JPS59164823A - Moving bed drum type coal burning boiler - Google Patents

Moving bed drum type coal burning boiler

Info

Publication number
JPS59164823A
JPS59164823A JP58039537A JP3953783A JPS59164823A JP S59164823 A JPS59164823 A JP S59164823A JP 58039537 A JP58039537 A JP 58039537A JP 3953783 A JP3953783 A JP 3953783A JP S59164823 A JPS59164823 A JP S59164823A
Authority
JP
Japan
Prior art keywords
amount
moving bed
air
coal
controller
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
JP58039537A
Other languages
Japanese (ja)
Inventor
Tadahiro Kishikawa
岸川 忠弘
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP58039537A priority Critical patent/JPS59164823A/en
Publication of JPS59164823A publication Critical patent/JPS59164823A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N5/00Systems for controlling combustion
    • F23N5/003Systems for controlling combustion using detectors sensitive to combustion gas properties
    • F23N5/006Systems for controlling combustion using detectors sensitive to combustion gas properties the detector being sensitive to oxygen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/08Regulating fuel supply conjointly with another medium, e.g. boiler water
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2225/00Measuring
    • F23N2225/08Measuring temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2235/00Valves, nozzles or pumps
    • F23N2235/02Air or combustion gas valves or dampers
    • F23N2235/04Air or combustion gas valves or dampers in stacks
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N5/00Systems for controlling combustion
    • F23N5/003Systems for controlling combustion using detectors sensitive to combustion gas properties

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

PURPOSE:To suppress the fluctuation of steam pressure even if quick and substantial change in flow rate of steam occurs, by providing a branch air feed pipe, combustion temperature measuring means, controllers for controlling the openings of compartment dampers and means for measuring the oxygen content of combustion gas. CONSTITUTION:Based on a sum signal (f) obtained from the amount of a steam pressure deviated from a set pressure value and a steam flow rate, the amount of air supply by a air supply fan 30 provided in the branch pipe 32 is adjusted. Then the opening of a damper 33 is controlled to adjust the amount of air that will be blown from below a moving bed 34. A combustion temperature pattern of each of the compartments 41 is formed by the sum signal (f), and the openings of the compartment dampers 41a are controlled in such a way that the combustion temperature signals by the combustion temperature measuring means 40 may be in conformity with the combustion temperature patterns of the compartments 41. Further the amount of coal to be fed in conformity with the amount of that air is assessed by the value obtained by an oxygen content converter 38 to correct the sum signal (f).

Description

【発明の詳細な説明】 本発明は、移動床ドラム形石炭焚ボイラの改良に関する
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a moving bed drum type coal-fired boiler.

第1図に従来の移動床ドラム形石炭焚ボイラを示す。こ
の石炭焚ゲイ°うは、水を給水ポンプ1、給水制御弁2
を―でドラム形?イラ3に供給し、蒸発部4で加熱して
蒸気を発生させ、蒸気を過熱部5.蒸気流量制御弁6を
経て所定の機器に供給する。
Figure 1 shows a conventional moving bed drum type coal-fired boiler. This coal-fired gas pump supplies water with water pump 1 and water supply control valve 2.
Is it drum-shaped? The steam is supplied to the boiler 3 and heated in the evaporation section 4 to generate steam, and the steam is supplied to the superheating section 5. The steam is supplied to predetermined equipment via the steam flow control valve 6.

この石炭焚ボイラでは、蒸気流量の要求に応じて蒸気流
量制御弁6を開閉すると蒸気流量が増減し、これと同時
に蒸気の圧力が変動する。
In this coal-fired boiler, when the steam flow control valve 6 is opened or closed in response to a steam flow rate request, the steam flow rate increases or decreases, and at the same time, the steam pressure fluctuates.

従ってこの圧力変動がないようにするため次のように制
御している。即ち蒸気圧力が変動すると、圧力変換器7
でこれを検知し、この検知信号と圧力設定器8からの圧
力設定値Sとの偏差信号が制御器9に入力される。
Therefore, in order to prevent this pressure fluctuation, control is performed as follows. That is, when the steam pressure fluctuates, the pressure transducer 7
This is detected, and a deviation signal between this detection signal and the pressure setting value S from the pressure setting device 8 is input to the controller 9.

一方蒸気流量を変換器10で検知して制御器11で信号
調整する。この制御器1ノの出力は、制御器9の出力に
加算されて、給炭装置12及び空気供給装置13に操作
信号として入力する。
On the other hand, the steam flow rate is detected by the converter 10 and the signal is adjusted by the controller 11. The output of the controller 1 is added to the output of the controller 9 and inputted to the coal feeder 12 and the air supply device 13 as an operation signal.

