JPH0674880B2 - Operation management device for equipment using steam - Google Patents

Operation management device for equipment using steam

Info

Publication number
JPH0674880B2
JPH0674880B2 JP61087431A JP8743186A JPH0674880B2 JP H0674880 B2 JPH0674880 B2 JP H0674880B2 JP 61087431 A JP61087431 A JP 61087431A JP 8743186 A JP8743186 A JP 8743186A JP H0674880 B2 JPH0674880 B2 JP H0674880B2
Authority
JP
Japan
Prior art keywords
steam
pressure
condensate
consumption
temperature
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
JP61087431A
Other languages
Japanese (ja)
Other versions
JPS62246700A (en
Inventor
義彦 長谷川
米村  政雄
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 JP61087431A priority Critical patent/JPH0674880B2/en
Publication of JPS62246700A publication Critical patent/JPS62246700A/en
Publication of JPH0674880B2 publication Critical patent/JPH0674880B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、蒸気使用機器がより少ない蒸気の消費でより
高品質で多くの生産をできるようにする蒸気使用機器の
運転管理装置に関する。
Description: TECHNICAL FIELD The present invention relates to an operation management apparatus for steam-using equipment, which enables the steam-using equipment to produce more products with higher quality while consuming less steam.

ボイラで作った蒸気は複数の蒸気使用機器に送られ、加
熱、蒸気、保温、冷却等の熱源として使用され、製品を
生産している。
The steam produced by the boiler is sent to multiple steam-using devices and used as a heat source for heating, steam, heat retention, cooling, etc. to produce products.

ボイラの蒸発量(蒸気の消費量)を把握することは、蒸
気(燃料)の消費量を最小にし、単位時間に於ける生産
を最大にし、より高い品質の製品を生産するという、省
エネルギー、生産性および品質向上のために重要であ
る。
Understanding the boiler evaporation (steam consumption) minimizes steam (fuel) consumption, maximizes production per unit of time, and produces higher quality products. It is important for improving quality and quality.

従来の技術 従来から、ボイラの蒸発量は、ボイラに設置された給水
メータの値からボイラの缶水ブロー分を除いて求めた
り、ボイラを運転するために使われた燃料消費量からボ
イラ効率を考慮して把握していた。
Conventional technology Conventionally, the evaporation amount of a boiler is obtained by excluding the boiler can water blow from the value of the water supply meter installed in the boiler, and the boiler efficiency is calculated from the fuel consumption used to operate the boiler. I was aware of it.

また、流量計を設置して蒸気消費量を測定するようにし
ていた。これを第2図を参照して説明する。
Also, a flow meter was installed to measure steam consumption. This will be described with reference to FIG.

ボイラ31で作った蒸気は蒸気主管32から分岐した蒸気導
入管33・34を通して、蒸気使用機器35・36に送られる。
蒸気使用機器35・36で加熱等の仕事をした蒸気は復水と
なって、スチームトラップ37・38で排除される。
The steam produced in the boiler 31 is sent to the steam-using devices 35 and 36 through the steam introducing pipes 33 and 34 branched from the steam main pipe 32.
Steam that has been used for heating or other work in the steam-using devices 35 and 36 becomes condensed water and is removed by the steam traps 37 and 38.

蒸気導入管33・34には蒸気使用機器35・36に供給する蒸
気を所望の圧力に減圧する減圧弁39・40と蒸気の供給を
制御する弁41・42を配置する。
In the steam introducing pipes 33, 34, pressure reducing valves 39, 40 for reducing the pressure of the steam supplied to the steam using devices 35, 36 to a desired pressure and valves 41, 42 for controlling the supply of the steam are arranged.

蒸気主管32に蒸気流量計43を配置して、蒸気主管32を流
れる蒸気量を測定し、蒸気消費量を把握する。
A steam flow meter 43 is arranged in the steam main pipe 32, the amount of steam flowing through the steam main pipe 32 is measured, and the steam consumption amount is grasped.

本発明が解決しようとする問題点 しかしながら、ボイラの蒸発量(蒸気の消費量)を求め
るだけでは、個々の蒸気使用機器でどれだけ蒸気を消費
したかが解らないので、蒸気消費量と生産性および品質
の関連が解らない。
Problems to be Solved by the Present Invention However, since it is not possible to know how much steam is consumed in each steam-using device, only by obtaining the evaporation amount (steam consumption amount) of the boiler, the steam consumption amount and the productivity can be improved. And the relation of quality is not understood.

