JP4480905B2 - Steam dryness or wetness measuring device - Google Patents

Steam dryness or wetness measuring device Download PDF

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Publication number
JP4480905B2
JP4480905B2 JP2001037837A JP2001037837A JP4480905B2 JP 4480905 B2 JP4480905 B2 JP 4480905B2 JP 2001037837 A JP2001037837 A JP 2001037837A JP 2001037837 A JP2001037837 A JP 2001037837A JP 4480905 B2 JP4480905 B2 JP 4480905B2
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Prior art keywords
steam
dryness
wetness
specific volume
dynamic pressure
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JP2002243611A (en
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正義 原田
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Tlv Co Ltd
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Tlv Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、蒸気中の水分の含有量、即ち蒸気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、所謂乾き度:Xを測定する装置に関する。乾き度がXの場合、湿り度は(1−X)で表される。各種ボイラや蒸気動力を利用する機器、乾燥設備などでは、熱管理のために蒸気の乾き度を測定する必要がある。これは蒸気中の水分の含有量によって例えば乾燥状態が変化してしまうためである。
【0002】
【従来の技術】
従来の蒸気の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乾き度を測定する絞り乾き度計がある。これは、ノズルに湿り蒸気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あるいは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。即ち、測定すべき湿り蒸気の圧力や乾き度が低い場合は、断熱膨張後に過熱蒸気状態とならないために、測定することができないのである。
【0004】
また上記従来の絞り乾き度計では、被測定蒸気を蒸気配管から取り出して、ノズルを介して測定容器に供給しなければならず、測定装置が大型化すると共に、蒸気配管外部の測定容器に供給した蒸気は系外に排出されるために蒸気損失が大きくなる問題があった。
【0005】
従って、本発明の課題は、測定可能な乾き度の範囲が広く、簡単に、且つ、蒸気配管外部へのサンプリングのための供給が不要で蒸気ロスの少ない、蒸気の乾き度又は湿り度測定装置を提供することである。
【0006】
【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、流下する蒸気の乾き度又は湿り度を測定するものにおいて、蒸気の動圧を検知するピトー管を用いた動圧検知手段と、当該動圧検知手段で検知した動圧値と、流速検出手段で検出した蒸気の流速から、動圧値=ρV2/2式、ただし、V:蒸気の流速、ρ:比重量によって、蒸気の比重量又は比容積を演算する比重量又は比容積演算手段と、当該蒸気の比重量又は比容積と、乾き度又は湿り度との関係式、すなわち、ρ=X/v〃+(1−X)/v´式、ただし、X:蒸気の乾き度、v〃:飽和蒸気の比容積、v´:飽和水の比容積、に基づいて蒸気の乾き度又は湿り度を算出する演算制御部とを具備することを特徴とする蒸気の乾き度又は湿り度測定装置にある。
【0010】
【発明の実施の形態】
動圧検知手段で流下する蒸気の動圧を検知して、この検知した動圧値と蒸気の流速から、比重量又は比容積演算手段で、動圧値=ρV2/2式により、比重量又は比容積を演算することができる。ここで、ρは蒸気の比重量で、Vは蒸気の流速であり、比容積:vはρの逆数として求めることができる。
【0011】
蒸気の比重量又は比容積と、蒸気の乾き度又は湿り度との間には、所定の定義式で表される関係式があり、比重量又は比容積演算手段で演算した値と、この関係式から、蒸気の乾き度又は湿り度を算出することができる。
【0012】
被測定蒸気の流速が不明確な場合は、請求項2に示すように、流速検出手段で蒸気の流速を検出して、検出した流速値を前記比重量又は比容積演算手段に供給して演算することができる。
【0013】
トー管に静圧管を備えた二重管とすることにより、ピトー管で総圧と静圧の差としての動圧と、静圧の両方を検知することができる。
【0014】
【実施例】
