JP3878344B2 - Fluid dryness measuring device - Google Patents
Fluid dryness measuring device Download PDFInfo
- Publication number
- JP3878344B2 JP3878344B2 JP32273898A JP32273898A JP3878344B2 JP 3878344 B2 JP3878344 B2 JP 3878344B2 JP 32273898 A JP32273898 A JP 32273898A JP 32273898 A JP32273898 A JP 32273898A JP 3878344 B2 JP3878344 B2 JP 3878344B2
- Authority
- JP
- Japan
- Prior art keywords
- dryness
- fluid
- steam
- measurement container
- ultrasonic
- 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
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Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N2291/00—Indexing codes associated with group G01N29/00
- G01N2291/02—Indexing codes associated with the analysed material
- G01N2291/028—Material parameters
- G01N2291/02845—Humidity, wetness
Landscapes
- Investigating Or Analyzing Materials By The Use Of Ultrasonic Waves (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、蒸気、冷媒などの気液が混合した流体の乾き度を測定する装置に関する。例えば、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当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。また、冷凍機、空気調和機などの冷凍機器においても、同様に冷媒の乾き度を知る必要がある。
【0002】
【従来の技術】
従来の流体乾き度測定装置としては、蒸気の等エンタルピ変化を利用して蒸気の乾き度を測定する絞り乾き度計がある。これは、湿り蒸気をノズルを通して測定容器内に噴射して断熱膨脹(等エンタルピ変化)させて過熱蒸気とし、ノズルの上流側の圧力と測定容器内の圧力及び温度を検出することにより、モリエール線図あるいは飽和蒸気表及び過熱蒸気表を用いて乾き度を測定するものである。
【0003】
【発明が解決しようとする課題】
上記従来の絞り乾き度計では、測定可能な蒸気圧力および乾き度の範囲が限られ、一部の湿り蒸気しか測定できない問題があった。すなわち、測定すべき湿り蒸気の圧力や乾き度が低い場合は、断熱膨張後過熱蒸気状態にならないためである。従って、本発明の技術的課題は、測定可能な乾き度の範囲が広く、簡単に乾き度を測定できる流体乾き度測定装置を提供することである。
【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、流体を充填する測定容器と、該測定容器に相対して取付けた超音波送波器及び超音波受波器と、該測定容器に取付けた圧力検出手段と、流体中を通る超音波の伝搬時間から音速を算出し該音速と圧力検出手段で検出された圧力信号から流体の乾き度を算出して出力する演算制御器とを具備することを特徴とする流体乾き度測定装置にある。
【0005】
【発明の実施の形態】
測定すべき流体を測定容器に充填し、測定容器に取付けた超音波送波器から超音波パルスを送信して相対する超音波受波器に受信させる。流体中を通る超音波の伝搬時間Tは、超音波送波器と超音波受波器間の距離をL、流体中の音速をCとすると、T=L/Cであるので、これより、流体中の音速を求めることができる。また、流体中の音速は流体の乾き度によって変化し、乾き度が低いほど音速は大きくなると言う関係がある。したがって、この音速と乾き度の関係に基づいて、上記の算出した音速から流体の乾き度を算出することができる。
【0006】
このように、本発明は、超音波の伝搬時間から流体の乾き度を算出するものであるので、流体を過熱蒸気状態にする必要がない。そのため、測定可能な乾き度の範囲が広く、簡単に乾き度を測定することができる。
【0007】
【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と図2参照)。本実施例は、蒸気乾き度測定装置に適用したものである。蒸気が流動する蒸気配管1の途中にバイパス管路2を設け、バイパス管路2に測定容器3と該測定容器3の下流に開閉弁4を介在させる。測定容器3に超音波送波器5と該超音波送波器5に相対して超音波受波器6を取付ける。超音波送波器5に発振器7を接続し、超音波受波器6に受信器8を接続し、発振器7および受信器8を演算制御器9に接続する。また、測定容器3に圧力検出手段10を取付け、演算制御器9に接続する。
【0008】
次に、この装置による蒸気乾き度の測定について説明する。先ず、開閉弁4を開けて蒸気配管1を流動する蒸気の一部をバイパス管路2内へ流入させる。そして、各部が充分に熱せられた後、開閉弁4を閉じて測定容器3内に蒸気を充填させる。続いて、演算制御器9は、発振器7にトリガー信号を供給して発振器7を発振させることにより、超音波送波器5に発振出力を供給して超音波パルスを送信させ、この超音波パルスを超音波受波器6に受信させる。超音波受波器6の受信信号は受信器8から演算制御器9に供給される。また、圧力検出手段10の検出信号は演算制御器9に供給される。
【0009】
演算制御器9は、超音波送波器5から超音波送受波器6への超音波の伝搬時間から蒸気中の音速を算出し、この算出した音速と圧力検出手段10で検出された圧力信号から蒸気の乾き度を算出して出力する。ここで、蒸気中の音速と蒸気の乾き度は、図2に示すように相関関係があり、音速が大きくなるほど乾き度は低くなると言う関係があり、また同一の音速であっても蒸気圧力が高いほど(P1>P2>P3)乾き度は高くなると言う関係がある。したがって、算出した音速と検出された圧力から蒸気の乾き度を算出することができる。
【0010】
【発明の効果】
上記のように本発明によれば、流体中の超音波の伝搬時間から流体の乾き度を算出することにより、流体を過熱状態にせずに乾き度を測定できるので、測定可能な乾き度の範囲が広くなると共に、簡単に乾き度を測定できると言う優れた効果を生じる。
【図面の簡単な説明】
【図1】本発明による蒸気乾き度測定装置の概略構成を示す図である。
【図2】本発明による蒸気乾き度測定装置で用いる各圧力ごとの流体中の音速と流体の乾き度の関係を示す図である。
【符号の説明】
1 蒸気配管
2 バイパス管路
3 測定容器
5 超音波送波器
6 超音波受波器
7 発振器
8 受信器
9 演算制御器
10 圧力検出手段[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for measuring the dryness of a fluid mixed with gas and liquid such as steam and refrigerant. For example, in various boilers and devices using steam power, it is necessary to know the dryness indicating the moisture content in steam, that is, the ratio of the mass of dry saturated steam to the total mass per unit volume of the steam flow. This is because the enthalpy of the steam varies depending on the moisture content. Similarly, it is necessary to know the dryness of the refrigerant in refrigeration equipment such as a refrigerator and an air conditioner.
