JPH05322155A - Fuel supply control device in combustion device - Google Patents
Fuel supply control device in combustion deviceInfo
- Publication number
- JPH05322155A JPH05322155A JP12484092A JP12484092A JPH05322155A JP H05322155 A JPH05322155 A JP H05322155A JP 12484092 A JP12484092 A JP 12484092A JP 12484092 A JP12484092 A JP 12484092A JP H05322155 A JPH05322155 A JP H05322155A
- Authority
- JP
- Japan
- Prior art keywords
- rate
- fuel
- flow rate
- control system
- 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.)
- Pending
Links
Landscapes
- Feeding And Controlling Fuel (AREA)
- Combustion Of Fluid Fuel (AREA)
- Flow Control (AREA)
- Control Of Non-Electrical Variables (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は微粉炭等の微粉燃料と液
体、気体等の流体燃料を同時に燃焼させる混焼型ボイ
ラ、加熱炉等の燃焼装置の燃料供給制御装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel supply control device for a combustion apparatus such as a co-firing type boiler and a heating furnace for simultaneously burning pulverized fuel such as pulverized coal and fluid fuel such as liquid or gas.
【0002】[0002]
【従来の技術】従来、例えば微粉炭と重油を同時に燃焼
させて蒸気を発生させる混焼型ボイラにおいては、これ
らの燃料の供給量を調節して蒸気圧力を一定に保つよう
にしている。2. Description of the Related Art Conventionally, for example, in a co-firing type boiler that simultaneously combusts pulverized coal and heavy oil to generate steam, the supply amount of these fuels is adjusted to keep the steam pressure constant.
【0003】図3はかかるボイラの燃料供給制御系を示
すものである。図3において、1はボイラで、このボイ
ラ1にはタンク2より搬送部3に切出された微粉炭がブ
ロア4により燃料搬送ライン5を通して供給されると共
に、図示しない重油タンク側より燃料供給ライン6を通
して重油が供給されるようになっている。この場合、タ
ンク2の下部にはモータ7により駆動されて微粉炭の切
出量を制御する切出量制御機構8が設けられ、また燃料
供給ライン6には流量制御弁9が設けられている。FIG. 3 shows a fuel supply control system for such a boiler. In FIG. 3, reference numeral 1 denotes a boiler, and the boiler 1 is supplied with pulverized coal cut out from a tank 2 to a conveying section 3 by a blower 4 through a fuel conveying line 5, and a fuel supply line from a heavy oil tank side (not shown). The heavy oil is supplied through No. 6. In this case, a cutout amount control mechanism 8 that is driven by a motor 7 to control the cutout amount of pulverized coal is provided in the lower portion of the tank 2, and a flow rate control valve 9 is provided in the fuel supply line 6. ..
【0004】一方、10はボイラから発生した蒸気圧力
を一定に保つための負荷指令、つまり燃料増減指令を出
す負荷調節器で、この負荷調節器10から出された燃料
増減指令は比率設定器11により設定された基準混焼率
に基づき配分する配分器12,13を通して流量調節計
14,15に設定値として入力される。この流量調節計
14は配分器12より入力される設定値に基づいてモー
タ7を制御することにより微粉炭の切出量を制御し、ま
た流量調節計15は配分器13より入力される設定値と
燃料供給ライン6に設けられた重油流量検出器16によ
り検出された流量との偏差により流量制御弁8を調節す
ることにより重油の供給量を制御する。On the other hand, 10 is a load controller for issuing a load command for keeping the steam pressure generated from the boiler constant, that is, a fuel increase / decrease command. The fuel increase / decrease command issued from this load controller 10 is the ratio setter 11 It is input as a set value to the flow rate controllers 14 and 15 through the distributors 12 and 13 which distribute based on the standard mixed combustion rate set by. The flow rate controller 14 controls the amount of pulverized coal cut out by controlling the motor 7 based on the set value input from the distributor 12, and the flow rate controller 15 sets the set value input from the distributor 13. And the flow rate detected by the heavy oil flow rate detector 16 provided in the fuel supply line 6 is adjusted to adjust the flow rate control valve 8 to control the supply amount of heavy oil.
