JP2802457B2 - Wetness measuring device - Google Patents

Wetness measuring device

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Publication number
JP2802457B2
JP2802457B2 JP3352417A JP35241791A JP2802457B2 JP 2802457 B2 JP2802457 B2 JP 2802457B2 JP 3352417 A JP3352417 A JP 3352417A JP 35241791 A JP35241791 A JP 35241791A JP 2802457 B2 JP2802457 B2 JP 2802457B2
Authority
JP
Japan
Prior art keywords
steam
flow meter
wetness
gas
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.)
Expired - Fee Related
Application number
JP3352417A
Other languages
Japanese (ja)
Other versions
JPH05164672A (en
Inventor
ウイリアム ラットクリフ ディビッド
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 JP3352417A priority Critical patent/JP2802457B2/en
Publication of JPH05164672A publication Critical patent/JPH05164672A/en
Application granted granted Critical
Publication of JP2802457B2 publication Critical patent/JP2802457B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は気体配管を流れる蒸気等
の湿り度を測定する装置に関する。各種ボイラや蒸気動
力を利用する機器では、蒸気中の水分の含有量、即ち蒸
気流の単位体積あたりの全質量に対する乾き飽和蒸気の
占める質量の割合を示す乾き度X、あるいは湿り度(1
−X)を知る必要がある。これは水分の含有量によって
蒸気のエンタルピが異なるためである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for measuring the wetness of steam flowing through a gas pipe. In various boilers and equipment using steam power, the dryness X or the wetness (1) indicating the content of moisture in the steam, that is, the ratio of the mass occupied by the dry saturated steam to the total mass per unit volume of the steam flow.
-X). This is because the enthalpy of the steam varies depending on the water content.

【0002】[0002]

【従来の技術】従来の蒸気の湿り度測定装置としては、
絞り乾き度計がある。これは、被測定湿り蒸気をノズル
を通して温度計及び圧力計を取付けた測定容器内に噴射
して断熱膨脹させ、過熱蒸気状態にして湿り度を測定す
るものである。また他の湿り度測定装置としては、二重
管の内側管内に被測定湿り蒸気を流し、外側管内に同量
の過熱蒸気を流し、この過熱蒸気流によって湿り蒸気を
加熱して過熱蒸気化し、被測定蒸気をサンプリングして
湿り度を測定するものがある。
2. Description of the Related Art Conventional steam wetness measuring devices include:
There is a squeezing dryness meter. In this method, the wet steam to be measured is jetted through a nozzle into a measuring vessel equipped with a thermometer and a pressure gauge, and is adiabatically expanded to make a superheated steam state to measure the wetness. Further, as another wetness measuring device, the wet steam to be measured is flown into the inner pipe of the double pipe, the same amount of superheated steam is flowed into the outer pipe, and the wet steam is heated by this superheated steam flow to become superheated steam. In some cases, the measured steam is sampled to measure the degree of wetness.

【0003】[0003]

【発明が解決しようとする課題】上記前者のものでは、
測定可能な湿り蒸気の範囲が限られる問題がある。即
ち、蒸気の圧力が低い場合は、容器内で過熱蒸気状態に
するのに圧力を非常に低くする必要があり、また蒸気の
湿り度が大きい場合には、膨脹後過熱蒸気状態にならな
いためである。また上記後者のものでは、加熱源として
過熱蒸気を必要とし、被測定湿り蒸気と同量の過熱蒸気
を流すことや被測定湿り蒸気をサンプリングすることも
困難である。従って、本発明の技術的課題は、測定可能
な湿り度の範囲が広く、簡単に湿り度を測定できるよう
にすることである。
In the former case,
There is a problem that the range of wet steam that can be measured is limited. That is, when the pressure of the steam is low, the pressure needs to be extremely low to make the superheated steam state in the vessel, and when the wetness of the steam is high, the steam does not become the superheated steam state after expansion. is there. In the latter case, the superheated steam is required as a heating source, and it is difficult to flow the same amount of superheated steam as the measured wet steam or to sample the measured wet steam. Therefore, a technical problem of the present invention is to make it possible to easily measure the wetness with a wide range of measurable wetness.

