JPS6018883B2 - Soot blower control device - Google Patents

Soot blower control device

Info

Publication number
JPS6018883B2
JPS6018883B2 JP9911079A JP9911079A JPS6018883B2 JP S6018883 B2 JPS6018883 B2 JP S6018883B2 JP 9911079 A JP9911079 A JP 9911079A JP 9911079 A JP9911079 A JP 9911079A JP S6018883 B2 JPS6018883 B2 JP S6018883B2
Authority
JP
Japan
Prior art keywords
soot blower
heat transfer
boiler
transfer surface
exhaust gas
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
Application number
JP9911079A
Other languages
Japanese (ja)
Other versions
JPS5623611A (en
Inventor
昇 岩永
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 Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP9911079A priority Critical patent/JPS6018883B2/en
Publication of JPS5623611A publication Critical patent/JPS5623611A/en
Publication of JPS6018883B2 publication Critical patent/JPS6018883B2/en
Expired legal-status Critical Current

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  • Incineration Of Waste (AREA)

Description

【発明の詳細な説明】 本発明はスートブロワの制御装置に係り、特にボィラ装
置の各伝熱面と対応して複数設けられたスートブロワの
制御装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a control device for a soot blower, and particularly to a control device for a plurality of soot blowers provided corresponding to each heat transfer surface of a boiler device.

ボィラ装置を運転していると、炉内にある水壁管群など
の伝熱面に煤や灰などが付着・蓄積して、伝熱面におけ
る熱交換性能が悪くなり、その結果、ボィラ装置の効率
を低下させる。
When the boiler equipment is operated, soot and ash adhere and accumulate on the heat transfer surfaces such as the water wall tube group in the furnace, deteriorating the heat exchange performance of the heat transfer surfaces, and as a result, the boiler equipment reduce the efficiency of

そのため適当な時期にス−トブロワを運転して、伝熱面
に付着・蓄積している蝶などを除去する必要がある。従
来このスートブロワの運転は、ボィラ運転員がボィラ装
置の排ガス温度やドラフトを常に測定し、排ガス温度や
ドラフトが上昇すると運転員の経験と照らし合わせてス
ートブロワの運転の必要性を判断していた。
Therefore, it is necessary to operate the soot blower at an appropriate time to remove butterflies and the like that have adhered to and accumulated on the heat transfer surface. Conventionally, the soot blower was operated by a boiler operator who constantly measured the exhaust gas temperature and draft of the boiler equipment, and when the exhaust gas temperature or draft rose, the operator judged the necessity of operating the soot blower by comparing it with the operator's experience.

これはボィラ伝熱面の汚れと排ガス温度やドラフトが一
定の関係にあることから、排ガス温度やドラフトを測定
することによって伝熱面の汚れの程度を推定しているが
、実際には排ガス温度やドラフトなどはボィラの負荷、
すなわち蒸気発生量によって大きく変化するため、スー
トブロワの運転時期の判断はボィラ運転員の経験に頼ら
ざるを得なかった。このようなことから、判断に際して
運転員の個人差が出て、適正なスートブロワの運転がな
されないとボィラ装置の効率が低下する。
This is because there is a certain relationship between contamination on the boiler heat transfer surface and exhaust gas temperature and draft, so the degree of contamination on the heat transfer surface is estimated by measuring the exhaust gas temperature and draft, but in reality the degree of contamination on the heat transfer surface is estimated by measuring the exhaust gas temperature and draft. and draft etc. are the load on the boiler,
In other words, since it varies greatly depending on the amount of steam generated, the decision on when to operate the soot blower has had to rely on the experience of the boiler operator. For this reason, there are individual differences among operators when making decisions, and if the soot blower is not operated properly, the efficiency of the boiler device will decrease.

また運転員は常に排ガス温度やドラフトの変化を監視し
ておく必要があり、そのために時間的に束縛されてしま
い作業能率が悪い。これらを改善するために、通常は伝
熱面の汚れの程度にかかわらず定期的にスートブロワを
運転している。
In addition, operators must constantly monitor changes in exhaust gas temperature and draft, which limits their time and reduces work efficiency. In order to improve these problems, a soot blower is normally operated regularly regardless of the degree of dirt on the heat transfer surface.

