JPH05296860A - Measuring apparatus for consumed calory of device using steam - Google Patents

Measuring apparatus for consumed calory of device using steam

Info

Publication number
JPH05296860A
JPH05296860A JP12265892A JP12265892A JPH05296860A JP H05296860 A JPH05296860 A JP H05296860A JP 12265892 A JP12265892 A JP 12265892A JP 12265892 A JP12265892 A JP 12265892A JP H05296860 A JPH05296860 A JP H05296860A
Authority
JP
Japan
Prior art keywords
steam
condensate
temperature
amount
heat
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
Application number
JP12265892A
Other languages
Japanese (ja)
Inventor
Yoshihiko Hasegawa
義彦 長谷川
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 JP12265892A priority Critical patent/JPH05296860A/en
Publication of JPH05296860A publication Critical patent/JPH05296860A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To measure the correct consuming calory in a device using steam even when the supplied steam is a saturated steam or a superheated steam. CONSTITUTION:A steam feed pipe 10 is connected to a device 1 using steam. The steam feed pipe 10 is provided with a steam flowmeter 3, a steam pressure sensor 8 and a steam temperature sensor 9. A condensate discharge pipe 20 is connected at the secondary side of the device 1, and a condensate flowmeter 21 and a steam trap 7 are set in the discharge pipe 20. A condensate temperature sensor 5 is mounted to the condensate flowmeter 21. The steam flowmeter 3, pressure sensor 8, temperature sensors 5, 9 and condensate flowmeter 21 are connected to an operating part 6.

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、蒸気を用いて各種加熱
や乾燥等の熱処理を行う蒸気使用機器の消費熱量測定装
置に関する。蒸気使用機器では蒸気の保有する潜熱を利
用して被熱処理物を熱処理するのであるが、供給する蒸
気の量は、省エネルギ―の観点から必要最少限であるこ
とが望ましい。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a calorie consumption measuring apparatus for steam-using equipment for performing various heat treatments such as heating and drying using steam. In equipment using steam, the latent heat of the steam is used to heat the object to be heat-treated, but the amount of steam supplied is preferably the minimum necessary from the viewpoint of energy saving.

【0002】[0002]

【従来の技術】従来の蒸気使用機器での消費熱量測定装
置としては、例えば特開昭62−246700号公報に
示されているようなものが用いられていた。これは、蒸
気使用機器から排出される復水の量を測定する復水流量
計を蒸気使用機器の出口側に取付け、この復水の温度を
検出する復水温度検出手段を取付けると共に、供給蒸気
の圧力を検出する蒸気圧力検出手段を取付けて、復水の
量と温度と蒸気の圧力から蒸気使用機器での消費熱量を
演算表示するものである。
2. Description of the Related Art As a conventional calorific value measuring device for a steam-using device, a device as disclosed in, for example, JP-A-62-246700 has been used. This is because a condensate flow meter that measures the amount of condensate discharged from steam-using equipment is installed on the outlet side of the steam-using equipment, and condensate temperature detection means that detects the temperature of this condensate is installed, and the supply steam The steam pressure detecting means for detecting the pressure is attached to calculate and display the amount of heat consumed by the steam-using device from the amount and temperature of condensed water and the pressure of steam.

【0003】[0003]

【発明が解決しようとする課題】上記従来のものでは、
供給蒸気が飽和蒸気である場合には正確に消費熱量を測
定することができるが、飽和蒸気以外の蒸気、例えば過
熱蒸気等、であれば消費熱量を正確に測定できない問題
があった。これは、供給蒸気の検出量は蒸気圧力だけで
あり、この圧力から供給蒸気を飽和蒸気であるものとし
て蒸気の保有熱量を換算しているためである。蒸気使用
機器に供給される蒸気は、通常蒸気ボイラ―で発生した
高圧の蒸気を、使用機器の仕様に応じて適宜に減圧した
ものである場合が多く、高圧蒸気を減圧すると、蒸気の
保有熱量は減少しないために過熱蒸気となりやすい。過
熱蒸気の保有熱量はその圧力と温度とにより決まり、圧
力だけでは正確な蒸気熱量を換算できないのである。
SUMMARY OF THE INVENTION In the above conventional one,
When the supply steam is saturated steam, the consumed heat amount can be accurately measured, but there is a problem that the consumed heat amount cannot be accurately measured in the case of steam other than saturated steam, for example, superheated steam. This is because the detected amount of the supply steam is only the steam pressure, and the stored heat quantity of the steam is converted from this pressure assuming that the supply steam is the saturated steam. The steam supplied to the steam-using equipment is often the high-pressure steam generated in a normal steam boiler, which is appropriately decompressed according to the specifications of the equipment used. Does not decrease, so it easily becomes superheated steam. The amount of heat of superheated steam is determined by its pressure and temperature, and it is not possible to convert the exact amount of steam heat only by the pressure.

