JPH01150703A - Steam load analyzer for boiler - Google Patents

Steam load analyzer for boiler

Info

Publication number
JPH01150703A
JPH01150703A JP31151987A JP31151987A JPH01150703A JP H01150703 A JPH01150703 A JP H01150703A JP 31151987 A JP31151987 A JP 31151987A JP 31151987 A JP31151987 A JP 31151987A JP H01150703 A JPH01150703 A JP H01150703A
Authority
JP
Japan
Prior art keywords
boiler
steam
sensors
fuel
load
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.)
Granted
Application number
JP31151987A
Other languages
Japanese (ja)
Other versions
JPH0788928B2 (en
Inventor
Toshihiro Kayahara
敏広 茅原
Sukeo Takechi
融夫 武智
Kazu Kubo
久保 和
Tetsuji Namoto
哲二 名本
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.)
Miura Co Ltd
Original Assignee
Miura 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 Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP31151987A priority Critical patent/JPH0788928B2/en
Publication of JPH01150703A publication Critical patent/JPH01150703A/en
Publication of JPH0788928B2 publication Critical patent/JPH0788928B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE: To easily measure the max. vapor consumption, boiler efficiency, etc., by attaching sensors for detecting flow rate signals to a fuel and feed water flowmeters and pressure sensor for measuring the internal pressure to a boiler, and providing a load analyzer for operating and storing the vapor load, based on the signals from the sensors. CONSTITUTION: A pressure sensor 2 for measuring the boiler pressure is provided at a boiler 1, and sensors 7 for converting flow rates to signals and sending to a load analyzer 6 are provided at a fuel flowmeter FO and feed water flowmeter WF. The load analyzer 6 receiving the signals of the fuel and feed water flow rates analyzes the load from these values to operate and store the vapor consumption, boiler efficiency, etc. A disc 12 is fixed to a rotary shaft 17 of an existing flowmeter 10 having a needle 11 and identifying pieces 13 such as metal pieces or paint pieces adhered to equal divisions of about 1/20-1/100 of full revolution. The sensors 7 disposed near the identifying pieces 13 use optical sensors or magnetic sensors.

Description

【発明の詳細な説明】 〔発明の利用分野〕 この発明は、ボイラー等の蒸気発生装置における蒸気負
荷分析装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a steam load analyzer in a steam generator such as a boiler.

〔従来技術〕[Prior art]

工場、ビル、商店などでは、蒸気を加熱手段や暖房手段
として使用するが、その蒸気発生装置としてボイラーを
設置している。ボイラーより発生する蒸気の使用量を測
定するための機器として蒸気流量計があるが、ボイラー
毎に蒸気流量計を配設しているところは一般に少なく、
それは高価なため、或いは、なくても別設支障がないな
どの理由による。通常、蒸気使用量としては、1時間毎
の給水流量及び燃料流量などの記録から平均値を計算す
る。
In factories, buildings, shops, etc., steam is used as a means of heating and heating, and boilers are installed as steam generating equipment. A steam flow meter is a device used to measure the amount of steam used by a boiler, but there are generally few places that have a steam flow meter installed in each boiler.
This is because it is expensive, or because there is no problem with installing it separately. Normally, the amount of steam used is calculated as an average value from hourly records of water supply flow rate, fuel flow rate, and the like.

ところが、蒸気使用量は第5図に示すように時間的に変
動する。よって、ボイラーの増設、更新などに際し、瞬
間蒸気使用量(最高蒸気使用量)や時間的負荷変化傾向
を知りたい場合、上記の平均値による分析方法では正確
な値が得られず、また、蒸気流量計を追設したのでは、
手間とコストがかかってしまう。
However, the amount of steam used fluctuates over time as shown in FIG. Therefore, if you want to know the instantaneous steam usage (maximum steam usage) or temporal load change trends when expanding or updating boilers, the analysis method using the average value described above will not provide accurate values; By adding a flow meter,
It takes time and cost.

〔発明の目的及び概要〕[Purpose and outline of the invention]

この発明は、上述の問題点を解消し、構造が簡単で、既
設のボイラーにも容易に取付は可能なボイラー用蒸気負
荷分析装置を提供することを目的とするものである。
It is an object of the present invention to solve the above-mentioned problems and to provide a steam load analyzer for a boiler that has a simple structure and can be easily installed in an existing boiler.