【0005】ところで、このようなボイラの燃料供給制
御系においては、負荷調節器10から出される同一指令
により,燃料供給ライン及び重油供給ラインを通して微
粉炭及び重油がボイラ1に供給されるが、これらの燃料
は粉末燃料と液体燃料のため、燃料供給の追従速度の違
いにより位相ずれが発生する。In the fuel supply control system of such a boiler, pulverized coal and heavy oil are supplied to the boiler 1 through the fuel supply line and the heavy oil supply line according to the same command issued from the load controller 10. Since the fuel is a powder fuel and a liquid fuel, a phase shift occurs due to the difference in the following speeds of fuel supply.
【0006】図4は燃料指令に対する各燃料の応答波形
を示すものである。この応答波形からも分かるように、
微粉炭は切出量制御による搬送量変化であり、重油は圧
送による流量変化であるため、微粉炭よりも追従性に優
れている。FIG. 4 shows a response waveform of each fuel in response to a fuel command. As you can see from this response waveform,
Pulverized coal has a better changeability than pulverized coal because it has a change in the amount conveyed by controlling the cut-out amount and changes in the flow rate of heavy oil due to pressure feeding.
【0007】[0007]
【発明が解決しようとする課題】このように従来の燃料
供給制御装置においては、負荷調節器10より出される
同一指令により微粉炭の切出量および重油の供給流量を
制御しているため、これら燃料供給の追従速度の大きな
差により微粉炭及び重油がボイラ1に供給されるまでに
位相ずれが生じ、結果的に外乱の発生により制御不安定
となる。As described above, in the conventional fuel supply control device, the cutting amount of the pulverized coal and the supply flow rate of the heavy oil are controlled by the same command issued from the load controller 10. Due to a large difference in follow-up speed of fuel supply, a phase shift occurs until pulverized coal and heavy oil are supplied to the boiler 1, and as a result, disturbance causes control instability.
【0008】本発明は、微粉燃料と液体または気体等の
流体燃料との時間の応答遅れによる位相ずれを解消して
外乱の発生を防止し、負荷変動時の燃料供給制御を安定
に行うことができる燃焼装置の燃料供給制御装置を提供
することを目的とする。The present invention eliminates the phase shift due to the response delay of the time between the fine powder fuel and the fluid fuel such as liquid or gas to prevent the occurrence of disturbance and to stably control the fuel supply when the load changes. An object of the present invention is to provide a fuel supply control device for a combustion device that can be used.
【0009】[0009]
【課題を解決するための手段】本発明は上記の目的を達
成するため、負荷調節器より出される負荷指令を基準混
焼率に基づいて配分し、これを設定値として微粉燃料制
御系の流量調節計および流体燃料制御系の流量調節計に
与えて燃焼装置に供給される微粉燃料流量および流体燃
料流量を制御するようにした燃料供給制御装置におい
て、前記各燃料制御系の流量調節計より出力される制御
指令値をそれぞれ取込んで微粉燃料の実混焼率を求める
演算器と、この演算器により求められた微粉燃料の実混
焼率と前記基準混焼率とを比較して実混焼率が基準混焼
率に対してある範囲内にあるか否かを判定する比較器
と、前記微粉燃料制御系の前記流量調節計の入力側に設
けられ前記比較器により実混焼率が基準混焼率に対して
ある範囲内にあると判定されると前記微粉燃料制御系の
流量調節計に入力される設定値を固定する保持器とを備
えたものである。In order to achieve the above object, the present invention distributes a load command issued from a load controller based on a standard co-firing rate, and uses this as a set value to adjust the flow rate of a fine powder fuel control system. And a flow rate controller of the fluid fuel control system to control the flow rate of the fine powder fuel and the flow rate of the fluid fuel supplied to the combustion device, the flow rate controller of each fuel control system outputs The actual mixed combustion ratio of the fine fuel and the reference mixed combustion ratio are calculated by comparing the actual mixed combustion ratio of the fine fuel obtained by this calculator with the reference mixed combustion ratio. A comparator for determining whether or not it is within a certain range with respect to the rate, and the actual mixed combustion rate with respect to the reference mixed combustion rate provided by the comparator provided on the input side of the flow rate controller of the fine powder fuel control system. Determined to be within range It is obtained and a cage for fixing the set value input to the flow controllers of the pulverized fuel control system to be.