しかしこの方法では、汚れの少ない伝熱面までも噴射媒
体(蒸気.空気)を使用して清掃するから、噴射媒体が
無駄になる。特にボィラ装置から発生した蒸気を噴射媒
体として使用する場合は、蒸気の減った分だけ補う必要
があり燃料を余計に必要とする。しかも汚れの少ない俵
熱面までも清掃するのであるから、ス−トブロワの運転
時間が長くかかり、そのためにボイラ装置の稼動率が下
がるなどの欠点がある。さらに、この欠点を解消するた
め、ボィラ装置の再熱器の蒸気温度を検出してバーナ頃
斜を制御し、所定のバーナ煩斜において炉壁に内張りさ
れた管群のうちの特定の管群をスートブローする手段が
、特公昭42一18斑6号公報に開示されている。
However, in this method, the injection medium (steam, air) is used to clean even the least contaminated heat transfer surface, which wastes the injection medium. In particular, when steam generated from a boiler device is used as an injection medium, it is necessary to compensate for the amount of steam that has been reduced, which requires additional fuel. Moreover, since even the hot surface of the bales, which is less contaminated, is cleaned, it takes a long time to operate the soot blower, which has disadvantages such as a reduction in the operating rate of the boiler system. Furthermore, in order to eliminate this drawback, the burner slope is controlled by detecting the steam temperature of the reheater of the boiler equipment, and a specific group of tubes from among the tube groups lined on the furnace wall at a predetermined burner slope is detected. A means for soot-blowing is disclosed in Japanese Patent Publication No. 42-18-18 No. 6.

しかしながら、このような手段は、バ−ナ鏡斜と当該管
群の蒸気温度との関係が一定の因果関係にあるから有効
であるのであって、当該管群以外の伝熱面、例えば、過
熱器、蒸発器、節炭器等のスートブローについてはこれ
を適用することができないという欠点を有する。本発明
の目的は、このような従来技術の欠点を解消し、スート
ブロワの運転時期ならびに各伝熱面のうちの清掃が必要
な伝熱面を正確に検知して、適正な清掃を行なうスート
ブロワの制御装贋を提供するにある。
However, such a method is effective because there is a certain causal relationship between the burner mirror slope and the steam temperature of the tube group, and it is effective because there is a certain causal relationship between the burner mirror tilt and the steam temperature of the tube group, and it is not possible to use heat transfer surfaces other than the tube group, such as overheating. This method has the disadvantage that it cannot be applied to soot blowing devices such as containers, evaporators, and economizers. The purpose of the present invention is to eliminate such drawbacks of the conventional technology, and to provide a soot blower that accurately detects the operating timing of the soot blower and which heat transfer surface requires cleaning among the heat transfer surfaces, and performs appropriate cleaning. There is a control device to provide counterfeiting.

この目的を達成するため、本発明は、ボィラ装置内の伝
熱面にそれぞれ対応して複数のスートブロヮとダスト付
着量を検出する汚れ度検出手段とを有し、各スートブロ
ワは個別に運転して対応する伝熱面を清掃することので
きるスートブロワを備えたものにおいて、前記ボィラ装
置の負荷条件別に塵道より排出される排ガス特性値の前
記ボィラ装置の効率に関連する許容限界値を記憶する記
憶部と、前記ボィラ装置の負荷条件と排ガス特性値とを
検出する検出部と、この検出部により検出された値が前
記許容限界値で定められる許容範囲外であるとき前記各
汚れ度検出手段に測定指令を与える測定指令出力手段と
、前記各汚れ度検出手段の検出値に基づいて所要のスー
トブロワに運転指令を与える運転指令出力手段とを設け
たことを特徴とする。
In order to achieve this object, the present invention has a plurality of soot blowers corresponding to each heat transfer surface in a boiler apparatus and a contamination degree detection means for detecting the amount of dust adhesion, and each soot blower is operated individually. In a device equipped with a soot blower capable of cleaning a corresponding heat transfer surface, a memory that stores permissible limit values related to the efficiency of the boiler device of exhaust gas characteristic values discharged from the dust path for each load condition of the boiler device. a detection unit that detects the load condition and exhaust gas characteristic value of the boiler device; and a detection unit that detects the load condition and exhaust gas characteristic value of the boiler device; The present invention is characterized in that it is provided with a measurement command output means for giving a measurement command, and an operation command output means for giving a driving command to a required soot blower based on the detection value of each of the dirt degree detection means.

以下、本発明の実施例を図面とともに説明する。Embodiments of the present invention will be described below with reference to the drawings.

