JPS5932713A - Air flow rate control process for boiler - Google Patents
Air flow rate control process for boilerInfo
- Publication number
- JPS5932713A JPS5932713A JP57139878A JP13987882A JPS5932713A JP S5932713 A JPS5932713 A JP S5932713A JP 57139878 A JP57139878 A JP 57139878A JP 13987882 A JP13987882 A JP 13987882A JP S5932713 A JPS5932713 A JP S5932713A
- Authority
- JP
- Japan
- Prior art keywords
- flow rate
- boiler
- air
- air flow
- fuel
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N1/00—Regulating fuel supply
- F23N1/02—Regulating fuel supply conjointly with air supply
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2235/00—Valves, nozzles or pumps
- F23N2235/02—Air or combustion gas valves or dampers
- F23N2235/06—Air or combustion gas valves or dampers at the air intake
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2237/00—Controlling
- F23N2237/02—Controlling two or more burners
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Regulation And Control Of Combustion (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はボイラの空気流量制御に係フ、特に、バーナ個
別に空燃比を好適に制御する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to air flow rate control in a boiler, and particularly to a method for suitably controlling the air-fuel ratio of each burner.
従来のボイラ空気流量制御方式は、第1図に示すように
ボイラlの合計空気流量(検出器51)を規定値に制御
するもので、バーナ6個別の空燃比は制御されず、特に
、石炭バーナや油とガスの混焼バーナなどで燃焼不安定
の要因となっていた。The conventional boiler air flow rate control method, as shown in Fig. 1, controls the total air flow rate (detector 51) of the boiler l to a specified value, but the air-fuel ratio of each burner 6 is not controlled. This was a cause of combustion instability in burners and oil and gas mixed combustion burners.
即ち、ボイラ1の合計重油流量(検出器52)に見合っ
て、合計空気光量(検出器51)を押込通風機2(以下
FDP)へロダンパ3によ量制御する方式であり、バー
ナ6個別の空燃比は制御しないため、バーナ6の上段と
下段、又は午前と午後で燃焼状態が異なシ、好適な燃焼
が期待できなかった。That is, the total amount of air light (detector 51) is controlled by the damper 3 of the forced draft fan 2 (hereinafter referred to as FDP) in accordance with the total heavy oil flow rate (detector 52) of the boiler 1, and Since the air-fuel ratio is not controlled, the combustion conditions differ between the upper and lower stages of the burner 6, or between the morning and the afternoon, and suitable combustion cannot be expected.
一方、プラント起動時は、ボイラ1の保安上から、空気
流量をバーナ6の点火本数如何にかかわらず、規定値以
上に保つ必要があり(第4図)、バーナの燃焼に寄与し
ない空気(11と12の間の量)は点火していないバー
ナのエアレジスタ(第2図の23)から逃がすことによ
り、燃焼バーナ6の空気量を過不足なく制御する必要が
おる。On the other hand, when starting up the plant, for the safety of the boiler 1, it is necessary to maintain the air flow rate above the specified value regardless of the number of ignitions of the burners 6 (Fig. It is necessary to control the amount of air in the combustion burner 6 to just the right amount by letting the amount between 1 and 12 escape from the air register (23 in FIG. 2) of the burner that is not ignited.
しかし、従来方式は、多数のバーナを一括して制御する
方式であp、バーナの入口共通母管圧力からバーナの合
計燃料量を求め、バーナの空気流量’1FDF出口と火
炉の差圧から求めて空燃比を制御し、バーナ個別の空燃
比は必ずしも適切に制御できない欠点がある。さらに、
従来方式は、この流量側#1を第3図に示すように、バ
ーナ個別の最適空燃比曲線14に対し、上限値13と下
限値15を設定し2、バーナ母管圧力に対し、I” D
F出口と火炉の圧力差が上限設定値を越えfc場合に
エアレジスタを開き、下限設定値以下になった場合に、
閉じるもので、いわゆる0N−OFF制御によりバー
すの空気流蓋を制御しているため、バーナ部の空燃比が
適正に維持できず、バーナ燃焼不安定と’x D s煙
色や未燃分がボイラから排出され、第2次公害全誘発さ
せる要因となっていた。However, in the conventional method, a large number of burners are controlled at once, and the total amount of fuel in the burners is determined from the common header pressure at the inlet of the burners, and the air flow rate of the burners is calculated from the differential pressure between the FDF outlet and the furnace. However, the air-fuel ratio of each burner cannot necessarily be controlled appropriately. moreover,
In the conventional system, as shown in Fig. 3, the upper limit value 13 and the lower limit value 15 are set for the optimum air-fuel ratio curve 14 for each burner on the flow rate side #1, and the burner main pipe pressure is set at I''. D
If the pressure difference between the F outlet and the furnace exceeds the upper limit set value fc, open the air register, and if the pressure difference falls below the lower limit set value,
The bar is closed by so-called 0N-OFF control.