【0004】[0004]

【課題を解決するための手段】上記の技術的課題を解決
するために講じた本発明の技術的手段は、気体配管に気
体中の水分を分離する気水分離器を配し、気水分離器の
排水口に水分量(W1)を測定するドレン流量計を設
け、気水分離器の気体出口に気体量(W2)を測定する
流量計を設けるか或いは気水分離器の入口に流体量(W
3)を測定する流量計を設け、前記測定したW1とW2
から或いはW1とW3から湿り度を算出する演算部を設
けたものである。
Technical means of the present invention taken in order to solve the above technical problems SUMMARY OF THE INVENTION are arranged steam separator for separating water in the gas to the gas pipe, steam-water separator Vessel
Drain flow meter for measuring water content (W1) at drain
And measure the gas amount (W2) at the gas outlet of the steam-water separator
Either a flow meter is provided or the fluid flow (W
A flow meter for measuring 3) is provided, and the measured W1 and W2 are measured.
Or a calculation unit for calculating the wetness from W1 and W3 .

【0005】[0005]

【作用】上記の技術的手段の作用は下記の通りである。
気体配管を流れる流体量を測定する流量計を気水分離器
の入口に設けた場合は、水分を含んだ気体の全流量が測
定され、気体配管を流れる流体量を測定する流量計を気
水分離器の蒸気出口に設けた場合は、気体のみの流体量
が測定される。また気水分離器で分離された水分量がド
レン流量計で測定される。水分量の全流量に対する割合
を演算部で算出することにより、湿り度を求めることが
できる。
The operation of the above technical means is as follows.
If a flow meter that measures the amount of fluid flowing through the gas pipe is provided at the inlet of the steam separator, the total flow rate of the gas containing water is measured, and the flow meter that measures the amount of fluid that flows through the gas pipe is used to measure When provided at the vapor outlet of the separator, the fluid amount of only gas is measured. The amount of water separated by the steam separator is measured by a drain flow meter. By calculating the ratio of the amount of water to the total flow rate by the calculation unit, the degree of wetness can be obtained.

【0006】[0006]

【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(図1ないし図4参照)。蒸気配管1に気水分離
器2を取付ける。気水分離器2には、蒸気出口3と排水
口4を設ける。蒸気出口3は蒸気流量計5の入口6と連
通し、排水口4はドレン流量計7の入口8と連通する。
参照番号9は演算部である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment showing a specific example of the above technical means will be described (see FIGS. 1 to 4). Attach steam separator 2 to steam pipe 1. The steam separator 2 is provided with a steam outlet 3 and a drain outlet 4. The steam outlet 3 communicates with the inlet 6 of the steam flow meter 5, and the drain port 4 communicates with the inlet 8 of the drain flow meter 7.
Reference numeral 9 is an operation unit.

【0007】気水分離器2の一例を図2に示す。ケ―シ
ング10に入口11、蒸気出口3、排水口4を形成し、
入口11に連通して円筒形状の隔壁部材12を取付け、
これを囲むケ―シング10との間に環状空間13を形成
する。環状空間13に傾斜壁からなる旋回羽根14と水
切り部材15を配置する。入口11から流入した被測定
蒸気は環状空間13を通過するときに、旋回羽根14で
方向を曲げられて旋回せしめられ、水分は蒸気より質量
が大きいので外側へ振出されて周囲のケ―シング10内
壁に沿って流下し、排水口4から流出する。軽い気体は
隔壁部材12の中央開口を経て蒸気出口3から流出す
る。尚、気水分離器としては、この旋回式に限らずあら
ゆるものを用いることができる。
FIG. 2 shows an example of the steam separator 2. An inlet 11, a steam outlet 3, and a drain 4 are formed in the casing 10,
A cylindrical partition member 12 is attached in communication with the inlet 11,
An annular space 13 is formed between the casing 10 and the casing 10 surrounding the casing. A swirl vane 14 and a drainer 15 made of an inclined wall are arranged in an annular space 13. When the vapor to be measured flowing from the inlet 11 passes through the annular space 13, its direction is deflected by the swirling vanes 14 to be swirled, and since the water has a larger mass than the steam, it is squirted outward to surround the surrounding casing 10. It flows down along the inner wall and flows out from the drain 4. Light gas flows out of the steam outlet 3 through the central opening of the partition member 12. It should be noted that the steam-water separator is not limited to this swirl type, and any type can be used.