[0002]
[Prior art]
As a conventional fluid dryness measuring apparatus, there is a squeeze dryness meter that measures the dryness of steam by utilizing the change in the isoenthalpy of steam. This is achieved by injecting wet steam into the measurement container through the nozzle and adiabatic expansion (isenthalpy change) to form superheated steam, and detecting the pressure upstream from the nozzle and the pressure and temperature in the measurement container. The dryness is measured using a figure or a saturated steam table and a superheated steam table.
[0003]
[Problems to be solved by the invention]
The above-mentioned conventional dryness meter has a problem that only a part of wet steam can be measured because the range of measurable vapor pressure and dryness is limited. That is, when the pressure or dryness of the wet steam to be measured is low, the superheated steam state is not obtained after adiabatic expansion. Therefore, the technical problem of the present invention is to provide a fluid dryness measuring device that has a wide range of dryness that can be measured and can easily measure dryness.
[0004]
[Means for Solving the Problems]
The technical means of the present invention taken in order to solve the above technical problem includes a measurement container filled with fluid, an ultrasonic transmitter and an ultrasonic receiver attached to the measurement container, Calculation control for calculating the sound speed from the pressure detection means attached to the measurement container and the propagation time of the ultrasonic wave passing through the fluid, and calculating and outputting the dryness of the fluid from the sound speed and the pressure signal detected by the pressure detection means A fluid dryness measuring apparatus, comprising:
[0005]
DETAILED DESCRIPTION OF THE INVENTION
A fluid to be measured is filled in a measurement container, and an ultrasonic pulse is transmitted from an ultrasonic transmitter attached to the measurement container and received by an opposing ultrasonic receiver. The propagation time T of the ultrasonic wave passing through the fluid is T = L / C, where L is the distance between the ultrasonic transmitter and the ultrasonic receiver, and C is the speed of sound in the fluid. The speed of sound in the fluid can be determined. In addition, there is a relationship that the speed of sound in the fluid changes depending on the dryness of the fluid, and the lower the dryness, the higher the speed of sound. Therefore, based on the relationship between the sound speed and the dryness, the dryness of the fluid can be calculated from the calculated sound speed.
[0006]
As described above, according to the present invention, the dryness of the fluid is calculated from the propagation time of the ultrasonic wave, and therefore it is not necessary to put the fluid in a superheated steam state. Therefore, the range of dryness that can be measured is wide, and the dryness can be easily measured.
[0007]
【Example】
An embodiment showing a specific example of the above technical means will be described (see FIGS. 1 and 2). This embodiment is applied to a vapor dryness measuring apparatus. A
[0008]
Next, the measurement of the vapor dryness by this apparatus will be described. First, the on-off
[0009]
The
[0010]
【The invention's effect】
As described above, according to the present invention, the dryness of the fluid can be measured without making the fluid overheated by calculating the dryness of the fluid from the propagation time of the ultrasonic wave in the fluid. As a result, an excellent effect is obtained that the dryness can be easily measured.
[Brief description of the drawings]
FIG. 1 is a diagram showing a schematic configuration of a vapor dryness measuring apparatus according to the present invention.
FIG. 2 is a diagram showing the relationship between the speed of sound in the fluid and the degree of dryness of the fluid for each pressure used in the vapor dryness measuring apparatus according to the present invention.
[Explanation of symbols]
DESCRIPTION OF
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32273898A JP3878344B2 (en) | 1998-11-13 | 1998-11-13 | Fluid dryness measuring device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32273898A JP3878344B2 (en) | 1998-11-13 | 1998-11-13 | Fluid dryness measuring device |
Publications (2)
Publication Number | Publication Date |
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JP2000146930A JP2000146930A (en) | 2000-05-26 |
JP3878344B2 true JP3878344B2 (en) | 2007-02-07 |
Family
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JP32273898A Expired - Fee Related JP3878344B2 (en) | 1998-11-13 | 1998-11-13 | Fluid dryness measuring device |
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JP (1) | JP3878344B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104132671B (en) * | 2014-08-13 | 2016-06-01 | 南通流量仪表厂有限公司 | Travelling speed is the passage control speed device of the steam of velocity of sound |
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1998
- 1998-11-13 JP JP32273898A patent/JP3878344B2/en not_active Expired - Fee Related
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JP2000146930A (en) | 2000-05-26 |
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