Since the airflow lid of the boiler is controlled, the air-fuel ratio in the burner section cannot be maintained properly, resulting in unstable burner combustion, smoke color, and unburned matter being discharged from the boiler, resulting in secondary pollution. It was a triggering factor.
本発明の目的に、各バーナ部の燃焼を安定に維持するた
め、数台のバーナ単位に燃焼部を分割して各々を独立し
て制御することによp、バーナ部の最適燃焼を図る空気
光量制御方法を提供するにある。For the purpose of the present invention, in order to maintain stable combustion in each burner section, the combustion section is divided into several burner units and each is controlled independently. The present invention provides a light amount control method.
本発明は、バーナ個別に空燃比を制御する手段として、
数個のバーナ単位に燃焼室を分離し、コンパートメント
即位の空気流量を最適に制御するものであり、鉤に、低
流並域での151を量計測の難しさの問題を克服する手
段として、バーナ燃料母管圧力とコンパートメント/火
炉差圧t(圧力信号として)計測して、これらから流量
を求め低流量域での空燃比制御を改善する一方、ボイラ
全体の空燃比を求め、これが最適となるような補正を加
えることによシポイラ全体の燃焼と効率向上ヲ崗るもの
である。The present invention provides means for controlling the air-fuel ratio of individual burners,
It separates the combustion chamber into several burner units and optimally controls the air flow rate in each compartment, and as a means to overcome the problem of difficulty in measuring the amount of 151 in the low flow area. The burner fuel main pipe pressure and the compartment/furnace differential pressure t (as a pressure signal) are measured, and the flow rate is determined from these to improve air-fuel ratio control in the low flow range. At the same time, the air-fuel ratio of the entire boiler is determined, and this is the optimal one. By adding such corrections, the overall combustion and efficiency of the sipoiler can be improved.
また、コンパートメント人口ダンパによる空気流量制御
を改善するため、人口圧力を規定値に制御できる手段と
して、起動時はIPレジスタを開閉操作することにより
、また、通常時i、J: 1” D F入ロダンバで制
御する方式を付加する。In addition, in order to improve the air flow control by the compartment population damper, as a means to control the population pressure to a specified value, by opening and closing the IP register at startup, and by opening and closing the IP register at normal times, Add a method to control with Rodanba.
以下、本発明の一実施例を第5図および第6図を用いて
説明する。An embodiment of the present invention will be described below with reference to FIGS. 5 and 6.
ボイラ燃焼系統図(第5図)において、バーナ6の燃焼
部Xe台のバーナ単位に分割し、各々のコンパートメン
トに対して、空気流量調節用ダンパ8と空気流量7、及
び燃料流!検出器53を設けて、各コンパートメントの
燃料#Lftに見合って空気流itt制御する方式とし
ている。In the boiler combustion system diagram (Fig. 5), the combustion section of the burner 6 is divided into Xe burner units, and each compartment has an air flow rate adjustment damper 8, an air flow rate 7, and a fuel flow! A detector 53 is provided to control the air flow itt according to the fuel #Lft in each compartment.
ところで、ボイラ起動時、バーナ点火本数が少なく、各
コンパートメントの空気流量の計測が難かしいため、コ
ンパートメントと火炉の差圧37がら空気がtii’e
、バーナ母管燃料圧力54から燃料流量を関数発生器3
2により求めて、この偏差信号を比例積分器34により
演算して、FDP人ロダンバ3を制御している。By the way, when the boiler is started, the number of burners ignited is small and it is difficult to measure the air flow rate in each compartment.
, the fuel flow rate from the burner main pipe fuel pressure 54 to the function generator 3
2, and this deviation signal is calculated by the proportional integrator 34 to control the FDP robot 3.
一方、ボイラは低負荷時は、空気流量を規定値に通常、
負荷時は、ボイラ全体の空気流量51を合ハ1゛燃料量
52に見合って最適値にそれぞれ制御する必要があるた
め、起動時はFDP人ロダンノ<3により1.l+!!