【0008】ドレン流量計7の一例を図3に示す。ケ―
シング16に入口8と出口17を形成する。ケ―シング
16の内部にカップ形状の仕切壁部材18を配置する。
仕切壁部材18の内部及び上方は入口8に連通し、外周
及び下方は出口17に連通する。仕切壁部材18の内外
は通孔19と堰20を通して連通する。出口17にフロ
―ト弁等の自動排水弁(図示せず)を取付ける。仕切壁
部材18内に球形の中空のフロ―ト21を配置する。フ
ロ―ト21にケ―シング16を気密的に貫通した作動棒
22を連結し、作動棒22にポテンショ・メ―タ23を
連結する。フロ―ト21が液面と共に浮上降下し、これ
と共に作動棒22が同時に変位する。この作動棒22の
変位をポテンショ・メ―タ23で電気信号に変換する。
この電気信号が演算部9に送られる。演算部9はポテン
ショ・メ―タ23で検出された液位と堰20を通過する
流量との関係に基いて水分量(W1)を算出する。尚、
ドレン流量計としては、この堰式に限らずあらゆるもの
を用いることができる。
FIG. 3 shows an example of the drain flow meter 7. K
An inlet 8 and an outlet 17 are formed in the thing 16. A cup-shaped partition member 18 is arranged inside the casing 16.
The inside and the upper part of the partition wall member 18 communicate with the inlet 8, and the outer periphery and the lower part communicate with the outlet 17. The inside and outside of the partition wall member 18 communicate with each other through a through hole 19 and a weir 20. At the outlet 17, an automatic drain valve (not shown) such as a float valve is attached. A spherical hollow float 21 is arranged in the partition wall member 18. An actuating rod 22 which hermetically penetrates the casing 16 is connected to the float 21, and a potentiometer 23 is connected to the actuating rod 22. The float 21 rises and falls with the liquid level, and the operating rod 22 is simultaneously displaced. The displacement of the operating rod 22 is converted into an electric signal by a potentiometer 23.
This electric signal is sent to the arithmetic unit 9. The calculation unit 9 calculates the water content (W1) based on the relationship between the liquid level detected by the potentiometer 23 and the flow rate passing through the weir 20. still,
The drain flow meter is not limited to this weir type, and any type can be used.

【0009】蒸気流量計5の一例を図4に示す。管形状
のケ―シング24の両端に入口6と出口25を形成し、
途中にオリフィス26を開けた絞り部材27を設ける。
オリフィス26の前後に圧力センサ―28,29を設
け、演算部9に連結する。演算部9は圧力センサ―2
8,29で検出された圧力による差圧に基いて蒸気量
(W2)を算出する。尚、蒸気流量計としては、この差
圧式に限らずあらゆるものを用いることができる。
FIG. 4 shows an example of the steam flow meter 5. An inlet 6 and an outlet 25 are formed at both ends of a tubular casing 24,
A throttle member 27 having an orifice 26 opened is provided on the way.
Pressure sensors 28 and 29 are provided before and after the orifice 26, and are connected to the calculation unit 9. The calculation unit 9 is a pressure sensor-2
The steam amount (W2) is calculated based on the pressure difference due to the pressure detected in steps 8 and 29. The steam flow meter is not limited to the differential pressure type, and any type can be used.

【0010】演算部9は算出した水分量W1と蒸気量W
2に基いて、湿り度W1/(W1+W2)を算出する。
上記実施例では、気水分離器の蒸気出口に蒸気流量計を
設けたが、気水分離器の入口に流量計を設けることもで
きる。この場合は、水分を含んだ蒸気量W3を測定し、
ドレン流量計で測定した水分量W1とに基いて、湿り度
W1/W3を算出する。また気水分離器2の分離効率が
100パーセントでなく、kパーセントの場合は、水分
W1を100・W1/kに補正して湿り度を算出す
る。
The calculating unit 9 calculates the calculated water content W1 and the calculated steam content W.
2, the wetness W1 / (W1 + W2) is calculated.
In the above embodiment, the steam flow meter is provided at the steam outlet of the steam separator, but a flow meter may be provided at the inlet of the steam separator. In this case, the amount of steam W3 containing water is measured,
The wetness W1 / W3 is calculated based on the water content W1 measured by the drain flow meter. When the separation efficiency of the steam separator 2 is not 100% but k%, the moisture amount W1 is corrected to 100 · W1 / k to calculate the wetness.