【0010】[0010]
【作用】このような構成の燃料供給制御装置にあって
は、演算器で求められた実混焼率が基準混焼率に対して
ある範囲内にあるときは微粉燃料制御系の流量調節計に
入力される設定値が固定されるので、設定値の変更頻度
が極力少なくなり、微粉燃料と流体燃料との時間の応答
遅れによる位相ずれが解消されるので、外乱の発生を防
止することが可能となり、負荷変動に追従した燃焼供給
制御を安定に行うことができる。In the fuel supply control device having such a structure, when the actual mixed combustion ratio calculated by the arithmetic unit is within a certain range with respect to the reference mixed combustion ratio, it is input to the flow rate controller of the fine powder fuel control system. Since the set value that is set is fixed, the frequency of changing the set value is reduced as much as possible, and the phase shift due to the response delay of the fine fuel and the fluid fuel is eliminated, so it is possible to prevent the occurrence of disturbance. Therefore, the combustion supply control that follows the load fluctuation can be stably performed.
【0011】[0011]
【実施例】以下本発明の一実施例を図面を参照して説明
する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.
【0012】図1は本発明による燃焼装置の燃料供給制
御装置の一例を示す系統構成図で、図3と同一部分には
同一符号を付してその説明を省略し、ここでは異なる点
についてのみ述べる。FIG. 1 is a system configuration diagram showing an example of a fuel supply control device for a combustion apparatus according to the present invention. The same parts as those in FIG. 3 are designated by the same reference numerals and the description thereof will be omitted. Here, only different points will be described. State.
【0013】本実施例では、図1に示すように流量調節
計14より出力される微粉炭切出量指令値と流量調節計
15より出力される重油流量指令値とを取込んで微粉炭
の実混焼率を求める演算器17、比率設定器11により
設定された微粉炭の基準混焼率と演算器17により求め
られた微粉炭の実混焼率とを比較し、微粉炭の実混焼率
が微粉炭の基準混焼率に対して所定の範囲内にあるかど
うかを判定する比較器18及び配分器12で配分された
燃料増減指令が入力され、比較器18により微粉炭の混
焼率が微粉炭の基準混焼率に対して所定の範囲内にある
と判定されると燃料増減指令負荷指令を固定する保持器
19をそれぞれ設け、微粉炭流量制御系を粗調整用と
し、重油燃料流量制御系を微調整用として機能させるよ
うにしたものである。次にこのように構成された燃料供
給制御装置の作用について述べる。In this embodiment, as shown in FIG. 1, the flow rate is adjusted.
Pulverized coal cutting amount command value output from total 14 and flow controller
Pulverized coal by incorporating the heavy oil flow rate command value output from 15
With the calculator 17 and the ratio setter 11 for obtaining the actual mixed burning rate of
Calculated by the standard co-firing rate of the pulverized coal set and the calculator 17.
The actual co-firing rate of the pulverized coal is compared to the actual co-firing rate of the pulverized coal.
Is within the specified range for the standard co-firing rate of pulverized coal
It is distributed by the comparator 18 and the distributor 12 for judging whether
The fuel increase / decrease command is input, and the comparator 18 mixes the pulverized coal.
The burning rate is within the specified range with respect to the standard mixed burning rate of pulverized coal
Retainer that fixes the fuel increase / decrease command load command when it is determined that
19 are provided respectively, and the pulverized coal flow rate control system is for coarse adjustment.
The heavy oil fuel flow control system to function as a fine adjustment.
It is a scam. Next, the fuel supply configured in this way
The operation of the feed control device will be described.