常時Cユコンパートメント入ロダンノく制御のコンパー
トメント重油流量53から関数発生器34で求めた空気
流量要求値を、合計空気流祉の偏差信号を比例積分器3
4で演算した信号によp1掛算器42を介して補正する
ことによp、合t1空気量ヲ目標値に推持できるように
する。第7図に重油流値に対する空気流量の関係を示す
。On the other hand, when the load is low, the boiler usually adjusts the air flow rate to the specified value.
When under load, it is necessary to control the air flow rate 51 of the entire boiler to the optimum value according to the total fuel amount 52, so at startup, the FDP is set to 1. l+! !
The required air flow rate value obtained by the function generator 34 is calculated from the compartment heavy oil flow rate 53 controlled by the constant C unit, and the deviation signal of the total air flow is calculated by the proportional integrator 3.
By correcting the signal calculated in step 4 via the p1 multiplier 42, the total air amount p and t1 can be maintained at the target value. FIG. 7 shows the relationship between the air flow rate and the heavy oil flow value.
また、コンパートメント人口ダンパの制御性を改善する
には、FDP出口圧力を規定値に維持する必要があり、
起動時はFDP出ロドロドラフトエアレジスタ23で、
通常時はFDP人ロメロダンパ3り行なう。なお、図中
4は重油ポンプ、5は重油流量調節弁、9μF’DF出
ロドラフト検出器、10はコンパートメント火炉差圧検
出器、16は安定燃焼特性図線、31はバーナ母管圧力
、21はランドボックス、22は炉内、37はコンパー
トメント火炉差圧、40は切替器、41ii:イJ号発
生器、42μ掛算器、53はコンパートメント重油流量
、54はコンバートメントノ仁−す母管圧力である。In addition, to improve the controllability of the compartment damper, it is necessary to maintain the FDP outlet pressure at a specified value.
At startup, FDP output rod draft air register 23,
Normally, the FDP person performs 3 Romero dampers. In addition, in the figure, 4 is a heavy oil pump, 5 is a heavy oil flow rate control valve, 9 μF' DF output draft detector, 10 is a compartment furnace differential pressure detector, 16 is a stable combustion characteristic diagram line, 31 is a burner main tube pressure, and 21 is a Land box, 22 is the inside of the furnace, 37 is the compartment furnace differential pressure, 40 is the switch, 41ii: A J generator, 42μ multiplier, 53 is the compartment heavy oil flow rate, 54 is the conversion header pressure. be.
本発明によれば、ボイラの1・−タル空燃比、並びに、
バーナ個別の空燃比が、プラント起動から通常負荷帯ま
で安定してii制御できるので、ボイラの安定燃焼とプ
ラントの効率向上の効果があり、また、ボイラの燃焼が
安定して行なえるため負荷変化率の向上も期待できる。According to the present invention, the 1-tal air-fuel ratio of the boiler, and
The air-fuel ratio of each burner can be controlled stably from plant start-up to normal load range, resulting in stable boiler combustion and improved plant efficiency.Also, since boiler combustion can be performed stably, load changes can be achieved. We can also expect the rate to improve.
第1図は、従来方式のボイラ燃焼系統図、第2図は、バ
ーナの燃焼部の断面図、第3図μ、重油バーナの安定燃
焼特性図、@4図は、ボイラの合言1空気流量設定因、
第5図は、本発明のコンパートメント燃焼ボイラの系統
図、第6図は、本発明の空気流量制御系統図、第′7図
は、ボイラの安定燃焼曲線図である。
7・・・コンパートメント人口燃料流値検出器、8・・
・U 7 バー トメント入ロダンパ、9・・・コンパ
ートメント人口燃料流値検出器、37・・・コンハート
メント火炉差圧、53・・・コンハートメント重油流量
、≠1胆
茅3 目
−−ハ゛〜1母管吏油圧力
$4 目
ホ呵う菓竹
め!;囚Figure 1 is a conventional boiler combustion system diagram, Figure 2 is a sectional view of the combustion section of the burner, Figure 3 μ is a diagram of stable combustion characteristics of a heavy oil burner, and Figure 4 is a boiler code 1 air Flow rate setting factor,
FIG. 5 is a system diagram of the compartment combustion boiler of the present invention, FIG. 6 is a system diagram of the air flow control system of the present invention, and FIG. '7 is a stable combustion curve diagram of the boiler. 7... Compartment artificial fuel flow value detector, 8...