本実施例においては動圧検知手段としてピトー管1を用いた例を示す。図1において、被測定蒸気が左側から右側へ流下する蒸気配管2のほぼ中心部に、ピトー管1の端部開口3配置して、上方の圧力変換器4と連通する。本実施例のピトー管1は、流体の総圧を検出することのできる一重管のものを使用する。
【0015】
端部開口3の上方には、被測定蒸気の静圧を検出する静圧検知手段としての圧力センサ5を取り付ける。ピトー管1で検出した総圧から圧力センサ5で検知した静圧を減じることにより、被測定蒸気の動圧を求めることができる。尚、ピトー管1に静圧管を備えて静圧を検知することのできる二重管方式のものを用いる場合、圧力センサ5は必ずしも取り付ける必要はない。また、被測定蒸気の静圧が既知の場合も、圧力センサ5は必ずしも取り付ける必要はない。
【0016】
圧力センサ5の更に上流側には、蒸気配管2内を通過する被測定蒸気の流速を検出する流速検出手段としての流速センサ6を取り付ける。流速センサ6は、内部を図示しないセンサ部6と流速変換器7とで構成する。尚、流速センサ6は、通過蒸気の流速が既知の場合は必ずしも取り付ける必要はない。
【0017】
ピトー管1の圧力変換器4と、圧力センサ5、及び、流速変換器7は、図示しない演算制御部と電気接続する。
【0018】
蒸気の乾き度:X又は湿り度:(1−X)を測定するには、まず、ピトー管1で被測定蒸気の総圧を検知し、この総圧と静圧の差としての動圧値と、蒸気の流速:Vとから、比重量又は比容積演算手段で、動圧値=ρV2/2式によって、蒸気の比重量又は比容積を演算する。尚、比容積:vは、比重量:ρの逆数として求まる。
【0019】
蒸気の比重量又は比容積と、蒸気の乾き度又は湿り度との間には、所定の関係式が存在する。即ち、ρ=X/v〃+(1−X)/v´式が成り立つ。ここで、ρは蒸気の比重量、Xは蒸気の乾き度、v〃は飽和蒸気の比容積、v´は飽和水の比容積である。v〃とv´は、被測定蒸気の静圧が判れば蒸気表から一義的に求めることができる。従って、圧力センサ5で蒸気配管2内の静圧を測定すると共に、予め記憶しておいた蒸気表の各圧力ごとの、飽和蒸気の比容積と飽和水の比容積から、v〃とv´を求めることができる。
【0020】
上記の式、ρ=X/v〃+(1−X)/v´において、ρとv〃とv´が求まることによって、被測定蒸気の乾き度:Xを求めることができ、同じく、湿り度:(1−X)を求めることができる。
【0022】
本実施例における流速センサ6としては、電磁式や超音波式、渦式、熱式、タービン式、あるいは、レーザードップラー式等従来公知のものを使用することができるものである。
【0023】
本実施例においては、蒸気配管2や流速センサ6、あるいは、ピトー管1等の保温に関して記載していないが、実施することが常識として省略した。
【0024】
また本実施例においては、流速センサ6の下流側に直接にピトー管1を配置した例を示したが、ピトー管1の上流側に多層多列状の整流器を配置することによって、ピトー管1に至る被測定蒸気の流れを整流して、ピトー管1でより正確に総圧と静圧の差としての動圧を検知することができる。
【0025】
また本実施例においては、ピトー管1として1つの端部開口3を有する例を示したが、特に蒸気配管2の径が大きい場合には、総圧を受ける複数の孔と静圧を受ける複数の孔をそれぞれ設けた所謂平均化ピトー管を用いることにより、被測定蒸気の動圧をより正確に検知することができる。
【0026】
本実施例においては、流速センサ6と圧力センサ5とピトー管1を、それぞれ別個に蒸気配管2に取り付けた例を示したが、これらをセンシング・ユニットとして一体化することにより、既設の蒸気配管の一部を変更することによって、この蒸気乾き度/湿り度測定装置ユニットを簡単に取り付けたり、あるいは、取り外したりすることができる。
【0027】
【発明の効果】
上記のように本発明によれば、被測定蒸気の動圧と流速から比重量又は比容積を演算して、この比重量又は比容積と、蒸気の乾き度又は湿り度との関係式から乾き度又は湿り度を算出することによって、蒸気を過熱状態にすることなく乾き度又は湿り度を測定できるので、測定可能範囲が限られることが無くなると共に、簡単に且つ蒸気ロス無く、蒸気の乾き度又は湿り度を測定することができる。
【図面の簡単な説明】
【図1】本発明による蒸気の乾き度又は湿り度測定装置の一部断面構成図。
【符号の説明】
1 ピトー管
2 蒸気配管
3 端部開口
4 圧力変換器
5 圧力センサ
6 流速センサ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for measuring so-called dryness: X, which indicates the moisture content in steam, that is, the ratio of the mass of dry saturated steam to the total mass per unit volume of steam. When the dryness is X, the wetness is represented by (1-X). In various boilers, equipment using steam power, drying equipment, etc., it is necessary to measure the dryness of steam for heat management. This is because, for example, the dry state changes depending on the moisture content in the steam.