【0014】負荷調節器10よりボイラ1から発生した
蒸気圧力が一定に保たれるように燃料増減指令が出され
ると、この燃料増減指令は比率設定器1により設定され
た基準混焼率に基づき配分器12、13により配分さ
れ、流量調節計14及び15に設定値としてそれぞれ与
えられる。この場合、演算器17では流量調節計14及
び15より出力される流量増減指令A,Bに基づいて微
粉炭の実混焼率をA/(A+B)により計算し、その値
を比較器18に入力する。この比較器18では、微粉炭
の実混焼率βと比率設定器11で設定された基準混焼率
αとを比較し、この微粉炭の実混焼率βが基準混焼率α
に対して(a,−b)の範囲内にあるか否かを判定し、
範囲内になければ従来同様に比率設定器11で設定され
た基準混焼率に基づく微粉炭増減指令を保持器19を通
して流量調節計14に設定値として与え、また範囲内に
あれば保持器19に保持指令を与えて配分器12より入
力される微粉炭増減指令値を固定し、これを流量調節計
14に設定値として与えることにより微粉炭の切出量が
一定になる。When the load controller 10 issues a fuel increase / decrease command so that the steam pressure generated from the boiler 1 is kept constant, the fuel increase / decrease command is distributed based on the reference mixed combustion rate set by the ratio setter 1. It is distributed by the devices 12 and 13 and is given to the flow controllers 14 and 15 as set values, respectively. In this case, the calculator 17 calculates the actual mixed combustion rate of the pulverized coal by A / (A + B) based on the flow rate increase / decrease commands A and B output from the flow rate controllers 14 and 15, and inputs the value to the comparator 18. To do. In this comparator 18, the actual mixed combustion rate β of the pulverized coal is compared with the reference mixed combustion rate α set by the ratio setting device 11, and the actual mixed combustion rate β of the pulverized coal is determined by the reference mixed combustion rate α.
For (a, -b) is determined whether or not,
If it is not within the range, a pulverized coal increase / decrease command based on the standard mixed combustion rate set by the ratio setter 11 is given to the flow rate controller 14 as a set value through the retainer 19 as in the conventional case. By giving a holding command to fix the pulverized coal increase / decrease command value input from the distributor 12, and by giving this to the flow rate controller 14 as a set value, the amount of pulverized coal cut out becomes constant.
【0015】従って、微粉炭実投入比率βがある範囲
(a,−b)内にあるときは、流量調節計15のみが配
分器13により基準混焼率に基づいて配分された重油増
減指令に追従して重油の供給流量を制御することによ
り、ボイラ1の蒸気圧力が設定値にコントロールされ
る。このように微粉炭制御系の流量調節計14は粗調整
用として機能し、重油制御系の流量調節計15は微徴用
として機能する。Therefore, when the pulverized coal actual input ratio β is within a certain range (a, -b), only the flow controller 15 follows the heavy oil increase / decrease command distributed by the distributor 13 based on the standard mixed combustion rate. Then, by controlling the supply flow rate of the heavy oil, the steam pressure of the boiler 1 is controlled to the set value. As described above, the flow rate controller 14 of the pulverized coal control system functions for coarse adjustment, and the flow rate controller 15 of the heavy oil control system functions for fine adjustment.
【0016】図2は負荷調節器10から出される燃料増
減指令と微粉炭制御系の流量調節計14および重油制御
系の流量調節計15の応答を示すタイムチャートであ
る。このタイムチャートからも分かるように、微粉炭の
実混焼率βが比率設定器で設定された基準混焼率αに対
してある範囲(a,−b)内にあれば粗調整用の負荷指
令に変化はないが、ある範囲(a,−b)外になると一
定速度で微粉炭の切出量が変化するように制御される。FIG. 2 is a time chart showing the fuel increase / decrease command issued from the load controller 10 and the response of the flow controller 14 of the pulverized coal control system and the flow controller 15 of the heavy oil control system. As can be seen from this time chart, if the actual co-firing rate β of pulverized coal is within a certain range (a, -b) with respect to the reference co-firing rate α set by the ratio setter, the load command for coarse adjustment is set. Although there is no change, when it is outside a certain range (a, -b), the cut amount of pulverized coal is controlled so as to change at a constant speed.