・U 7 Rod damper with bartment, 9... Compartment artificial fuel flow value detector, 37... Conhartment furnace differential pressure, 53... Conhartment heavy oil flow rate, ≠1 3rd--high ~1 Master pipe oil pressure $4 You idiot! ;prisoner
Claims (1)
ナ単位に燃焼室ヲ分割したコンパートメント燃焼ボイラ
において、コンパートメントの燃料流社と空気流量を計
測する手段と、前記コンパートメントの空気流mを制御
するダンハラ設は前記バーナの空燃比が最適になるよう
コンパートメント人ロダンバを制御することを特徴とす
るボイラの空気流量制御方法。1. In a compartmental combustion boiler in which the combustion chamber of a boiler consisting of a large number of burners is divided into units of several burners, a means for measuring the fuel flow rate and air flow rate in the compartment, and a means for controlling the air flow m in the compartment. The Danhara installation is a method for controlling the air flow rate of a boiler, characterized by controlling a compartment rotor so that the air-fuel ratio of the burner is optimized.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57139878A JPS5932713A (en) | 1982-08-13 | 1982-08-13 | Air flow rate control process for boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57139878A JPS5932713A (en) | 1982-08-13 | 1982-08-13 | Air flow rate control process for boiler |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5932713A true JPS5932713A (en) | 1984-02-22 |
JPH0315088B2 JPH0315088B2 (en) | 1991-02-28 |
Family
ID=15255667
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57139878A Granted JPS5932713A (en) | 1982-08-13 | 1982-08-13 | Air flow rate control process for boiler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5932713A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03163298A (en) * | 1989-11-07 | 1991-07-15 | Babcock & Wilcox Co:The | Heat insulating pipe structure |
US7950919B2 (en) * | 2004-10-14 | 2011-05-31 | Shell Oil Company | Method and apparatus for monitoring and controlling the stability of a burner of a fired heater |
CN112797437A (en) * | 2021-02-03 | 2021-05-14 | 华能武汉发电有限责任公司 | Intelligent air supply control method, equipment and storage medium |
-
1982
- 1982-08-13 JP JP57139878A patent/JPS5932713A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03163298A (en) * | 1989-11-07 | 1991-07-15 | Babcock & Wilcox Co:The | Heat insulating pipe structure |
US7950919B2 (en) * | 2004-10-14 | 2011-05-31 | Shell Oil Company | Method and apparatus for monitoring and controlling the stability of a burner of a fired heater |
CN112797437A (en) * | 2021-02-03 | 2021-05-14 | 华能武汉发电有限责任公司 | Intelligent air supply control method, equipment and storage medium |
CN112797437B (en) * | 2021-02-03 | 2022-03-22 | 华能武汉发电有限责任公司 | Intelligent air supply control method, equipment and storage medium |
Also Published As
Publication number | Publication date |
---|---|
JPH0315088B2 (en) | 1991-02-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4716858A (en) | Automatic firing rate control mode means for a boiler | |
JP3101823B2 (en) | Control method for low NOx combustion system | |
US4373897A (en) | Open draft hood furnace control using induced draft blower and exhaust stack flow rate sensing | |
JPS5886323A (en) | Forced exhaust airtight gas boiler through microprocessor control | |
JPS5932713A (en) | Air flow rate control process for boiler | |
JPH08200015A (en) | Method for operating combined plant | |
AU2007330307B2 (en) | Batch waste gasification process | |
JP2620638B2 (en) | Pulse combustor ignition control device | |
US4644904A (en) | Gas fired heating boiler | |
JP3561309B2 (en) | Boiler combustion control method | |
JP3242239B2 (en) | Fuel gas control method and device | |
JP2002130606A (en) | Control device for drum level of boiler | |
JPS6023717A (en) | Method of controlling amount of combustion air in coal burning boiler | |
JPS62138619A (en) | Combustion device | |
JPH04136611A (en) | Combustion control | |
JPH06180102A (en) | Controller for amount of boiler feedwater | |
JPH0637972B2 (en) | Combustion control device | |
JPS633205B2 (en) | ||
JPS602806A (en) | Pulse burner with variable combustion amount | |
JP2651342B2 (en) | Control method of combustion type superheater | |
JPH0799245B2 (en) | Boiler start control device | |
JP3033806B2 (en) | Combustion stop device for incomplete combustion of combustion equipment | |
JPS58110918A (en) | Operation of boiler | |
JPH0223766B2 (en) | ||
JPH0223924Y2 (en) |