即ち、この発明は、ボイラー(1)に対して燃料供給ラ
イン(3)、給水ライン(4)及び蒸気ライン(9)を
それぞれ接続するとともに、前記燃料供給ライン(3)
及び給水ライン(4)にそれぞれ燃料流量計(OF)、
給水流量計(WF)を挿入して成る装置において、各々
の前記流量計に流量信号を検出するためのセンサー(7
)を設け、前記ボイラー(1)に缶内圧力を測定するた
めの圧力センサー(2)を設け、これらのセンサーから
の信号により蒸気負荷を演算し、記憶するための負荷分
析器(6)を設けたことを特徴とするものである。
That is, the present invention connects a fuel supply line (3), a water supply line (4), and a steam line (9) to the boiler (1), and also connects the fuel supply line (3) to the boiler (1).
and a fuel flow meter (OF) in the water supply line (4), respectively.
In a device in which a water supply flowmeter (WF) is inserted, a sensor (7) for detecting a flow rate signal is installed in each of the flowmeters.
), the boiler (1) is provided with a pressure sensor (2) for measuring the internal pressure of the boiler, and a load analyzer (6) is provided for calculating and storing the steam load based on the signals from these sensors. It is characterized by the fact that it has been provided.

〔発明の実施例] 以下、この発明の好ましい実施例を図面に基づいて説明
する。図中(1)はボイラー、(2)はこのボイラーに
設けた、缶内圧力を測定するための圧力センサー、(3
)は燃料供給ライン、(4)は給水ラインである。燃料
供給ライン(3)中には、燃料流量計(OF)、燃料供
給ポンプ(OP)及び電磁開閉弁(5)を挿設し、前記
燃料流量計(OF)には、燃料流量を信号に変換して負
荷分析器(6)に送るためのセンサー(7)を設けてい
る。また、給水ライン(3)中には、給水流量計(WF
)、給水ポンプ(神)及び逆止弁(8)を挿設し、前記
給水流量計(WF)には、給水流量を信号に変換して負
荷分析器(6)に送るためのセンサー(7)を設けてい
る。(9)は蒸気ラインであり、主蒸気弁06)を挿設
している。
[Embodiments of the Invention] Preferred embodiments of the present invention will be described below based on the drawings. In the figure, (1) is a boiler, (2) is a pressure sensor installed in this boiler to measure the pressure inside the can, and (3)
) is a fuel supply line, and (4) is a water supply line. A fuel flow meter (OF), a fuel supply pump (OP), and an electromagnetic on-off valve (5) are inserted into the fuel supply line (3), and the fuel flow meter (OF) receives a signal indicating the fuel flow rate. A sensor (7) is provided for conversion and sending to a load analyzer (6). In addition, there is a water supply flowmeter (WF) in the water supply line (3).
), a water supply pump (controller), and a check valve (8) are installed, and the water supply flow meter (WF) is equipped with a sensor (7) for converting the water supply flow rate into a signal and sending it to the load analyzer (6). ) has been established. (9) is a steam line, into which a main steam valve 06) is inserted.

図中の破線は信号線を示し、圧力、燃料流量及び給水流
量の炉信号を受けた負荷分析器(6)は、それらの値か
ら負荷分析を行い、蒸気使用量やボイラー効率などを演
算・記憶する。データの回収時間、サンプリング回数・
時間は予め適宜、設定してお第2図から第4図に、既設
流量計にセンサーを取り付けた構造を示す。指針aOを
有する流量計0(I)の回転軸(17)に円板02)を
固着しているが、この円板の外縁近傍部分には、1回転
分を1720〜1/100程度に等分割した位置に金属
片或いは塗料片などの識別片側を付着させている。金属
片を付着させる場合には、円板の材質は非金属性のもの
にする。
The broken lines in the figure indicate signal lines, and the load analyzer (6) receives the furnace signals of pressure, fuel flow rate, and feed water flow rate, performs load analysis from those values, and calculates steam usage, boiler efficiency, etc. Remember. Data collection time, sampling frequency,
The time is set appropriately in advance. Figures 2 to 4 show a structure in which a sensor is attached to an existing flowmeter. A disk 02) is fixed to the rotating shaft (17) of a flowmeter 0 (I) having a pointer aO, and near the outer edge of this disk there is a rotational speed equal to about 1720 to 1/100. An identification piece such as a piece of metal or paint is attached to one side of the divided position. If a metal piece is to be attached, the material of the disc should be non-metallic.