ボィラ装置1の炉内には水壁管群などから構成4された
複数の例えば第1伝熱面2と第2伝熱面4が設けられて
おり、前記第1鎧熱面2には第1スートブロヮ3と第1
伝熱面2の排ガス上流側と下流側との差圧を測定する第
1差圧計12が、また前記第2民熱面4には第2スート
ブoヮ5と第2伝熱面4の差圧を測定する第2差圧計1
3がそれぞれ備えられている。
In the furnace of the boiler device 1, a plurality of, for example, a first heat transfer surface 2 and a second heat transfer surface 4, each of which is composed of a group of water wall tubes, etc., are provided. 1 soot blow 3 and 1
A first differential pressure gauge 12 is provided to measure the differential pressure between the upstream side and the downstream side of the exhaust gas on the heat transfer surface 2, and a pressure difference between the second soot tube 5 and the second heat transfer surface 4 is provided on the second civil heating surface 4. Second differential pressure gauge 1 that measures pressure
3 are provided respectively.

各スートブロワ3,6は個別に運転して対応する伝熱面
2,4を蒸気や空気などの噴射媒体で清掃することがで
きる。石油やガスなどの燃料は燃料配管8からボィラ装
置1のバーナ19に供給されて炉内で燃焼し、生成した
燃焼ガスは各伝熱面2,4を通り煙道10から排ガス2
0として排出される。
Each soot blower 3, 6 can be operated individually to clean the corresponding heat transfer surface 2, 4 with a jetting medium such as steam or air. Fuel such as oil or gas is supplied from the fuel pipe 8 to the burner 19 of the boiler device 1 and combusted in the furnace, and the generated combustion gas passes through each heat transfer surface 2 and 4 and flows from the flue 10 into the exhaust gas 2.
Emitted as 0.

この燃料の燃焼によってポィラ装置1の缶水21が加熱
され、蒸気22となって蒸気配管6を通って蒸気使用場
所へ送られる。前記燃料配管8には燃料の使用量を測定
する燃料流量計9が、蒸気配管6には蒸気発生量を測定
する蒸気流量計7が、塵道10には排ガス20の温度を
測定する排ガス温度計11とポイラ装置1のドラフト排
ガス20の圧力を測定するドラフト計18がそれぞれ配
設されている。そしてこれら燃料流量計9、蒸気流量計
7、排ガス温度計11、ドラフト計18はそれぞれ連続
的に測定を行なっており、それぞれの測定値は信号とし
てマイクロコンピュータからなる制御装魔23の比較判
断部24に入力される。制御装置23には他に記憶部2
5があり、ここには例えば蒸気発生量と使用燃料量との
関係、蒸気発生量と排ガス温度との関係、蒸気発生量と
ドラフトとの関係等のポィラ装置の効率に係わる実験デ
ータや計算値がまとめられ、当該効率に影響を与える要
因の1つとしての所謂伝熱面の汚れ許容限界を判断する
ためのデータが記憶されている。
The combustion of this fuel heats the canned water 21 in the boiler device 1, turns it into steam 22, and sends it through the steam pipe 6 to the place where the steam is used. The fuel pipe 8 has a fuel flow meter 9 that measures the amount of fuel used, the steam pipe 6 has a steam flow meter 7 that measures the amount of steam generated, and the dust pipe 10 has an exhaust gas temperature meter that measures the temperature of the exhaust gas 20. 11 and a draft gauge 18 for measuring the pressure of the draft exhaust gas 20 of the boiler device 1 are respectively provided. The fuel flow meter 9, the steam flow meter 7, the exhaust gas temperature meter 11, and the draft meter 18 each measure continuously, and each measured value is sent as a signal to the comparison judgment section of the control device 23 consisting of a microcomputer. 24. The control device 23 also includes a storage section 2.
5, which includes experimental data and calculated values related to the efficiency of the boiler, such as the relationship between the amount of steam generated and the amount of fuel used, the relationship between the amount of steam generated and the exhaust gas temperature, and the relationship between the amount of steam generated and draft. are compiled, and data for determining the so-called contamination tolerance limit of the heat transfer surface, which is one of the factors that affect the efficiency, is stored.

前述の使用燃料量、排ガス温度、ドラフトなどの伝熱面
の汚れに関係するボィラ特性は蒸気発生量別、すなわち
ボィラの負荷条件別にまとめて記憶されている。前述の
ように蒸気流量計7、燃料流量計9、排ガス温度計11
、ドラフト計18で実測された値は制御装置23の比較
判断部24に入力され、そのボイラ負荷条件(蒸気発生
量によって決められる)での実測した燃料使用量、排ガ
ス温度、ドラフト値などは前記記憶部25から入力され
たデー夕とそれぞれ照合される。
The boiler characteristics related to the amount of fuel used, exhaust gas temperature, contamination of heat transfer surfaces such as draft, etc., are collectively stored for each steam generation amount, that is, for each boiler load condition. As mentioned above, the steam flow meter 7, the fuel flow meter 9, the exhaust gas temperature meter 11
, the values actually measured by the draft meter 18 are input to the comparison/judgment section 24 of the control device 23, and the actually measured fuel usage amount, exhaust gas temperature, draft value, etc. under the boiler load condition (determined by the amount of steam generation) are as described above. The data inputted from the storage unit 25 are compared with each other.