給炭装置12は、この操作信号に応じて移動床14の速
度変更1石炭19の散布量の調整などをおこない、給炭
量を調整する。石炭19は、散布機(図示せず)によっ
て移動床14の一面に散布される。上記空気供給装Wj
usは、操作信号に応じて燃焼に必要な空気を調整する
。空気は、移動床14の下からダンノぐ15・・・を介
して吹き上げる空気16と助燃用空気17に分岐されて
供給される。このように給炭及び空気16゜17を供給
することによシ燃焼量が変化し、蒸発部4の受熱量が変
化して、ドラム形?イラ3の圧力制御がなされる。
The coal feeding device 12 changes the speed of the movable bed 14, adjusts the amount of coal 19 spread, and adjusts the amount of coal fed in response to this operation signal. Coal 19 is spread over one surface of moving bed 14 by a spreader (not shown). The above air supply system Wj
us adjusts the air necessary for combustion according to the operation signal. The air is branched into air 16 and auxiliary combustion air 17 that are blown up from below the movable bed 14 via dunnage pipes 15 . . . . In this way, by supplying coal and air 16°17, the amount of combustion changes, the amount of heat received by the evaporator 4 changes, and the drum-shaped? The pressure of the blower 3 is controlled.

なお、移動床14上で燃えつきた灰18は移動床14の
移動によって灰処理部(図示せず)に送られる。
Incidentally, the ash 18 burned on the moving bed 14 is sent to an ash processing section (not shown) by the movement of the moving bed 14.

しかしこの移動床ドラム形石炭焚デイラは、供給される
石炭粒形の大小比率、散布機の回転数などが変化すると
移動床14の移動方向の給炭散布パターンが変動する。
However, in this moving-bed drum-type coal-fired deira, the coal feeding distribution pattern in the moving direction of the moving bed 14 changes when the size ratio of the supplied coal particles, the rotation speed of the spreader, etc. change.

散布パターンが変動すると移動床14の全面では、空気
吹き抜は部と、埋火状態部とが発生して燃焼状態が不均
一となり、全体を燃焼させるためには過剰な量の空気1
6を供給する必要がある。     。
When the dispersion pattern fluctuates, over the entire surface of the moving bed 14, there will be some air vents and some buried fire areas, resulting in uneven combustion, and an excessive amount of air will be needed to burn the whole area.
It is necessary to supply 6. .

過剰な空気16が供給されていると、空気16を増減し
ても燃焼量を増減することができず、燃焼量の制御が困
難である。従って燃焼を増加するときは供給炭が燃焼し
なければならず。
If excessive air 16 is supplied, the amount of combustion cannot be increased or decreased even if the amount of air 16 is increased or decreased, making it difficult to control the amount of combustion. Therefore, when increasing combustion, the supplied coal must be burned.

又減少するときは移動床14上の石炭の燃焼が小さくな
るのを待たなければならない。
Moreover, when the amount decreases, it is necessary to wait until the combustion of coal on the moving bed 14 becomes smaller.

この結果急速大巾な蒸気流量が変化してもこれに的確に
対応することが難しく、蒸奥圧力の変動が大きくなシ、
運転に支障をきたす問題がある。
As a result, it is difficult to respond accurately to rapid changes in the steam flow rate, and the pressure in the steamer is subject to large fluctuations.
There is a problem that interferes with driving.

本発明は、上記事情に鑑みてなされたもので、その目的
とするところは、急速大巾な蒸気流量変化があっても、
これに良好に対応でき、蒸気圧力の変動を抑えることが
できる移動床ドラム形石炭焚ゲイラを得んとするもので
ある。
The present invention has been made in view of the above circumstances, and its purpose is to
It is an object of the present invention to provide a moving bed drum-type coal-fired galley that can cope well with this and can suppress fluctuations in steam pressure.