前記識別片側に近接させて設けたセンサー(7)として
は、光センサー或いは磁気センサーなどを用いる。04
)はセンサー(7)を流量計00)に固定するための固
定部材、05)はその止め具である。以上のような構造
により、サンプリング時間あたりいくつの識別片がセン
サーの前面を横切ったかを積算しておけば、流量の微小
な変化量を測定することができる。
As the sensor (7) provided close to one side of the identification, an optical sensor, a magnetic sensor, or the like is used. 04
) is a fixing member for fixing the sensor (7) to the flowmeter 00), and 05) is its stopper. With the structure described above, minute changes in flow rate can be measured by integrating the number of identification pieces that cross the front surface of the sensor per sampling time.

上記の実施例は、信号発信機能のない流量計を用いる場
合であるが、信号発信機能を有する流量計は、その機能
を利用する。
Although the above embodiment uses a flowmeter without a signal transmission function, a flowmeter having a signal transmission function utilizes that function.

続いて、得られたデータをもとに、蒸気使用量及びボイ
ラー効率を算出する方法について説明する。まず、蒸気
使用量の算出方法について説明するが、これは蒸気圧力
と燃料流量のデータに基づいて算出する。データのサン
プリング時間は10see毎程度が適当である。
Next, a method for calculating steam usage and boiler efficiency based on the obtained data will be explained. First, a method for calculating the amount of steam used will be explained, which is calculated based on steam pressure and fuel flow rate data. Appropriate data sampling time is approximately every 10sees.

(1)缶内蒸気圧カ一定時 缶内蒸気圧カニ定のときは、人熱分の熱量が全て蒸気発
生に費やされるので、 缶内蒸気圧カニ 5 kg/crM G (飽和涼気の
エンタルピー657.99kcal/ kg、飽和水の
エンタルピー159.559kca j/kg )ボイ
ラー効率:90% 給水温度:20°C(飽和水のエンタルピー20.03
kcal/kg ) 燃料流1 : 0.191 / 10secとすると、 入熱量=燃料流量×比重×燃料の発熱量−〇、 19X
 O,86X 10200= 1667 (kcal〕 藩気早−入熱量×ボイラー効率÷エンタルピー増加分 = 1667X O,90÷(657,99−20,0
3)= 2.35kg (2)缶内蒸気圧力下降時 缶内蒸気圧力が下降しているときは、自己蒸発量分を加
算する。サンプリング時間中に缶内圧力が5.4→4.
6kg/cJGになった場合、缶内の保有水量を200
1、他の条件は上記のものと同様とすると、 自己蒸発量=χkg 5.4 kg / CTII Gの飽和蒸気のエンタル
ピー658.64kcal/kg、飽和水のエンタルピ
ー162.174kcal/kg4、6 kg / c
wt Gの飽和蒸気のエンタルピー657.28kca
l/kg、飽和水のエンタルピー156.810kca
l/kg(200−χ’) X 156.810+χX
 657.99=162.174 X200 これを解くと、χ=2.14kg よって蒸気量の総和は2.35+ 2.14= 4.4
9kg(3)缶内蒸気圧力上昇時 缶内蒸気圧力が上昇しているときは、ボイラーの保有水
量分のエンタルピー上昇に必要な熱量を差し引いて計算
する。サンプリング時間中に缶内圧力が4.6→5.4
 kg / ctM Gになった場合、他の条件は上記
のものと同様とすると、 (162,174−156,810) X 200 =
 1(172.8kca11(172.8÷657.9
9= 1.63kgよって蒸気量は2.35−1.63
= 0.72kg以上のようにして蒸気使用量は算出す
るが、ボイラーの種類、運転条件などを考慮して、適宜
、補正係数を用いる。
(1) When the steam pressure inside the can is constant When the steam pressure inside the can is constant, all of the human heat is used to generate steam, so the steam pressure inside the can is 5 kg/crMG (Enthalpy of saturated cool air 657 .99 kcal/kg, enthalpy of saturated water 159.559 kca j/kg) Boiler efficiency: 90% Feed water temperature: 20°C (enthalpy of saturated water 20.03
kcal/kg) Fuel flow 1: 0.191/10sec, heat input = fuel flow rate x specific gravity x calorific value of fuel - 〇, 19X
O, 86
3) = 2.35 kg (2) When the steam pressure inside the can is decreasing When the steam pressure inside the can is decreasing, add the amount of self-evaporation. During the sampling period, the pressure inside the can increased from 5.4 to 4.
If it becomes 6kg/cJG, reduce the amount of water held in the can by 200
1. Assuming other conditions are the same as above, self-evaporation amount = χ kg 5.4 kg / enthalpy of saturated steam of CTII G 658.64 kcal/kg, enthalpy of saturated water 162.174 kcal/kg4, 6 kg / c.
Enthalpy of saturated steam of wt G 657.28 kca
l/kg, enthalpy of saturated water 156.810kca
l/kg (200-χ') X 156.810+χX
657.99 = 162.174
9kg (3) When the steam pressure inside the can increases When the steam pressure inside the can increases, calculate by subtracting the amount of heat required to increase the enthalpy of the amount of water held in the boiler. During the sampling time, the pressure inside the can increased from 4.6 to 5.4.
kg/ctMG, assuming other conditions are the same as above, (162,174-156,810) x 200 =
1 (172.8kca11 (172.8÷657.9
9 = 1.63kg, so the amount of steam is 2.35-1.63
The amount of steam used is calculated as follows: = 0.72 kg or more, but a correction factor is used as appropriate, taking into consideration the type of boiler, operating conditions, etc.