【0004】従って本発明の技術的課題は、供給蒸気が
飽和蒸気のみならず過熱蒸気であっても蒸気使用機器で
の消費熱量が正確に測定できる蒸気使用機器の消費熱量
測定装置を得ることである。
Therefore, a technical problem of the present invention is to obtain a calorie consumption measuring apparatus for steam-using equipment capable of accurately measuring the calorie consumption of steam-using equipment even if the supply steam is not only saturated steam but also superheated steam. is there.

【0005】[0005]

【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、蒸気使用機器
に蒸気を供給する蒸気供給管を接続し、該蒸気供給管に
供給蒸気量を測定する蒸気流量検出手段を取付け、供給
蒸気の圧力と温度を検出する蒸気圧力温度検出手段を配
置し、蒸気使用機器から排出される復水の温度を検出す
る復水温度検出手段を配置して、蒸気流量検出手段と蒸
気圧力温度検出手段と復水温度検出手段からの信号によ
り蒸気使用機器での消費熱量を演算する演算部を設けた
ものである。
Means for Solving the Problems The technical means of the present invention taken to solve the above technical problem is to connect a steam supply pipe for supplying steam to a steam using device and supply the steam supply pipe to the steam supply pipe. A steam flow rate detection unit that measures the amount of steam is attached, a steam pressure temperature detection unit that detects the pressure and temperature of the supply steam is installed, and a condensate temperature detection unit that detects the temperature of the condensate discharged from the equipment using steam is installed. Arranged, a calculation unit for calculating the amount of heat consumed in the steam-using device is provided by signals from the steam flow rate detection means, the steam pressure temperature detection means, and the condensate temperature detection means.

【0006】[0006]

【作用】上記の技術的手段の作用は下記の通りである。
蒸気流量検出手段と蒸気圧力温度検出手段を配置したこ
とにより、蒸気使用機器に供給される熱量が演算され
る。すなわち、蒸気流量と圧力と温度から、供給蒸気が
飽和蒸気であってもあるいは過熱蒸気であっても、供給
熱量を演算することができる。また、復水温度検出手段
により、蒸気使用機器から排出される復水の温度が検出
され、蒸気使用機器内で消費されずに復水として排出さ
れる排出熱量が演算される。すなわち、復水は液相のみ
であり、その温度を検出することにより、復水の保有熱
量を演算することができる。従って、供給熱量から排出
熱量を減ずれば、蒸気使用機器での消費熱量を演算する
ことができる。
The operation of the above technical means is as follows.
By arranging the steam flow rate detecting means and the steam pressure temperature detecting means, the amount of heat supplied to the equipment using steam is calculated. That is, the amount of heat supplied can be calculated from the steam flow rate, pressure, and temperature regardless of whether the supplied steam is saturated steam or superheated steam. Further, the condensate temperature detecting means detects the temperature of the condensate discharged from the steam-using device, and calculates the exhaust heat amount discharged as condensate without being consumed in the steam-using device. That is, the condensate is only in the liquid phase, and the retained heat of the condensate can be calculated by detecting its temperature. Therefore, if the exhaust heat amount is subtracted from the supplied heat amount, the consumed heat amount in the steam using device can be calculated.

【0007】[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1参照)。蒸気使用機器1に蒸気を供給する
蒸気供給管10を接続し、この蒸気供給管10に順次、
蒸気流量検出手段としての蒸気流量計3と、蒸気圧力温
度検出手段としての圧力センサ―8及び温度センサ―9
を取付ける。蒸気使用機器1の二次側には、蒸気使用機
器1で生じた復水を排出する復水排出管20を接続し
て、復水流量計21と、復水の温度を検出する復水温度
検出手段としての温度センサ―5を取付けると共に、流
下してきた復水を自動的に排出するスチ―ムトラップ7
を取付ける。復水流量計21は、蒸気使用機器1内で蒸
気あるいは復水の漏洩がなければ必ずしも必要でなく、
また、スチ―ムトラップ7も蒸気使用機器1内で生じる
復水の量が一定していれば必ずしも必要ではない。蒸気
流量計3と圧力センサ―8と温度センサ―5,9及び復
水流量計21はそれぞれ演算部6と接続する。
EXAMPLE An example showing a concrete example of the above technical means will be described (see FIG. 1). A steam supply pipe 10 for supplying steam is connected to the steam using device 1, and the steam supply pipe 10 is sequentially connected to the steam supply pipe 10.
Steam flowmeter 3 as steam flow rate detecting means, and pressure sensor-8 and temperature sensor-9 as steam pressure temperature detecting means
Install. A condensate discharge pipe 20 for discharging condensate generated in the steam using device 1 is connected to the secondary side of the steam using device 1, and a condensate flow meter 21 and a condensate temperature for detecting the temperature of the condensate are connected. A steam trap 7 that attaches a temperature sensor 5 as a detecting means and automatically discharges the condensate that has flowed down.
Install. The condensate flow meter 21 is not necessarily required if there is no leakage of steam or condensate in the steam using device 1.
Further, the steam trap 7 is not always necessary if the amount of condensed water generated in the steam using device 1 is constant. The steam flow meter 3, the pressure sensor-8, the temperature sensors-5, 9 and the condensate flow meter 21 are connected to the computing unit 6, respectively.