すなわち本発明は、移動床の下方に設けられその移動方
向に沿う複数個のコンパートメントダンパを有する分岐
送気管と、各コン・り一トメントダンパに対応する移動
床3の上方にそれぞれ−−9−−一、、−!鋳   、 設けた複数個の燃焼温度計測手段と、同計測手段の検知
信号にもとづいて対応する各コンパートメントダン・母
に開度制御信号を出力する制御器と、上記移動床で生じ
る燃焼ガスの酸素含有率を計測する計測手段と、同計測
手段の検知信号にもとづいて移動床給炭装置に給炭量制
御信号を出力する制御器とを具備したことを特徴とする
That is, the present invention provides a branch air pipe having a plurality of compartment dampers provided below the moving floor and along the moving direction thereof, and above the moving floor 3 corresponding to each compartment damper. -One,,-! The casting machine includes a plurality of combustion temperature measuring means provided, a controller that outputs an opening control signal to each corresponding compartment Dan/Mother based on the detection signal of the measuring means, and The present invention is characterized by comprising a measuring means for measuring the content rate, and a controller for outputting a coal feeding amount control signal to a moving bed coal feeding device based on a detection signal of the measuring means.

以下本発明を第2図に示す移動床ドラム形石炭焚?イラ
を参照して説明する。
Hereinafter, the present invention will be explained using a moving bed drum type coal-fired system as shown in FIG. This will be explained with reference to Ira.

図面は、空気及び給炭の制御系を示す。この制御系は、
蒸気流路2ノに設けた過熱部22と蒸気流量制御弁23
との連通部中間に圧力変換器24を配設している。この
圧力変換器24からの信号と圧力設定器25からの信号
8のとの偏差信号が第1制御器26に入力している。ま
た蒸気流路2ノには蒸気流量制御弁゛23の後流側に蒸
気流量変換器27が設けられ、流量信号を第2制御器2
8に入力している。第1制御器26と第2制御器28と
の信号を加算した信号fは、第3制御器29.空気供給
ファン3θ及び第4制御器31に入力している。第3制
御器29の出力信号は分岐送気管32のダン・り33に
入力しヤダンノ4開度を制御するようにしている。この
分岐送気管:9.21f:、、空気供給ファン30によ
って移動床34に下方から空気35を送るとともに、上
方から助燃用空気36を送っている。また第3制御器2
9の出力信号は、第5制御器37に入力している。第5
制御器37には、石炭の燃焼で生じる燃焼ガスの酸素含
有率を検知し、電気信号に変−換する酸素含有率変換器
38からの信号が入力している。第5制御器37は第3
制御器29の信号に酸素含有率変換器38の信号を補正
した値を給炭制御信号として給炭装置39に入力する。
The drawing shows the air and coal feed control system. This control system is
Superheating section 22 and steam flow control valve 23 provided in steam flow path 2
A pressure transducer 24 is disposed in the middle of the communication section with the pressure transducer 24. A deviation signal between the signal from the pressure transducer 24 and the signal 8 from the pressure setting device 25 is input to the first controller 26 . Further, a steam flow rate converter 27 is provided in the steam flow path 2 on the downstream side of the steam flow rate control valve 23, and the flow rate signal is transmitted to the second controller 2.
8 is entered. The signal f, which is the sum of the signals from the first controller 26 and the second controller 28, is sent to the third controller 29. It is input to the air supply fan 3θ and the fourth controller 31. The output signal of the third controller 29 is input to the opening 33 of the branch air pipe 32 to control the opening degree of the opening 4. This branch air pipe: 9.21f: , Air 35 is sent to the moving bed 34 from below by the air supply fan 30, and auxiliary combustion air 36 is sent from above. Also, the third controller 2
The output signal of 9 is input to the fifth controller 37. Fifth
A signal is input to the controller 37 from an oxygen content converter 38 that detects the oxygen content of combustion gas produced by combustion of coal and converts it into an electrical signal. The fifth controller 37
A value obtained by correcting the signal from the oxygen content converter 38 to the signal from the controller 29 is input to the coal feeding device 39 as a coal feeding control signal.

給炭装置39はこの入力信号にもとづいて移動床34へ
の給炭量を決定する。
The coal feeding device 39 determines the amount of coal to be fed to the moving bed 34 based on this input signal.