次に、ボイラー効率の算出方法について説明するが、こ
れは燃料流量と給水流量のデータに基づいて算出する。
Next, a method for calculating boiler efficiency will be explained, which is calculated based on data on fuel flow rate and water supply flow rate.

データのサンプリング時間は蒸気使用量のときより長く
、1時間或いは1日毎のデータでも良い。
The data sampling time is longer than that for steam usage, and may be hourly or daily data.

ボイラー効率η−(出熱量子入熱量)X100%人熱量
=燃料の発熱量= 10200kcal/kg    
−出熱量=発生蒸気量×発生蒸気の保有熱発生蒸気量=
給水量÷燃料使用量 =852kg÷58.7kg = 14.51 kg/
kg発生蒸気の保有熱(平均蒸気圧5kg/c1iIG
Boiler efficiency η - (heat output quantum heat input) x 100% human calorific value = calorific value of fuel = 10200kcal/kg
- Amount of heat output = Amount of steam generated x Amount of heat generated by the generated steam =
Water supply amount ÷ Fuel usage amount = 852 kg ÷ 58.7 kg = 14.51 kg/
Retained heat of kg generated steam (average steam pressure 5 kg/c1iIG
.

乾き度0.99) = (0,99x 657.99+ 0.01x 15
9.559) −20,030= 632.976kc
al/kg 、°、η= (14,51X632.976)÷102
00x 100=90.0% 上述のようにして得られたデータは、負荷分析器に記憶
させておき、必要に応じて出力、確認し、またそのデー
タをもとに、より詳細な分析を試みる。
Dryness 0.99) = (0,99x 657.99+ 0.01x 15
9.559) -20,030= 632.976kc
al/kg, °, η= (14,51X632.976)÷102
00x 100=90.0% The data obtained as described above is stored in the load analyzer, outputted and confirmed as necessary, and a more detailed analysis is attempted based on the data. .

〔発明の効果] この発明は、以上のような構成により、最高蒸気使用量
やボイラー効率などの正確な値を容易に計測できる。特
に、微小時間当たりの蒸気負荷を、蒸気圧力の変化を考
慮して正確に分析できる点で優れている。構成も簡単で
低コストで済み、既設のボイラーにも、同じく既設され
ている給水及び燃料流量計を利用して容易に対応可能で
ある。
[Effects of the Invention] With the above configuration, the present invention can easily measure accurate values such as the maximum amount of steam used and boiler efficiency. In particular, it is excellent in that it is possible to accurately analyze the steam load per minute time by taking into account changes in steam pressure. The configuration is simple and low cost, and it can be easily applied to existing boilers by using the existing water supply and fuel flow meters.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の実施例のシステムを示した概略説明
図、第2図はこの発明の実施例における既設流量計のセ
ンサー取付は構造を示した斜視図、第3図はその構造を
構成する円板の平面図、第4図は第2図の一部縦断面図
、第5図は蒸気負荷の時間的変動を示すグラフである。 (1)・・・ボイラー (2)・・・圧力センサー (3)・・・燃料供給ライン (4)・・・給水ライン (6)・・・負荷分析器 (7)・・・センサー (9)・・・蒸気ライン (10)・・・流量計 02)・・・円板 03)・・・識別片 θ″D・・・回転軸 (OF)・・・燃料流量計 (WF)・・・給水流量計 特許出願人   三浦工業株式会社 第1図 第 2 図 第3図 第5ダ 時間
Fig. 1 is a schematic explanatory diagram showing a system according to an embodiment of this invention, Fig. 2 is a perspective view showing the structure of sensor installation of an existing flowmeter in an embodiment of this invention, and Fig. 3 is a configuration of the structure. FIG. 4 is a partial vertical sectional view of FIG. 2, and FIG. 5 is a graph showing temporal fluctuations in steam load. (1)...Boiler (2)...Pressure sensor (3)...Fuel supply line (4)...Water supply line (6)...Load analyzer (7)...Sensor (9) )... Steam line (10)... Flow meter 02)... Disc 03)... Identification piece θ''D... Rotating shaft (OF)... Fuel flow meter (WF)...・Water supply flowmeter patent applicant: Miura Kogyo Co., Ltd. Figure 1 Figure 2 Figure 3 Figure 5 Time