ポィラ装置1を運転しているうちに伝熱面2,4に煤や
灰が付着・蓄積して汚れがひどくなると伝熱面2,4で
の伝熱効率が低下し、そのボィラ負荷条件での正常運転
時に比べて燃料使用量は増え、熱回収率が悪いから排ガ
ス温度は上昇し、燃料ガスの流れが悪くドラフト値も下
降する。従って比較判断部24で実測値とデータとを照
合することにより、実測した蒸気発生量の条件において
まず、ボィラ菱贋の効率を判断し、これにより、鏡熱面
2,4の汚れが許容限界に達しているか否かを自動的に
判断することができる。比較判断部24での比較演算結
果は、計器盤16に表示される。ボィラ運転員は、この
計器盤16の表示を見て伝熱面2,4の汚れが許容限界
に達しているか否かを知ることができる。
While the boiler device 1 is in operation, if soot and ash adhere to and accumulate on the heat transfer surfaces 2 and 4 and the dirt becomes severe, the heat transfer efficiency on the heat transfer surfaces 2 and 4 will decrease, and the boiler load conditions will deteriorate. Compared to normal operation, the amount of fuel used increases, the exhaust gas temperature rises due to the poor heat recovery rate, and the draft value decreases due to poor fuel gas flow. Therefore, by comparing the actual measurement value with the data in the comparison/judgment section 24, the efficiency of the boiler is determined under the conditions of the actually measured steam generation amount, and thereby the contamination of the mirror heating surfaces 2 and 4 is within the permissible limit. It is possible to automatically determine whether the target has been reached. The comparison calculation result in the comparison/judgment section 24 is displayed on the instrument panel 16. The boiler operator can see the display on the instrument panel 16 and know whether the dirt on the heat transfer surfaces 2 and 4 has reached the allowable limit.

この表示に基づいて運転員が制御装置23に差圧計12
,13の測定指令を与えるか、あるいは前述の比較判断
部24の比較判断結果により差圧計12,13の測定指
令を自動的に与える。差圧計12,13によってそれぞ
れの伝熱面2,4の差圧が測定される。
Based on this display, the operator controls the differential pressure gauge 12 to the control device 23.
. Differential pressures on the respective heat transfer surfaces 2 and 4 are measured by differential pressure gauges 12 and 13.

蝶などの付着量が多いとその伝熱面での燃焼ガスの流動
抵抗が大きくなるから、伝熱面の上流側と下流側とでは
大きな圧力差が生じる。従って差圧計12,13での測
定によって清掃が必要な伝熱面2あるし、は(および)
4を特定することができ、その結果に基づいて伝熱面2
あるし・は(および)4に対応するス−トブロワ3ある
し、は(および)5に指令盤15から運転指令を与え、
噴射媒体で付着している煤などを吹き落して清掃する。
勿論、他の原因によりボィラ装置の効率が低下している
場合には、各差圧計の測定圧力は小さく、この場合スー
トブロワの運転指令は出力されない。
If there is a large amount of butterflies attached, the flow resistance of the combustion gas on the heat transfer surface will increase, so a large pressure difference will occur between the upstream and downstream sides of the heat transfer surface. Therefore, there is a heat transfer surface 2 that requires cleaning according to the measurement with the differential pressure gauges 12 and 13.
4 can be specified, and based on the result, the heat transfer surface 2
Give operating commands from the command panel 15 to the soot blowers 3 and 5 corresponding to the soot blowers 3 and 4;
Clean by blowing away the soot, etc. that has adhered to it with the spray medium.
Of course, if the efficiency of the boiler device is reduced due to other causes, the pressure measured by each differential pressure gauge will be small, and in this case no soot blower operation command will be output.

また制御菱鷹23に入力された各測定値は一定時間ごと
に記録装置17に記録されるとともに、スートブロワ3
,5の運転前と運転後の各測定値もあわせて記録されて
いる。
In addition, each measurement value inputted to the control unit 23 is recorded in the recording device 17 at regular intervals, and the soot blower 3
, 5 before and after operation are also recorded.