【0017】このように本実施例では、負荷調節器10
より出される燃料増減指令を配分器12,13により比
率設定器11で設定された基準混焼率αに基づいて配分
し、これを設定値として微粉炭制御系の流量調節計14
および重油制御系1の流量調節計15に与えてボイラ1
へ供給される微粉炭の切出量および重油流量を制御する
燃料供給制御装置において、流量調節計14,15より
出力される流量増減指令値A,Bを演算器17に与えて
微粉炭の実混焼率βを求め、これを比較器18に与えて
比率設定器11で設定された基準混焼率αと比較して微
粉炭の実混焼率βが基準混焼率に対してある範囲(a,
−b)内にあるか否かを判定し、範囲内にあれば配分器
12より流量調節計14に設定値として入力される微粉
炭増減指令値を保持器19により固定するようにしたの
で、微粉炭制御系の流量調節計14の設定値の変更頻度
を極力少なくすることができ、負荷調節器10より出さ
れる燃料増減指令と流量調節計14により制御される微
粉炭の切出量との間に位相ずれがなくなり、負荷変動に
追従した燃料供給制御を安定に行うことができ、ボイラ
1から安定した蒸気圧力を得ることができる。Thus, in this embodiment, the load adjuster 10
The fuel increase / decrease command issued by the distributor is distributed by the distributors 12 and 13 based on the reference mixed combustion rate α set by the ratio setting device 11, and the flow controller 14 of the pulverized coal control system is used as the set value.
And the boiler 1 by giving it to the flow rate controller 15 of the heavy oil control system 1.
In the fuel supply control device for controlling the amount of cut pulverized coal and the flow rate of heavy oil supplied to the pulverized coal, the flow rate increase / decrease command values A and B output from the flow rate controllers 14 and 15 are given to the calculator 17 to determine the actual pulverized coal. The co-firing rate β is determined, and this is given to the comparator 18 and compared with the reference co-firing rate α set by the ratio setting device 11, and the actual co-firing rate β of the pulverized coal is within a range (a,
-B) is determined, and if it is within the range, the pulverized coal increase / decrease command value input as a set value from the distributor 12 to the flow rate controller 14 is fixed by the retainer 19. The frequency of changing the set value of the flow rate controller 14 of the pulverized coal control system can be reduced as much as possible, and the fuel increase / decrease command issued from the load controller 10 and the cut amount of the pulverized coal controlled by the flow rate controller 14 can be controlled. There is no phase shift between them, fuel supply control that follows load changes can be performed stably, and stable steam pressure can be obtained from the boiler 1.
【0018】[0018]
【発明の効果】以上述べたように本発明によれば、微粉
燃料と液体または気体等の流体燃料との時間の応答遅れ
による位相ずれを解消して外乱の発生を防止し、負荷変
動時の燃料供給制御を安定に行うことができる燃焼装置
の燃料供給制御装置を提供できる。As described above, according to the present invention, the phase shift due to the response delay in time between the fine powder fuel and the fluid fuel such as liquid or gas is eliminated to prevent the occurrence of disturbance and to prevent the occurrence of disturbance. It is possible to provide a fuel supply control device for a combustion device that can stably perform fuel supply control.
【図1】本発明による燃料供給制御装置の一実施例を示
す系統構成図。FIG. 1 is a system configuration diagram showing an embodiment of a fuel supply control device according to the present invention.
【図2】同実施例の作用を説明するためのタイムチャー
トを示す図。FIG. 2 is a view showing a time chart for explaining the operation of the embodiment.
【図3】従来の燃料供給制御装置を示す系統構成図。FIG. 3 is a system configuration diagram showing a conventional fuel supply control device.
【図4】同装置の作用を説明するためのタイムチャート
を示す図。FIG. 4 is a view showing a time chart for explaining the operation of the apparatus.
1……ボイラ、2……タンク、3……搬送部、4……ブ
ロア、5……燃料搬送ライン、6……燃料供給ライン、
7……モータ、8……切出量制御機構、9……流量制御
弁、10……負荷調節器、1……比率設定器、12,1
3……配分器、14,15……流量調節計、16……重
油流量検出器、17……演算器、18……比較器、19
……保持器。1 ... boiler, 2 ... tank, 3 ... conveying section, 4 ... blower, 5 ... fuel conveying line, 6 ... fuel supply line,
7 ... Motor, 8 ... Cutting amount control mechanism, 9 ... Flow control valve, 10 ... Load controller, 1 ... Ratio setting device, 12, 1
3 ... Distributor, 14, 15 ... Flow rate controller, 16 ... Heavy oil flow rate detector, 17 ... Computing unit, 18 ... Comparator, 19
…… Cage.
