフイス9部に流れがあるか否かを圧力セ
ンサー5a,5bで検知すると共に、オリフィス9前後
の圧力を圧力センサー5a,5bで測定し、測定結果を
もとにオリフイス9を通過する流量を演算する演算部5
0、及び、演算結果を表示したり異常状態を警報する表
示部51を圧力センサー5a,5bと接続する。圧力セ
ンサー5a,5b、演痺部50,及び、表示部51の電
源は、気水分離器4の外周に取付けた熱発電素子10に
より供給する。すなわち、気水分離器4は高温の蒸気並
びにドレンにより満たされており、当該熱エネルギーを
電気エネルギーに変換して供給する。参照番@52は蒸
気使用機器2で発生したドレンを排出するためのスチー
ムトラップ、53は蒸気管3で発生したドレンを排出す
るためのスチームトラップである。The pressure sensors 5a and 5b and the orifice 9 monitor the flow rate measuring section. The pressure sensors 5a and 5b detect whether there is a flow in the orifice 9, and the pressure before and after the orifice 9 is measured with the pressure sensors 5a and 5b, and the flow rate passing through the orifice 9 is calculated based on the measurement results. arithmetic unit 5
0, and a display unit 51 that displays calculation results and warns of abnormal conditions is connected to the pressure sensors 5a and 5b. Power for the pressure sensors 5a, 5b, the numbing section 50, and the display section 51 is supplied by a thermoelectric generating element 10 attached to the outer periphery of the steam/water separator 4. That is, the steam/water separator 4 is filled with high-temperature steam and drain, and converts the thermal energy into electrical energy and supplies it. Reference number @52 is a steam trap for discharging condensate generated in the steam-using equipment 2, and reference number 53 is a steam trap for discharging condensate generated in the steam pipe 3.
気水分離器4は、本体11に入口12、蒸気出口7、ト
レン出口8を形戊し、入口12に連通して円筒形状の隔
壁部材20を取付け、これを囲む本体11との間に環状
空間16を形或する。八口12と環状空間16の間にコ
ーン形状のスクリーン31を配し、環状空間16の下部
は排水弁6の排水溜り室26の上部と連通する。排水溜
り室26の上部は隔壁部材20の中央開口を通して蒸気
出口7と連通する。環状空間16には傾斜壁からなる旋
回羽根24を配置する。また隔壁部材20の下部は外側
へ拡がったフレアー状の水切り部18を形或する。The steam/water separator 4 has an inlet 12, a steam outlet 7, and a train outlet 8 formed in a main body 11, a cylindrical partition member 20 is attached to communicate with the inlet 12, and an annular partition member 20 is connected to the main body 11 surrounding the main body 11. Shape the space 16. A cone-shaped screen 31 is arranged between the eight ports 12 and the annular space 16, and the lower part of the annular space 16 communicates with the upper part of the drain chamber 26 of the drain valve 6. The upper part of the drainage sump chamber 26 communicates with the steam outlet 7 through the central opening of the partition member 20. In the annular space 16, a swirling vane 24 made of an inclined wall is arranged. Further, the lower portion of the partition member 20 is formed with a flared drainage portion 18 that expands outward.
排水溜り室26の底部には排水弁6としてスチームトラ
ップを形戒する。排水溜り室26の底部にドレン出口8
に通じる排水弁口28を形成し、対向して球形の弁フロ
ート30を自由状態で収容し、フロート力バー32で覆
う。フロート力バー32の上部には通気口34を開ける
。従って八口12から流入した蒸気とドレンの混合流体
は環状空間16を通過する時に、旋回羽根24で方向を
曲げられて旋回せしめられ、水分は蒸気より質屋が大ぎ
いので外側へ振出ざれて周囲の本体内壁に沿って排水溜
り室26に流下し、軽い蒸気は隔壁部材20の中央開口
を経て蒸気出口7に流出する。A steam trap is provided at the bottom of the drain chamber 26 as a drain valve 6. A drain outlet 8 is provided at the bottom of the drain chamber 26.