[0002]
[Prior art]
As a conventional steam dryness measuring device, there is a squeeze dryness meter that measures dryness by utilizing the isoenthalpy change of steam. This is done by injecting wet steam through the nozzle into the measuring vessel and adiabatic expansion (change in enthalpy) to form superheated steam. The dryness is measured using a figure, a saturated steam table or 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 the dryness of the wet steam to be measured is low, the superheated steam state is not obtained after the adiabatic expansion, and therefore it cannot be measured.
[0004]
Moreover, in the above conventional dryness meter, the steam to be measured must be taken out from the steam pipe and supplied to the measuring container through the nozzle, and the measuring apparatus is enlarged and supplied to the measuring container outside the steam pipe. Since the steam was discharged out of the system, there was a problem that the steam loss increased.
[0005]
Accordingly, an object of the present invention is to provide an apparatus for measuring the dryness or wetness of steam, which has a wide range of dryness that can be measured, is simple, does not require supply for sampling outside the steam pipe, and has low steam loss. Is to provide.
[0006]
[Means for Solving the Problems]
The means of the present invention taken in order to solve the above problems is to measure the dryness or wetness of the flowing steam, and the dynamic pressure detecting means using a Pitot tube for detecting the dynamic pressure of the steam, and the dynamic pressure value detected by the dynamic pressure detection means, the flow rate of steam detected by the flow rate detecting means, the dynamic pressure value = pV 2/2 equation, however, V: flow velocity of the vapor, [rho: the specific weight, the ratio of steam Relational expression between specific weight or specific volume calculating means for calculating weight or specific volume, specific weight or specific volume of the steam and dryness or wetness, that is, ρ = X / v〃 + (1−X) / V ′ formula, where X is the degree of dryness of steam, v 〃 is the specific volume of saturated steam, and v ′ is the specific volume of saturated water, and the calculation control unit calculates the dryness or wetness of the steam. It exists in the dryness or wetness measuring apparatus of the vapor | steam characterized by comprising.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
The dynamic pressure of the steam flowing down is detected by the dynamic pressure detecting means, and the specific weight or specific volume calculating means is used to calculate the specific weight or specific volume from the detected dynamic pressure value and the flow velocity of the steam according to the dynamic pressure value = ρV2 / 2. The specific volume can be calculated. Here, ρ is the specific weight of the steam, V is the flow velocity of the steam, and the specific volume: v can be obtained as the reciprocal of ρ.
[0011]
Between the specific weight or specific volume of steam and the dryness or wetness of steam, there is a relational expression expressed by a predetermined definition formula, and this relation with the value calculated by the specific weight or specific volume calculating means. From the equation, the dryness or wetness of the steam can be calculated.
[0012]
When the flow velocity of the steam to be measured is unclear, as shown in claim 2, the flow velocity detection means detects the flow velocity of the steam and supplies the detected flow velocity value to the specific weight or specific volume calculation means. can do.