【0011】[0011]

【発明の効果】本発明は下記の特有の効果を生じる。上
記のように本発明によれば、水分を含んだ気体を過熱状
態にしたり、過熱蒸気を必要としないので、測定可能な
湿り度の範囲が広くなると共に、簡単に湿り度を測定で
きる。また気体配管を流れる流量が判るので、気体配管
に連結する機器の運転効率を改善したり、気体配管の異
常を判断するデ―タが得られる。
The present invention has the following specific effects. As described above, according to the present invention, since the gas containing moisture is not overheated or superheated steam is required, the range of measurable wetness is widened and the wettability can be easily measured. In addition, since the flow rate flowing through the gas pipe is known, it is possible to improve the operation efficiency of equipment connected to the gas pipe and obtain data for judging an abnormality in the gas pipe.

【図面の簡単な説明】[Brief description of the drawings]

【図1】図1は本発明の実施例の湿り度測定装置の構成
図である。
FIG. 1 is a configuration diagram of a wetness measuring apparatus according to an embodiment of the present invention.

【図2】図2は図1の気水分離器の断面図である。FIG. 2 is a sectional view of the steam separator of FIG. 1;

【図3】図3は図1のドレン流量計の断面図である。FIG. 3 is a sectional view of the drain flow meter of FIG. 1;

【図4】図4は図1の蒸気流量計の断面図である。FIG. 4 is a sectional view of the steam flow meter of FIG. 1;

【符号の説明】 1 蒸気配管 2 気水分離器 3 蒸気出口 4 排水口 5 蒸気流量計 7 ドレン流量計 9 演算部[Explanation of Signs] 1 Steam pipe 2 Steam separator 3 Steam outlet 4 Drain port 5 Steam flow meter 7 Drain flow meter 9 Operation unit

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 気体配管に気体中の水分を分離する気水
分離器を配し、気水分離器の排水口に水分量(W1)を
測定するドレン流量計を設け、気水分離器の気体出口に
気体量(W2)を測定する流量計を設けるか或いは気水
分離器の入口に流体量(W3)を測定する流量計を設
け、前記測定したW1とW2から或いはW1とW3から
湿り度を算出する演算部を設けた湿り度測定装置。
1. A gas-water separator for separating water in a gas is provided in a gas pipe, and a water content (W1) is supplied to a drain port of the gas-water separator.
Provide a drain flow meter for measurement, at the gas outlet of the steam separator
Provide a flow meter to measure gas volume (W2)
Install a flow meter at the inlet of the separator to measure the fluid volume (W3).
A wetness measuring device provided with a calculation unit for calculating the wetness from the measured W1 and W2 or from W1 and W3 .
JP3352417A 1991-12-13 1991-12-13 Wetness measuring device Expired - Fee Related JP2802457B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3352417A JP2802457B2 (en) 1991-12-13 1991-12-13 Wetness measuring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3352417A JP2802457B2 (en) 1991-12-13 1991-12-13 Wetness measuring device

Publications (2)

Publication Number Publication Date
JPH05164672A JPH05164672A (en) 1993-06-29
JP2802457B2 true JP2802457B2 (en) 1998-09-24

Family

ID=18423938

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3352417A Expired - Fee Related JP2802457B2 (en) 1991-12-13 1991-12-13 Wetness measuring device

Country Status (1)

Country Link
JP (1) JP2802457B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6531476B2 (en) * 2015-04-07 2019-06-19 東京電力ホールディングス株式会社 Wetness measurement system and method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61246515A (en) * 1985-04-23 1986-11-01 Takuma Co Ltd Detecting method and device for water concentration of exhaust gas in incinerator

Also Published As

Publication number Publication date
JPH05164672A (en) 1993-06-29

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