【0008】蒸気流量計3は、従来周知のどのような型
式のものでも用いることができるが、オリフィス式やカ
ルマン渦式等の流量計が適している。同様に圧力センサ
―8や温度センサ―5,9等も従来周知のものを用いる
ことができる。また復水流量計21には超音波式や電磁
式の流量計が適している。
The steam flow meter 3 may be of any known type, but an orifice type or Karman vortex type flow meter is suitable. Similarly, as the pressure sensor-8, the temperature sensors-5, 9 and the like, conventionally known ones can be used. An ultrasonic type or electromagnetic type flowmeter is suitable for the condensate flowmeter 21.

【0009】蒸気供給管10の流量計3の一次側には供
給蒸気を減圧する減圧弁11と、蒸気供給管10内の蒸
気と復水を分離するセパレ―タ22を設けると共に、セ
パレ―タ22に分離した復水を系外に排出するスチ―ム
トラップ23を設ける。また、蒸気使用機器1には被熱
処理物を供給する供給管12を弁14を介して接続する
と共に、同じく被熱処理物を取出す取出し管13を接続
する。
On the primary side of the flow meter 3 of the steam supply pipe 10, there is provided a pressure reducing valve 11 for decompressing the supply steam, a separator 22 for separating the steam in the steam supply pipe 10 from the condensate, and a separator. A steam trap 23 for discharging the condensed water separated into 22 out of the system is provided. Further, a supply pipe 12 for supplying an object to be heat-treated is connected to the steam-using device 1 via a valve 14, and a take-out pipe 13 for taking out the object to be heat-treated is also connected.

【0010】次に作用を説明する。蒸気供給管10から
供給される蒸気によって被加熱物は潜熱加熱されて被加
熱物取出し管13から取出される。供給される蒸気の量
は蒸気流量計3で測定される。潜熱加熱により熱を奪わ
れた蒸気は復水化して蒸気使用装置1の二次側に取り付
けられた復水流量計21を経てスチ―ムトラップ7から
排出される。蒸気流量計3と圧力センサ―8及び温度セ
ンサ―9,5からのそれぞれの信号が演算部6に入力さ
れる。演算部6で、蒸気流量と蒸気圧力及び温度から蒸
気使用機器1に供給された蒸気の熱量が演算され、復水
温度から復水として排出される排出熱量が演算され、両
者の差から蒸気使用機器1での消費熱量が演算される。
この場合、復水流量計21で検出した復水量を上記復水
温度と乗じることにより更に正確に排出熱量を演算する
ことができる。
Next, the operation will be described. The object to be heated is latently heated by the steam supplied from the steam supply pipe 10 and taken out from the object to be heated take-out pipe 13. The amount of steam supplied is measured by the steam flow meter 3. The steam deprived of the heat by the latent heating is condensed to be discharged from the steam trap 7 through the condensed water flow meter 21 attached to the secondary side of the steam using apparatus 1. The respective signals from the steam flow meter 3, the pressure sensor 8 and the temperature sensors 9 and 5 are input to the arithmetic unit 6. The calculation unit 6 calculates the heat quantity of the steam supplied to the steam using apparatus 1 from the steam flow rate, the steam pressure and the temperature, calculates the discharge heat quantity discharged as condensed water from the condensate temperature, and uses the steam from the difference between the two. The heat consumption amount in the device 1 is calculated.
In this case, the exhaust heat amount can be calculated more accurately by multiplying the condensate amount detected by the condensate flow meter 21 by the condensate temperature.

【0011】[0011]

【発明の効果】上記のように本発明によれば、蒸気使用
機器に供給される蒸気が、飽和蒸気であっても過熱蒸気
であっても、蒸気使用機器で消費される熱量を正確に測
定することができる。
As described above, according to the present invention, whether the steam supplied to the steam using device is saturated steam or superheated steam, the amount of heat consumed by the steam using device is accurately measured. can do.