A drain valve opening 28 is formed which leads to an opposing spherical valve float 30 which is freely accommodated therein and covered by a float force bar 32 . A vent hole 34 is opened in the upper part of the float force bar 32. Therefore, when the mixed fluid of steam and condensate flowing in from the eight mouths 12 passes through the annular space 16, its direction is bent by the swirling vanes 24 and the water is swirled, and the moisture is shaken out to the outside and surroundings. The light vapor flows down along the inner wall of the main body into the drainage sump chamber 26, and the light vapor flows out through the central opening of the partition member 20 to the vapor outlet 7.
弁フロート30は排水溜り室26の水位と共に浮上降下
して排水弁口28を開閉し、排水溜り室26に溜るドレ
ンを自動的にドレン出口8へ排出する。本実施例におい
ては、気水分離部とスチームトラップを一体にした気水
分離器4を示したが、スチームトラップは必ずしも必要
ではなく、要は気水分離ざれたドレンのみがドレン出口
8から排出ざれればよく、通常の二一ドル弁や玉形弁で
あってもよい。The valve float 30 floats up and down with the water level in the drain chamber 26 to open and close the drain valve port 28, and automatically discharges the drain accumulated in the drain chamber 26 to the drain outlet 8. In this embodiment, a steam/water separator 4 is shown that integrates a steam/water separating section and a steam trap, but the steam trap is not necessarily necessary, and only the drain from which the steam/water has been separated is discharged from the drain outlet 8. It may be a regular twenty-one dollar valve or a globe valve.
ボイラー1のキャリ”−オーバーにより発生した水滴や
蒸気管3での自然放熱で発生したドレンは、気水分離器
4で分離ざれ、オリフィス9に至る。Water droplets generated due to carry-over of the boiler 1 and drain generated due to natural heat radiation in the steam pipe 3 are separated by a steam/water separator 4 and reach an orifice 9.
キャリーオーバーが多くなったり、スチームトラップ5
3が排出不良を起こしドレンを排出できなくなると、オ
リフィス9へ至るドレン量も多くなり、蒸気管3の異常
を検知することができる。If there is too much carryover or steam trap 5
3 causes a discharge failure and cannot discharge the condensate, the amount of condensate reaching the orifice 9 increases, and an abnormality in the steam pipe 3 can be detected.
第1図は本発明の蒸気管の異常検出装置の概略構或図で
ある。
1:ボイラー 2:蒸気使用機器3:蒸気管
4:気水分離器5a,5b:圧カセンサーFIG. 1 is a schematic diagram of a steam pipe abnormality detection device according to the present invention. 1: Boiler 2: Steam-using equipment 3: Steam pipe
4: Steam separator 5a, 5b: Pressure sensor
Claims (1)
、該気水分離器に蒸気出口とドレン出口を設け、ドレン
出口に連通してオリフィスを取付け、該オリフィスの前
後に圧力検出手段を設けて差圧を検知することによりオ
リフィスを通過する流体量を測定する流量測定部を設け
た蒸気管の異常検出装置。1. A steam separator that separates steam and condensate is placed in the steam pipe, a steam outlet and a drain outlet are provided in the steam pipe, an orifice is installed in communication with the drain outlet, and pressure is detected before and after the orifice. An abnormality detection device for a steam pipe, which includes a flow rate measuring section that measures the amount of fluid passing through an orifice by detecting differential pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15326489A JPH0320197A (en) | 1989-06-14 | 1989-06-14 | Malfunction detector for steam pipe |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15326489A JPH0320197A (en) | 1989-06-14 | 1989-06-14 | Malfunction detector for steam pipe |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0320197A true JPH0320197A (en) | 1991-01-29 |
JPH0553999B2 JPH0553999B2 (en) | 1993-08-11 |
Family
ID=15558656
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15326489A Granted JPH0320197A (en) | 1989-06-14 | 1989-06-14 | Malfunction detector for steam pipe |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0320197A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014112000A (en) * | 2012-12-05 | 2014-06-19 | Tlv Co Ltd | Gas-liquid separator |
-
1989
- 1989-06-14 JP JP15326489A patent/JPH0320197A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014112000A (en) * | 2012-12-05 | 2014-06-19 | Tlv Co Ltd | Gas-liquid separator |
Also Published As
Publication number | Publication date |
---|---|
JPH0553999B2 (en) | 1993-08-11 |
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