上記空気供給ファン30は、第1及び第2制′御器26
.28の加算信号fにもとづいて回転数制御される。ま
た第4制御器3ノには、複数個の燃焼温度計測手段4θ
からの信号が入力されて“る・これら計測手段“は・移
動床″“の千゛方にその移動方向に沿・て一定間隔で設
けられ、上記7分岐送気管32に形成して移動床34の
下方に設けた複数個のコン・り一トメント41・・・に
対応している。第4制御器31は、第1及び第2制御器
26.28からの加算信号fと燃焼温度によシ各コンパ
ートメント41・・・の燃焼温度・ぐターンを作り、計
測手段40・・・からの信号によシ各コンノぐ一トメン
ト41・・・がこのツクターンとなるように演算処理し
、各コンパートメントダンパ41aに出力している。
The air supply fan 30 has first and second controllers 26
.. The rotation speed is controlled based on the addition signal f of 28. Further, the fourth controller 3 includes a plurality of combustion temperature measuring means 4θ.
These measuring means are provided at regular intervals along the direction of movement of the moving bed, and are formed in the seven-branch air pipe 32 to detect the movement of the moving bed. It corresponds to a plurality of control points 41 . . . provided below the controller 34. The fourth controller 31 generates a combustion temperature of each compartment 41 based on the addition signal f from the first and second controllers 26, 28 and the combustion temperature, and generates a combustion temperature signal from the measuring means 40... Based on the signal, each compartment 41... performs arithmetic processing so as to achieve this turn, and outputs the result to each compartment damper 41a.

このように構成された移動床ドラム形石炭焚ゼイラは、
蒸気圧力が設定圧力値から偏差した量と蒸気流量との加
算信号fにもとづいて分岐送気管32に設けた空気供給
ファン30の空気供給量を調節するとともに、ダンパ3
3の開度を制御して移動床34の下方から送風する空気
量を調節する。従って必要燃焼量を発生するために適正
な空気量を供給することができる。また加算信号f(必
要燃焼量信号)によって各コンパ−トメント41の燃焼
温度ツヤターンを作す、各燃焼温度計測手段40・・・
で得た各部燃焼温度信号が各コンパ−トメント41の燃
焼温度パターント一致スるようにコンパートメントダン
ノj41&の開度を制御する。このため空気35の供給
量、供給パターンを最小かつ最適なものとすることがで
きる。更にこの空気量に見合う給炭量を、酸素含有率変
換器38で得た燃焼ガスの酸素含有率により的確に評価
して、この計測信号にもとづいて加算信号fを補正して
いるので、給炭量を適正な値に調整することができる。
The moving bed drum-shaped coal-fired zeira constructed in this way is
The air supply amount of the air supply fan 30 provided in the branch air pipe 32 is adjusted based on the sum signal f of the amount by which the steam pressure deviates from the set pressure value and the steam flow rate, and the damper 3
3 to adjust the amount of air blown from below the moving floor 34. Therefore, an appropriate amount of air can be supplied to generate the required combustion amount. In addition, each combustion temperature measuring means 40 .
The opening degrees of the compartments 41 and 41 are controlled so that the combustion temperature signals obtained in each section match the combustion temperature pattern of each compartment 41. Therefore, the supply amount and supply pattern of the air 35 can be minimized and optimized. Furthermore, the amount of coal to be fed that corresponds to this amount of air is accurately evaluated using the oxygen content of the combustion gas obtained by the oxygen content converter 38, and the addition signal f is corrected based on this measurement signal, so that The amount of charcoal can be adjusted to an appropriate value.

以上説明したように本発明によれば、移動床面の燃焼状
態を均一にして空気の吹き抜は部や埋火、状態部の発生
を防止して、移動床の下部から吹込む空気量を最少にで
きる。従って、この空気量を増減することによシ燃焼量
を増減することができ、圧力変動があっても重油燃焼や
ガス燃焼と同等の連応性が実現できる。
As explained above, according to the present invention, the combustion state on the movable bed surface is made uniform, the air venting is prevented from occurring, and the amount of air blown from the lower part of the movable bed is reduced. Minimum possible. Therefore, by increasing or decreasing this amount of air, the amount of combustion can be increased or decreased, and even if there are pressure fluctuations, it is possible to achieve coordination equivalent to heavy oil combustion or gas combustion.

また石炭粒形及び石炭の質が変化して燃#、量が変化し
ても、□燃焼ガス中の酸素含有率を検知して供給した空
気流量の中の酸素消費量を知シ、これにもとづいて給炭
量を制御するので、適正な給炭系が実現できる顕著な効
果を奏する。
In addition, even if the coal particle shape and coal quality change and the fuel number and quantity change, the oxygen content in the combustion gas can be detected and the amount of oxygen consumed in the supplied air flow rate can be determined. Since the amount of coal feed is controlled based on this, a remarkable effect is achieved in that an appropriate coal feed system can be realized.