[0013]
By a double tube with a static tube to pin toe tube, it can detect the dynamic pressure as the difference between total pressure and static pressure in the Pitot tube, both static.
[0014]
【Example】
In the present embodiment, an example in which the Pitot tube 1 is used as the dynamic pressure detection means is shown. In FIG. 1, the end opening 3 of the pitot tube 1 is disposed at substantially the center of the steam pipe 2 where the steam to be measured flows from the left side to the right side, and communicates with the upper pressure transducer 4. The pitot tube 1 of the present embodiment uses a single tube that can detect the total pressure of the fluid.
[0015]
Above the end opening 3, a pressure sensor 5 as a static pressure detecting means for detecting the static pressure of the steam to be measured is attached. By subtracting the static pressure detected by the pressure sensor 5 from the total pressure detected by the Pitot tube 1, the dynamic pressure of the steam to be measured can be obtained. In addition, when using the thing of the double pipe | tube system which equips the pitot tube 1 with a static pressure tube and can detect a static pressure, the pressure sensor 5 does not necessarily need to be attached. Further, even when the static pressure of the vapor to be measured is known, the pressure sensor 5 does not necessarily have to be attached.
[0016]
On the further upstream side of the pressure sensor 5, a flow velocity sensor 6 is attached as a flow velocity detection means for detecting the flow velocity of the steam to be measured passing through the steam pipe 2. The flow rate sensor 6 is configured by a sensor unit 6 and a flow rate converter 7 (not shown). Note that the flow rate sensor 6 is not necessarily attached when the flow rate of the passing steam is known.
[0017]
The pressure converter 4, the pressure sensor 5, and the flow rate converter 7 of the pitot tube 1 are electrically connected to an arithmetic control unit (not shown).
[0018]
In order to measure the dryness of steam: X or the wetness: (1-X), first, the total pressure of the steam to be measured is detected by the Pitot tube 1, and the dynamic pressure value as the difference between the total pressure and the static pressure. From the steam flow velocity V, the specific weight or specific volume calculating means calculates the specific pressure or specific volume of the steam according to the dynamic pressure value = ρV 2/2. The specific volume: v is obtained as the reciprocal of the specific weight: ρ.
[0019]
There is a predetermined relationship between the specific weight or specific volume of the steam and the dryness or wetness of the steam. That is, ρ = X / v〃 + (1−X) / v ′ is established. Here, ρ is the specific weight of steam, X is the dryness of steam, v 蒸 気 is the specific volume of saturated steam, and v ′ is the specific volume of saturated water. v〃 and v ′ can be uniquely determined from the steam table if the static pressure of the steam to be measured is known. Accordingly, the static pressure in the steam pipe 2 is measured by the pressure sensor 5, and v〃 and v ′ are calculated from the specific volume of saturated steam and the specific volume of saturated water for each pressure in the steam table stored in advance. Can be requested.
[0020]
In the above equation, ρ = X / v〃 + (1−X) / v ′, ρ, v〃, and v ′ can be obtained, whereby the dryness of the steam to be measured: X can be obtained. Degree: (1-X) can be obtained.
[0022]
As the flow rate sensor 6 in the present embodiment, a conventionally known sensor such as an electromagnetic type, an ultrasonic type, a vortex type, a thermal type, a turbine type, or a laser Doppler type can be used.
[0023]
In the present embodiment, the heat insulation of the steam pipe 2, the flow velocity sensor 6, the pitot pipe 1, etc. is not described, but the implementation is omitted as common sense.
[0024]
In the present embodiment, an example is shown in which the Pitot tube 1 is arranged directly on the downstream side of the flow velocity sensor 6, but by arranging a multilayer multi-row rectifier on the upstream side of the Pitot tube 1, the Pitot tube 1 is arranged. The pitot tube 1 can rectify the flow of the steam to be measured, and the dynamic pressure as the difference between the total pressure and the static pressure can be detected more accurately.