スートブロワの運転時期、即ち、ボィラ装置の効率低下
を検出するのに、伝熱面の汚れに関係するボィラ特性の
うち1つの特性を測定しても前記検出は可能であるが、
2つ以上の特性を合わせて測定する方が判断の正確性が
増すから望ましい。
In order to detect the operating timing of the soot blower, that is, a decrease in the efficiency of the boiler device, it is possible to detect the above by measuring one of the boiler characteristics related to dirt on the heat transfer surface.
It is desirable to measure two or more characteristics together because it increases the accuracy of judgment.

本発明は前述のような構成になっており、スートブロワ
の運転時期が正確に把握でき、しかも清掃の必要な伝熱
面が特定できるから、効率の良いスートプロワ運転が行
なわれ、しかも噴射媒体の損失を軽減し、ボィラ装置の
改善が図れる。
The present invention has the above-described configuration, and since it is possible to accurately determine the operating timing of the soot blower and to identify the heat transfer surface that requires cleaning, the soot blower can be operated efficiently and the loss of the injection medium can be reduced. It is possible to improve the boiler equipment.

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

図は本発明の実施例に係るスートブロワの制御方式を説
明するための概略構成図である。 1・・・・・・ボイラ装置、2,4・・・・・・伝熱面
、3,5・・・・・・スートブロワ、12,13・・・
・・・差圧計、22・・・・・・蒸気、23・・・・・
・制御装置、24・・・・・・比較判断部、25・・・
・・・記憶部。
The figure is a schematic configuration diagram for explaining a control method of a soot blower according to an embodiment of the present invention. 1... Boiler device, 2, 4... Heat transfer surface, 3, 5... Soot blower, 12, 13...
...Differential pressure gauge, 22...Steam, 23...
-Control device, 24... Comparison/judgment section, 25...
...Memory department.

Claims (1)

【特許請求の範囲】[Claims] 1 ボイラ装置内の伝熱面にそれぞれ対応して複数のス
ートブロワとダスト付着量を検出する汚れ度検出手段と
を有し、各スートブロワは個別に運転して対応する伝熱
面を清掃することのできるスートブロワを備えたものに
おいて、前記ボイラ装置の負荷条件別に煙道より排出さ
れる排ガス特性値の前記ボイラ装置の効率に関連する許
容限界値を記憶する記憶部と、前記ボイラ装置の負荷条
件と排ガス特性値とを検出する検出部と、この検出部に
より検出された値が前記許容限界値で定められる許容範
囲外であるとき前記各汚れ度検出手段に測定指令を与え
る測定指令出力手段と、前記各汚れ度検出手段の検出値
に基づいて所要のスートブロワに運転指令を与える運転
指令出力手段とを設けたことを特徴とするスートブロワ
の制御装置。
1 It has a plurality of soot blowers corresponding to each heat transfer surface in the boiler equipment and a contamination degree detection means for detecting the amount of dust adhesion, and each soot blower is operated individually to clean the corresponding heat transfer surface. In the soot blower, the storage unit stores permissible limit values related to the efficiency of the boiler device of characteristic values of exhaust gas discharged from the flue according to the load conditions of the boiler device; a detection unit that detects an exhaust gas characteristic value; and a measurement command output unit that issues a measurement command to each of the dirt level detection units when the value detected by the detection unit is outside the tolerance range defined by the tolerance limit value; A control device for a soot blower, comprising operation command output means for giving an operation command to a required soot blower based on the detection value of each of the dirt level detection means.
JP9911079A 1979-08-04 1979-08-04 Soot blower control device Expired JPS6018883B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9911079A JPS6018883B2 (en) 1979-08-04 1979-08-04 Soot blower control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9911079A JPS6018883B2 (en) 1979-08-04 1979-08-04 Soot blower control device

Publications (2)

Publication Number Publication Date
JPS5623611A JPS5623611A (en) 1981-03-06
JPS6018883B2 true JPS6018883B2 (en) 1985-05-13

Family

ID=14238678

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9911079A Expired JPS6018883B2 (en) 1979-08-04 1979-08-04 Soot blower control device

Country Status (1)

Country Link
JP (1) JPS6018883B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59215502A (en) * 1983-05-20 1984-12-05 堺市 Waste-heat boiler
JPS6031759A (en) * 1983-08-01 1985-02-18 帝人株式会社 Deodorising padding
JPS6071815A (en) * 1983-09-28 1985-04-23 Hitachi Zosen Corp Water spouting type soot blower of exhaust gas economizer
JPH02125992U (en) * 1988-12-29 1990-10-17

Also Published As

Publication number Publication date
JPS5623611A (en) 1981-03-06

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