Claims (1)
混焼率に基づいて配分し、これを設定値として微粉燃料
制御系の流量調節計および流体燃料制御系の流量調節計
に与えて燃焼装置に供給される微粉燃料流量および流体
燃料流量を制御するようにした燃料供給制御装置におい
て、前記各燃料制御系の流量調節計より出力される制御
指令値をそれぞれ取込んで微粉燃料の実混焼率を求める
演算器と、この演算器により求められた微粉燃料の実混
焼率と前記基準混焼率とを比較して実混焼率が基準混焼
率に対してある範囲内にあるか否かを判定する比較器
と、前記微粉燃料制御系の前記流量調節計の入力側に設
けられ前記比較器により実混焼率が基準混焼率に対して
ある範囲内にあると判定されると前記微粉燃料制御系の
流量調節計に入力される設定値を固定する保持器とを備
えたことを特徴とする燃焼装置の燃料供給制御装置。1. A combustor in which a load command issued from a load controller is distributed based on a reference co-firing rate and is given to a flow controller of a fine fuel control system and a flow controller of a fluid fuel control system as a set value. In the fuel supply control device for controlling the flow rate of the fine powder fuel and the flow rate of the fluid fuel supplied to the fuel cell, the control command values output from the flow rate controller of each fuel control system are respectively taken in to obtain the actual mixed combustion rate of the fine fuel powder. By comparing the actual mixed combustion rate of the pulverized fuel obtained by this arithmetic unit with the reference mixed combustion rate to determine whether the actual mixed combustion rate is within a certain range with respect to the reference mixed combustion rate. A comparator and the pulverized fuel control system is provided on the input side of the flow rate controller, and when the comparator determines that the actual co-firing rate is within a certain range with respect to the reference co-firing rate, the pulverized fuel control system Input to the flow controller And a retainer for fixing a set value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12484092A JPH05322155A (en) | 1992-05-18 | 1992-05-18 | Fuel supply control device in combustion device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12484092A JPH05322155A (en) | 1992-05-18 | 1992-05-18 | Fuel supply control device in combustion device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05322155A true JPH05322155A (en) | 1993-12-07 |
Family
ID=14895396
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12484092A Pending JPH05322155A (en) | 1992-05-18 | 1992-05-18 | Fuel supply control device in combustion device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05322155A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017090019A (en) * | 2015-11-16 | 2017-05-25 | 大阪瓦斯株式会社 | Powder combustion device and powder combustion method |
-
1992
- 1992-05-18 JP JP12484092A patent/JPH05322155A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017090019A (en) * | 2015-11-16 | 2017-05-25 | 大阪瓦斯株式会社 | Powder combustion device and powder combustion method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7513117B2 (en) | Method for operating a furnace | |
US4798531A (en) | Process and apparatus for the control of the air and fuel supply to a plurality of burners | |
US4278052A (en) | Boiler control system | |
US3159345A (en) | Control system for utilization of variable flow fuel | |
US2093122A (en) | Combustion control | |
JPH05322155A (en) | Fuel supply control device in combustion device | |
US3481538A (en) | Boiler control apparatus | |
JPS63286614A (en) | Combustion control of boller | |
US4113418A (en) | Rotary burner control | |
JPH07280256A (en) | In-furnace pressure controlling method for burning furnace | |
JP2551411B2 (en) | Multistage control type air-fuel ratio control method and apparatus in combustion apparatus | |
JP3132977B2 (en) | Fuel control device for heavy oil / emulsion mixed-fired boiler | |
JPH11159756A (en) | Water injection control device for oil fired dln combustor | |
JPS62276318A (en) | Mill outlet temperature control method | |
JPH0412329Y2 (en) | ||
JPS5895118A (en) | Method for controlling steam temperature | |
JPS5813809B2 (en) | Combustion control method using low excess air | |
JPS6021639Y2 (en) | Furnace pressure control device for combustion equipment | |
JPS6246123A (en) | Sox concentration control method in high speed fluidized bed boiler | |
JPH01305215A (en) | Pulverized coal feed device | |
SU580402A1 (en) | Device for automatic control of uniflow steam boiler | |
SU471493A1 (en) | Fuel-air ratio control system | |
JPH11337049A (en) | Control method and apparatus for controlling mill primary air damper of a pulverized coal fired boiler | |
JPH0160734B2 (en) | ||
JPH0451722B2 (en) |