[0025]
Further, in this embodiment, an example having one end opening 3 as the Pitot tube 1 has been shown. However, particularly when the diameter of the steam pipe 2 is large, a plurality of holes receiving the total pressure and a plurality of receiving the static pressure. By using so-called averaged Pitot tubes provided with respective holes, the dynamic pressure of the steam to be measured can be detected more accurately.
[0026]
In the present embodiment, the flow velocity sensor 6, the pressure sensor 5, and the Pitot tube 1 are separately attached to the steam pipe 2. However, by integrating these as a sensing unit, an existing steam pipe is provided. This vapor dryness / wetness measuring device unit can be easily attached or detached by changing a part of the above.
[0027]
【The invention's effect】
As described above, according to the present invention, the specific weight or specific volume is calculated from the dynamic pressure and flow velocity of the steam to be measured, and the dryness is calculated from the relational expression between the specific weight or specific volume and the dryness or wetness of the steam. By calculating the degree or wetness, it is possible to measure the dryness or wetness without making the steam overheated. Alternatively, the wetness can be measured.
[Brief description of the drawings]
FIG. 1 is a partial cross-sectional configuration diagram of a vapor dryness or wetness measuring apparatus according to the present invention.
[Explanation of symbols]
1 Pitot pipe 2 Steam pipe 3 End opening 4 Pressure transducer 5 Pressure sensor 6 Flow rate sensor

Claims (1)

流下する蒸気の乾き度又は湿り度を測定するものにおいて、蒸気の動圧を検知するピトー管を用いた動圧検知手段と、当該動圧検知手段で検知した動圧値と、流速検出手段で検出した蒸気の流速から、動圧値=ρV2/2式、ただし、V:蒸気の流速、ρ:比重量によって、蒸気の比重量又は比容積を演算する比重量又は比容積演算手段と、当該蒸気の比重量又は比容積と、乾き度又は湿り度との関係式、すなわち、ρ=X/v〃+(1−X)/v´式、ただし、X:蒸気の乾き度、v〃:飽和蒸気の比容積、v´:飽和水の比容積、に基づいて蒸気の乾き度又は湿り度を算出する演算制御部とを具備することを特徴とする蒸気の乾き度又は湿り度測定装置。For measuring the dryness or wetness of the flowing steam, the dynamic pressure detecting means using a Pitot tube for detecting the dynamic pressure of the steam, the dynamic pressure value detected by the dynamic pressure detecting means, and the flow velocity detecting means from the flow rate of the detected steam dynamic pressure value = pV 2/2 equation, however, V: flow velocity of the vapor, [rho: the specific weight, a specific weight or specific volume calculation means for calculating a specific weight or specific volume of the steam, Relational expression between specific weight or specific volume of steam and dryness or wetness, that is, ρ = X / v〃 + (1-X) / v ′ formula, where X: dryness of steam, v〃 An apparatus for calculating the dryness or wetness of the steam based on the specific volume of saturated steam, v ′: the specific volume of saturated water, and a dryness or wetness measuring apparatus for steam .
JP2001037837A 2001-02-15 2001-02-15 Steam dryness or wetness measuring device Expired - Lifetime JP4480905B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS629253A (en) * 1985-07-05 1987-01-17 Sumitomo Metal Ind Ltd Measuring method for dryness of wet steam
JP2001027595A (en) * 1999-07-15 2001-01-30 Tlv Co Ltd Steam dryness measuring apparatus
JP2001033333A (en) * 1999-07-16 2001-02-09 Tokyo Gas Co Ltd Pressure measuring instrument
JP2002243612A (en) * 2001-02-15 2002-08-28 Tlv Co Ltd Control device for vapor dryness or wetness

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS629253A (en) * 1985-07-05 1987-01-17 Sumitomo Metal Ind Ltd Measuring method for dryness of wet steam
JP2001027595A (en) * 1999-07-15 2001-01-30 Tlv Co Ltd Steam dryness measuring apparatus
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JP2002243612A (en) * 2001-02-15 2002-08-28 Tlv Co Ltd Control device for vapor dryness or wetness

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