本発明の技術的課題は、従って、蒸気使用機器毎の蒸気
消費量と生産性および品質との関連に於いて、蒸気使用
機器の運転を管理できるようにすることである。
The technical problem of the present invention is therefore to make it possible to manage the operation of steam-using equipment in relation to the steam consumption and productivity and quality of each steam-using equipment.

問題点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、蒸気使用機器毎に蒸気消費量を測定表示する
流量計を配置し、蒸気使用機器毎に蒸気圧力と復水温度
および生産物の温度を測定表示する手段を設け、蒸気使
用機器毎の蒸気消費量と蒸気圧力および復水温度から蒸
気使用機器毎の消費熱量を演算表示する手段を設けると
共に、各々の蒸気使用機器に供給する蒸気を調節する制
御弁の開閉を蒸気使用機器毎の上記測定値によって制御
するようにした、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 dispose a flow meter for measuring and displaying the steam consumption amount for each steam using device, and for each steam using device. Is equipped with means for measuring and displaying steam pressure, condensate temperature and product temperature, and means for calculating and displaying steam consumption for each steam using device and steam pressure and condensing water for each steam using device At the same time, the opening and closing of the control valve for adjusting the steam supplied to each steam using device is controlled by the above measured value for each steam using device.

作用 上記の技術的手段の作用は下記の通りである。Action The action of the above technical means is as follows.

流量計を蒸気使用機器毎に取り付けているので、蒸気使
用機器毎の蒸気消費量を測定できる。生産性は別途単位
時間当たりでデータ取りできる。また、生産物の温度を
測定したり、蒸気圧力と復水温度を測定するので、蒸気
消費量と蒸気圧力および復水温度から蒸気使用機器毎の
消費熱量を測定でき、製品の品質を管理するデータが得
られる。
Since a flow meter is attached to each steam-using device, the steam consumption of each steam-using device can be measured. Data can be collected separately for productivity per unit time. Moreover, since the temperature of the product is measured and the steam pressure and the condensate temperature are measured, it is possible to measure the calorie consumption of each steam-using device from the steam consumption amount, the steam pressure and the condensate temperature, and control the quality of the product Data is obtained.

従って、これらのデータに基づいて蒸気使用機器の運転
を管理することができる。
Therefore, the operation of the steam-using device can be managed based on these data.

発明の効果 蒸気消費量と蒸気圧力と復水温度および生産物の温度を
測定するので、これらの測定データを自動的にペンレコ
ーダー等に一度に表示することができ、個々の蒸気使用
機器の運転状態を一目で把握できる。
Effects of the invention Since steam consumption, steam pressure, condensate temperature, and product temperature are measured, these measured data can be automatically displayed at one time on a pen recorder, etc. You can grasp the status at a glance.

また、蒸気消費量や蒸気圧力あるいは生産物の温度に応
じて、制御弁の開閉を制御するので、自動的に製品の品
質を管理することができる。
Moreover, since the opening and closing of the control valve is controlled according to the steam consumption, the steam pressure or the temperature of the product, the quality of the product can be automatically controlled.

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)。
Example An example showing a specific example of the above technical means will be described (see FIG. 1).

ボイラ1で作った蒸気は蒸気主管2から分岐した蒸気導
入管3・4を通して、蒸気使用機器5・6に送られる。
蒸気使用機器5、6で加熱等の仕事をした蒸気は復水と
なって、スチームトラップ7・8で自動的に排除され
る。
The steam produced in the boiler 1 is sent to the steam-using devices 5 and 6 through the steam introducing pipes 3 and 4 branched from the steam main pipe 2.
The steam that has been used for heating or the like in the steam-using devices 5 and 6 becomes condensed water and is automatically removed by the steam traps 7 and 8.

蒸気導入管3・4には蒸気使用機器5・6に供給する蒸
気を所望の圧力に減圧する減圧弁9・10と蒸気の供給を
制御する制御弁11・12を配置する。
In the steam introducing pipes 3 and 4, pressure reducing valves 9 and 10 for reducing the pressure of the steam supplied to the steam using devices 5 and 6 to a desired pressure and control valves 11 and 12 for controlling the supply of the steam are arranged.

蒸気使用機器5・6とスチームトラップ7・8の間に復
水流量計13・14を配置する。復水流量計13・14に復水の
温度を測定する復水温度センサー15・16を内蔵させる。
Condensate flowmeters 13 and 14 are placed between the steam-using devices 5 and 6 and the steam traps 7 and 8. The condensate flow meters 13 and 14 have condensate temperature sensors 15 and 16 for measuring the temperature of the condensate.