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

第1図は従来の移動床ドラム形石炭焚?イラの概略説明
図、第2図は本発明の一実施例を示す移動床ドラム形石
炭焚ぎイラの概略説明図である。 21・・・蒸気流路、22・・・過熱部、23・・・蒸
気流量制御弁、24・・・圧力変換器、25・・・圧力
設定器、26・・・第1制御器、27・・・蒸気流量変
換器、28・・・第2制御器、29・・・第3制御器、
30・・・空気供給ファン、3ノ・・・第4制御器、3
2・・・分岐送気管、33・・・ダン・ぐ、34・・・
移動−床、35・・・空気、36・・・助燃用空気、3
7・・・第5制御器、38・・・酸素含有率変換器、′
39・・・給炭装置、40・・・燃焼温度計測手段、4
1・・・コンパートメント、41a・・・コンパートメ
ントダンパ平 。
Figure 1 shows a conventional moving bed drum type coal firing system? Fig. 2 is a schematic explanatory diagram of a moving bed drum type coal-fired oven showing an embodiment of the present invention. 21... Steam flow path, 22... Superheating section, 23... Steam flow control valve, 24... Pressure converter, 25... Pressure setter, 26... First controller, 27 ... steam flow rate converter, 28 ... second controller, 29 ... third controller,
30... Air supply fan, 3... Fourth controller, 3
2... Branch air pipe, 33... Dang, 34...
Movement - floor, 35...Air, 36...Air for auxiliary combustion, 3
7... Fifth controller, 38... Oxygen content converter,'
39... Coal feeding device, 40... Combustion temperature measuring means, 4
1... Compartment, 41a... Compartment damper flat.

Claims (1)

【特許請求の範囲】[Claims] 移動床の下方に設けられその移動方向に沿う複数個のコ
ンノクートメントダンパを有する分岐送気管と、各コン
ハートメントダン・り1・ζ対応する移動床の上方にそ
れぞれ設けた複数個の燃焼温度計測手段と、同計測手段
の検知信号にもとライて、対応スる各コン・り一トメン
トダンパ・に開度制御信号を出力する制御器と、上記移
動床で生じる燃焼ガスの酸素含有率を4測する計測手段
と、同計測手段の検知信号にもとづいて移動床給炭装置
に給炭量制御信号を出力する制御器とを具備したことを
特徴とする移動床ドラム形石炭焚ボイラ。
A branch air pipe provided below the moving bed and having a plurality of conhartement dampers along the moving direction thereof, and a plurality of combustion pipes provided above the moving bed corresponding to each conhartement damper 1 and ζ. a temperature measuring means, a controller that outputs an opening control signal to each corresponding compression damper based on the detection signal of the measuring means, and a controller that outputs an opening control signal to each corresponding compression damper; A moving bed drum type coal-fired boiler, characterized in that it is equipped with a measuring means for measuring the ratio, and a controller for outputting a coal feeding amount control signal to a moving bed coal feeding device based on a detection signal of the measuring means. .
JP58039537A 1983-03-10 1983-03-10 Moving bed drum type coal burning boiler Pending JPS59164823A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58039537A JPS59164823A (en) 1983-03-10 1983-03-10 Moving bed drum type coal burning boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58039537A JPS59164823A (en) 1983-03-10 1983-03-10 Moving bed drum type coal burning boiler

Publications (1)

Publication Number Publication Date
JPS59164823A true JPS59164823A (en) 1984-09-18

Family

ID=12555797

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58039537A Pending JPS59164823A (en) 1983-03-10 1983-03-10 Moving bed drum type coal burning boiler

Country Status (1)

Country Link
JP (1) JPS59164823A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0352619A2 (en) * 1988-07-29 1990-01-31 MARTIN GmbH für Umwelt- und Energietechnik Process for regulating the firing power in combustion plants
FR2683027A1 (en) * 1991-10-25 1993-04-30 Pillard Chauffage LOAD REGULATION METHOD AND DEVICE FOR BOILER WITH MECHANICAL GRID.
CN112440403A (en) * 2019-08-30 2021-03-05 株式会社钟化 Apparatus and method for producing expanded beads

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0352619A2 (en) * 1988-07-29 1990-01-31 MARTIN GmbH für Umwelt- und Energietechnik Process for regulating the firing power in combustion plants
FR2683027A1 (en) * 1991-10-25 1993-04-30 Pillard Chauffage LOAD REGULATION METHOD AND DEVICE FOR BOILER WITH MECHANICAL GRID.
CN112440403A (en) * 2019-08-30 2021-03-05 株式会社钟化 Apparatus and method for producing expanded beads
CN112440403B (en) * 2019-08-30 2023-03-21 株式会社钟化 Apparatus and method for producing expanded beads

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