Claims (2)

【特許請求の範囲】[Claims] (1)ボイラー(1)に対して燃料供給ライン(3)、
給水ライン(4)及び蒸気ライン(9)をそれぞれ接続
するとともに、前記燃料供給ライン(3)及び給水ライ
ン(4)にそれぞれ燃料流量計(OF)、給水流量計(
WF)を挿入して成る装置において、各々の前記流量計
に流量信号を検出するためのセンサー(7)を設け、前
記ボイラー(1)に缶内圧力を測定するための圧力セン
サー(2)を設け、これらのセンサーからの信号により
蒸気負荷を演算し、記憶するための負荷分析器(6)を
設けたことを特徴とするボイラー用蒸気負荷分析装置。
(1) a fuel supply line (3) to the boiler (1);
A water supply line (4) and a steam line (9) are connected to the fuel supply line (3) and a water supply line (4), respectively, and a fuel flow meter (OF) and a water supply flow meter (
WF), each of the flowmeters is provided with a sensor (7) for detecting a flow rate signal, and the boiler (1) is provided with a pressure sensor (2) for measuring the internal pressure of the boiler. 1. A steam load analyzer for a boiler, characterized in that a load analyzer (6) is provided for calculating and storing the steam load based on signals from these sensors.
(2)回転積算型流量計(10)の回転軸(17)に円
板(12)を同軸に固着するとともに、この円板上に多
数の識別片(13)を円周方向にほぼ等分割して設け、
かつ前記識別片(13)に近接してセンサー(7)を設
けたことを特徴とする特許請求の範囲第1項に記載のボ
イラー用蒸気負荷分析装置。
(2) A disk (12) is fixed coaxially to the rotating shaft (17) of the rotary integrating flowmeter (10), and a large number of identification pieces (13) are divided almost equally in the circumferential direction on this disk. and provide
The steam load analyzer for a boiler according to claim 1, further comprising a sensor (7) provided close to the identification piece (13).
JP31151987A 1987-12-08 1987-12-08 Steam load analyzer for boiler Expired - Lifetime JPH0788928B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31151987A JPH0788928B2 (en) 1987-12-08 1987-12-08 Steam load analyzer for boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31151987A JPH0788928B2 (en) 1987-12-08 1987-12-08 Steam load analyzer for boiler

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP8237314A Division JP2737753B2 (en) 1996-08-19 1996-08-19 Steam load analyzer for boiler

Publications (2)

Publication Number Publication Date
JPH01150703A true JPH01150703A (en) 1989-06-13
JPH0788928B2 JPH0788928B2 (en) 1995-09-27

Family

ID=18018215

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31151987A Expired - Lifetime JPH0788928B2 (en) 1987-12-08 1987-12-08 Steam load analyzer for boiler

Country Status (1)

Country Link
JP (1) JPH0788928B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120052453A1 (en) * 2010-09-15 2012-03-01 General Electric Company Submetering hydrocarbon fueled water heaters with energy manager systems

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120052453A1 (en) * 2010-09-15 2012-03-01 General Electric Company Submetering hydrocarbon fueled water heaters with energy manager systems
US9217654B2 (en) * 2010-09-15 2015-12-22 General Electric Company Submetering hydrocarbon fueled water heaters with energy manager systems

Also Published As

Publication number Publication date
JPH0788928B2 (en) 1995-09-27

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