蒸気導入管3・4の蒸気圧力を測定する圧力センサー17
・18と蒸気使用機器5・6の生産物の温度を測定する生
産物温度センサー19・20を復水流量計13・14に電気的に
連結する。また、復水流量計13・14に制御弁11・12とペ
ンレコーダー21・22を電気的に連結する。
Pressure sensor 17 for measuring the steam pressure in the steam inlet pipes 3 and 4
・ Electrically connect the product temperature sensors 19 and 20 that measure the product temperatures of 18 and steam-using devices 5 and 6 to the condensate flowmeters 13 and 14. Further, the control valves 11 and 12 and the pen recorders 21 and 22 are electrically connected to the condensate flow meters 13 and 14.

復水流量計13・14は復水の流量を測定して蒸気使用機器
5・6で消費する蒸気消費量を測定表示すると共に、圧
力センサー17・18で検出した圧力値と生産物温度センサ
ー19・20および復水温度センサー15・16で検出した温度
値を表示する。また、これらの測定値はペンレコーダー
21・22に電圧出力される。
The condensate flowmeters 13 and 14 measure the flow rate of the condensate to measure and display the amount of steam consumed by the steam-using devices 5 and 6, as well as the pressure value detected by the pressure sensors 17 and 18 and the product temperature sensor 19.・ Displays the temperature value detected by 20 and condensate temperature sensor 15 ・ 16. In addition, these measured values are
The voltage is output to 21 and 22.

また、復水流量計13・14は蒸気消費量と蒸気圧力および
復水温度、すなわち、蒸気消費量と蒸気のエンタルピー
および復水のエンタルピーの関係から熱量を演算表示す
ると共に、蒸気消費量や蒸気圧力あるいは生産物の温度
に基づいて、蒸気使用機器5・6に供給する蒸気を調節
する制御弁11・12の開閉制御を行う。
Also, the condensate flow meters 13 and 14 calculate and display the calorific value from the steam consumption, steam pressure and condensate temperature, that is, the relationship between the steam consumption and the enthalpy of steam and the enthalpy of condensate, and at the same time, the steam consumption and steam Based on the pressure or the temperature of the product, the opening / closing control of the control valves 11 and 12 for adjusting the steam supplied to the steam using devices 5 and 6 is performed.

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

第1図は本発明による蒸気消費量測定装置の一実施例の
概略とその配管状態を示す図であり、第2図は従来の蒸
気流量計の配管状態を示す図である。 5・6:蒸気使用機器 11・12:制御弁 13・14:復水流量計 15・16:復水温度センサー 17・18:圧力センサー 19・20:生産物温度センサー
FIG. 1 is a diagram showing an outline of an embodiment of a steam consumption measuring device according to the present invention and its piping condition, and FIG. 2 is a diagram showing the piping condition of a conventional steam flow meter. 5/6: Steam-using equipment 11/12: Control valve 13/14: Condensate flow meter 15/16: Condensate temperature sensor 17/18: Pressure sensor 19/20: Product temperature sensor

フロントページの続き (56)参考文献 特開 昭59−212606(JP,A) 特開 昭58−136730(JP,A) 特開 昭57−118129(JP,A) 実開 昭60−54920(JP,U)Continuation of the front page (56) Reference JP 59-212606 (JP, A) JP 58-136730 (JP, A) JP 57-118129 (JP, A) Actual development 60-54920 (JP , U)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】蒸気使用機器毎に蒸気消費量を測定表示す
る流量計を配置し、蒸気使用機器毎に蒸気圧力と復水温
度および生産物の温度を測定表示する手段を設け、蒸気
使用機器毎の蒸気消費量と蒸気圧力および復水温度から
蒸気使用機器毎の消費熱量を演算表示する手段を設ける
と共に、各々の蒸気使用機器に供給する蒸気を調節する
制御弁の開閉を蒸気使用機器毎の上記測定値によって制
御するようにした、蒸気使用機器の運転管理装置。
1. A steam flow meter for measuring and displaying a steam consumption amount for each device using steam, and means for measuring and displaying a steam pressure, a condensate temperature and a product temperature are provided for each device using steam. A means for calculating and displaying the amount of heat consumed by each steam-using device from the steam consumption, steam pressure, and condensate temperature of each steam-using device is provided, and the opening and closing of the control valve for adjusting the steam supplied to each steam-using device An operation management device for steam-using equipment, which is controlled by the above measured value of.
JP61087431A 1986-04-15 1986-04-15 Operation management device for equipment using steam Expired - Fee Related JPH0674880B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61087431A JPH0674880B2 (en) 1986-04-15 1986-04-15 Operation management device for equipment using steam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61087431A JPH0674880B2 (en) 1986-04-15 1986-04-15 Operation management device for equipment using steam