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

【図1】本発明の蒸気使用機器の消費熱量測定装置の実
施例の構成図である。
FIG. 1 is a configuration diagram of an embodiment of a device for measuring heat consumption of steam-using equipment according to the present invention.

【符号の説明】[Explanation of symbols]

1 蒸気使用機器 3 蒸気流量計 5 復水温度センサ― 6 演算部 8 蒸気圧力センサ― 9 蒸気温度センサ― 10 蒸気供給管 11 減圧弁 21 復水流量計 1 Steam-using equipment 3 Steam flow meter 5 Condensate temperature sensor-6 Calculation unit 8 Steam pressure sensor-9 Steam temperature sensor-10 Steam supply pipe 11 Pressure reducing valve 21 Condensate flow meter

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 蒸気使用機器に蒸気を供給する蒸気供給
管を接続し、該蒸気供給管に供給蒸気量を測定する蒸気
流量検出手段を取付け、供給蒸気の圧力と温度を検出す
る蒸気圧力温度検出手段を配置し、蒸気使用機器から排
出される復水の温度を検出する復水温度検出手段を配置
して、蒸気流量検出手段と蒸気圧力温度検出手段と復水
温度検出手段からの信号により蒸気使用機器での消費熱
量を演算する演算部を設けた蒸気使用機器の消費熱量測
定装置。
1. A steam pressure pipe for connecting a steam supply pipe for supplying steam to a device using steam, and mounting steam flow rate detecting means for measuring the amount of supplied steam on the steam supply pipe to detect the pressure and temperature of the supplied steam. A condensate temperature detecting means is arranged to detect the temperature of the condensate discharged from the equipment using steam, and a signal from the steam flow rate detecting means, the steam pressure temperature detecting means and the condensate temperature detecting means is arranged. A device for measuring the amount of heat consumed by steam-using equipment, which is equipped with a calculation unit that calculates the amount of heat consumed by equipment using steam.
JP12265892A 1992-04-15 1992-04-15 Measuring apparatus for consumed calory of device using steam Pending JPH05296860A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12265892A JPH05296860A (en) 1992-04-15 1992-04-15 Measuring apparatus for consumed calory of device using steam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12265892A JPH05296860A (en) 1992-04-15 1992-04-15 Measuring apparatus for consumed calory of device using steam

Publications (1)

Publication Number Publication Date
JPH05296860A true JPH05296860A (en) 1993-11-12

Family

ID=14841433

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12265892A Pending JPH05296860A (en) 1992-04-15 1992-04-15 Measuring apparatus for consumed calory of device using steam

Country Status (1)

Country Link
JP (1) JPH05296860A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004347081A (en) * 2003-05-26 2004-12-09 Kurita Water Ind Ltd Steam loss evaluating method, steam loss evaluation, and steam loss evaluating program
JP2006162380A (en) * 2004-12-06 2006-06-22 Takasago Thermal Eng Co Ltd Measuring method of input energy of equipment apparatus, and measuring method of steam flow rate
JP2011185478A (en) * 2010-03-05 2011-09-22 Hitachi Plant Technologies Ltd Cooling system
JP2012185100A (en) * 2011-03-07 2012-09-27 National Institute Of Advanced Industrial & Technology Method for measuring steam flow rate, and heat supply system
JP2013185914A (en) * 2012-03-07 2013-09-19 National Institute Of Advanced Industrial & Technology Method for measuring steam flow rate, and heat supply system

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5594123A (en) * 1979-01-08 1980-07-17 Babcock & Wilcox Co Heat flow meter

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5594123A (en) * 1979-01-08 1980-07-17 Babcock & Wilcox Co Heat flow meter

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004347081A (en) * 2003-05-26 2004-12-09 Kurita Water Ind Ltd Steam loss evaluating method, steam loss evaluation, and steam loss evaluating program
JP4581336B2 (en) * 2003-05-26 2010-11-17 栗田工業株式会社 Steam loss evaluation method, steam loss evaluation device
JP2006162380A (en) * 2004-12-06 2006-06-22 Takasago Thermal Eng Co Ltd Measuring method of input energy of equipment apparatus, and measuring method of steam flow rate
JP4694185B2 (en) * 2004-12-06 2011-06-08 高砂熱学工業株式会社 Method for measuring input energy of equipment and method for measuring steam flow rate
JP2011185478A (en) * 2010-03-05 2011-09-22 Hitachi Plant Technologies Ltd Cooling system
JP2012185100A (en) * 2011-03-07 2012-09-27 National Institute Of Advanced Industrial & Technology Method for measuring steam flow rate, and heat supply system
JP2013185914A (en) * 2012-03-07 2013-09-19 National Institute Of Advanced Industrial & Technology Method for measuring steam flow rate, and heat supply system

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