Publications (2)

Publication Number Publication Date
JPS62246700A JPS62246700A (en) 1987-10-27
JPH0674880B2 true JPH0674880B2 (en) 1994-09-21

Family

ID=13914676

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61087431A Expired - Fee Related JPH0674880B2 (en) 1986-04-15 1986-04-15 Operation management device for equipment using steam

Country Status (1)

Country Link
JP (1) JPH0674880B2 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2684235B2 (en) * 1990-09-14 1997-12-03 株式会社テイエルブイ Abnormality diagnosis device for steam-using equipment
JP2684239B2 (en) * 1990-10-15 1997-12-03 株式会社テイエルブイ Abnormality diagnosis device for steam-using equipment
JP2684240B2 (en) * 1990-10-15 1997-12-03 株式会社テイエルブイ Productivity control device for steam-using equipment
JP2684241B2 (en) * 1990-10-15 1997-12-03 株式会社テイエルブイ Productivity control device for steam-using equipment
CN104121481A (en) * 2014-07-30 2014-10-29 山东宏信化工股份有限公司 Double-flow-direction steam conveying system
CN105465608A (en) * 2014-09-12 2016-04-06 付开领 Temperature and pressure reducing device
CN109798445B (en) * 2019-02-25 2024-04-16 新奥数能科技有限公司 Steam tempering system and application method thereof
CN110345383A (en) * 2019-06-05 2019-10-18 精楷电子科技(上海)有限公司 A kind of on-Line Monitor Device and jet chimney
CN114216056A (en) * 2021-12-22 2022-03-22 华能酒泉发电有限公司 Method for measuring local pressure loss of conveying steam pipe

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57118129A (en) * 1981-01-16 1982-07-22 Ricoh Co Ltd Method and device for measuring quantity of heat of jet fluid
JPS58136730A (en) * 1982-02-05 1983-08-13 Daido Steel Co Ltd Blowing gas control device for reflux type vacuum degassing device
JPS59212606A (en) * 1983-05-18 1984-12-01 バブコツク日立株式会社 Controller for temperature of steam
JPS6054920U (en) * 1983-09-21 1985-04-17 株式会社 テイエルブイ drain flow meter

Also Published As

Publication number Publication date
JPS62246700A (en) 1987-10-27

Similar Documents

Publication Publication Date Title
CN106872514A (en) Steady Heat Transfer process heat transfer coefficient and dirtiness resistance value on-line monitoring system and method
US4876897A (en) Steam quality measurement apparatus and method
JPH0674880B2 (en) Operation management device for equipment using steam
CN101939626B (en) Method and arrangement for measuring at least one physical magnitude, such as temperature, flow or pressure of the cooling fluid flowing in an individual cooling element cycle of a cooling element in a metallurgical furnace
CN212585877U (en) Ultrasonic heat meter for air conditioner valve
CN108871821A (en) Based on mean value-moving range method air cooler energy efficiency state method of real-time
CN106596164A (en) Heat exchanger energy efficiency online detection device
Takitani et al. Density wave instability in once-through boiling flow system,(I) Experiment
JPH06341917A (en) Flow rate detector
CN204201492U (en) The real-time monitoring device that a kind of high-pressure power plant feed water preheater bypass duct leaks
CN105572168A (en) Thermal type steam dryness meter
JP2000215366A (en) Water pipe leakage monitoring device
JP2684240B2 (en) Productivity control device for steam-using equipment
KR200361542Y1 (en) Equipment of Error Checking and Correcting for Heat and Flow Meter
JP3168917B2 (en) Flow measurement device
CN207198010U (en) Steel plant's cooling water corrosion speed detection simulation operating mode device
CN207675754U (en) Recirculated water on-line detecting system
CN1090391A (en) Carbon monodixe conversion process steam ratio measuring controller technology
JP3063514B2 (en) Flow measurement method using pressure sensor
KR900005477B1 (en) Electric by heated steam quality meter and its method
CN101324457A (en) Intelligent detection method of steam tiny flow quantity
CN212459486U (en) Gas phase heat exchange experiment testing device for plate heat exchanger
JP5915465B2 (en) Boiler thermal output measuring device
SU1537952A1 (en) Method of monitoring cinder deposition of heated surface of steam boiler
CN107270955A (en) Use the fuel sub-metering of combustion rate signal

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees