JPH0561521B2 - - Google Patents

Info

Publication number
JPH0561521B2
JPH0561521B2 JP12003081A JP12003081A JPH0561521B2 JP H0561521 B2 JPH0561521 B2 JP H0561521B2 JP 12003081 A JP12003081 A JP 12003081A JP 12003081 A JP12003081 A JP 12003081A JP H0561521 B2 JPH0561521 B2 JP H0561521B2
Authority
JP
Japan
Prior art keywords
auxiliary steam
boiler
pressure
reducing valve
pressure reducing
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 - Lifetime
Application number
JP12003081A
Other languages
Japanese (ja)
Other versions
JPS5822805A (en
Inventor
Koji Yamamoto
Hiromi Kamogawa
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 JP12003081A priority Critical patent/JPS5822805A/en
Publication of JPS5822805A publication Critical patent/JPS5822805A/en
Publication of JPH0561521B2 publication Critical patent/JPH0561521B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はボイラ装置に係り、特に単数または複
数の他のボイラ装置(以下、他缶と称す)から補
助蒸気が供給できる機構を備えたボイラ装置に関
する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a boiler device, and particularly to a boiler equipped with a mechanism that allows auxiliary steam to be supplied from one or more other boiler devices (hereinafter referred to as other boiler devices). Regarding equipment.

〔従来の技術〕[Conventional technology]

第1図は、従来のこの種ボイラ装置の補助蒸気
系統図である。
FIG. 1 is an auxiliary steam system diagram of a conventional boiler device of this type.

この図において、1は補助蒸気の供給を受けよ
うとする本ボイラ装置の補助蒸気ヘツダで、他缶
の1つである1号他缶2との間は第1供給管3で
接続されている。また、他缶の1つである2号他
缶4と補助蒸気ヘツダ1との間は第2供給管5で
接続されている。
In this figure, 1 is the auxiliary steam header of this boiler device which is going to receive the supply of auxiliary steam, and it is connected to No. 1, which is one of the other cans, and the other can 2 through the first supply pipe 3. . Further, a second supply pipe 5 is connected between the No. 2 other can 4, which is one of the other cans, and the auxiliary steam header 1.

第1供給管3の途中には第1減圧弁6と第1圧
力調節計7が、また、第2供給管5の途中には第
2減圧弁8と第2圧力調節計9がそれぞれ付設さ
れている。図に示すように、第1圧力調節計7は
第1減圧弁6の出口側に、第2圧力調節計9は第
2減圧弁8の出口側にそれぞれ配置され、第1お
よび第2圧力調節弁7,9で検出される圧力信号
に基づいて第1および第2減圧弁6,8で簡単な
開度調節を行うようになつている。
A first pressure reducing valve 6 and a first pressure regulator 7 are provided in the middle of the first supply pipe 3, and a second pressure reducing valve 8 and a second pressure regulator 9 are provided in the middle of the second supply pipe 5. ing. As shown in the figure, the first pressure regulator 7 is disposed on the outlet side of the first pressure reducing valve 6, and the second pressure regulator 9 is disposed on the outlet side of the second pressure reducing valve 8. Based on the pressure signals detected by the valves 7 and 9, the opening degree of the first and second pressure reducing valves 6 and 8 is simply adjusted.

この従来のものでは、各々の他缶2,4から補
助蒸気ヘツダ1に流入する補助蒸気量の制限は考
慮されておらず、他缶2,4の運転状態に関係な
く、第1および第2減圧弁6,8の出口側圧力が
一定になるように制御されていた。
This conventional method does not take into consideration the restriction of the amount of auxiliary steam flowing into the auxiliary steam header 1 from each of the other cans 2 and 4, and the first and second The pressure on the outlet side of the pressure reducing valves 6 and 8 was controlled to be constant.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

ところがこの制御方式では、各ボイラ装置は運
転状態が異なるため、他缶よりの補助蒸気の取出
し量を最適に配分することができず、各種のトラ
ブルを生じる。
However, in this control method, since each boiler device has a different operating state, it is not possible to optimally allocate the amount of auxiliary steam taken out from other cans, resulting in various troubles.

本発明の目的は、このような従来技術の欠点を
解消し、適正な補助蒸気の供給ができるボイラ装
置を提供するにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a boiler device that can overcome the drawbacks of the prior art and can appropriately supply auxiliary steam.

〔課題を解決するための手段〕[Means to solve the problem]

この目的を達成するため、本発明は、 他のボイラ装置から水蒸気の補給ができる補助
蒸気供給経路を備えたものにおいて、 前記水蒸気の補給ができる他のボイラ装置が複
数あり、 補助蒸気供給経路制御系に、前記各ボイラ装置
の運転状態などを考慮して各ボイラ装置からの補
助蒸気供給比率をそれぞれ割り当てることのでき
る比率設定手段と、 その比率設定手段によつて設定された補助蒸気
供給比率に基づいて求められた各ボイラ装置の補
助蒸気供給量に対して、当該ボイラ装置の負荷に
応じて補助蒸気供給上限値が設定できる制限値設
定手段とが設けられていることを特徴とするもの
である。
In order to achieve this object, the present invention is provided with an auxiliary steam supply path capable of replenishing steam from another boiler device, wherein there are a plurality of other boiler devices capable of replenishing the steam, and auxiliary steam supply path control. A ratio setting means that can allocate an auxiliary steam supply ratio from each boiler device to the system in consideration of the operating state of each boiler device, etc., and an auxiliary steam supply ratio set by the ratio setting means. A limit value setting means is provided for setting an upper limit value of auxiliary steam supply in accordance with the load of the boiler device, with respect to the auxiliary steam supply amount of each boiler device determined based on the boiler device. be.

〔実施例〕〔Example〕

次に本発明の実施例を図とともに説明する。第
2図はこの実施例に係るボイラ装置の補助蒸気系
統図、第3図はその補助蒸気の供給量制御ブロツ
ク図である。
Next, embodiments of the present invention will be described with reference to the drawings. FIG. 2 is an auxiliary steam system diagram of the boiler apparatus according to this embodiment, and FIG. 3 is a block diagram for controlling the supply amount of the auxiliary steam.

第2図に示すように、本ボイラ装置の補助蒸気
ヘツダ1と1号他缶2との間は第1供給管3で、
補助蒸気ヘツダ1と2号他缶4との間は第2供給
管5でそれぞれ接続されている。
As shown in FIG. 2, a first supply pipe 3 is connected between the auxiliary steam header 1 and the No. 1 other can 2 of this boiler device.
Auxiliary steam header 1 and No. 2 other cans 4 are connected by second supply pipes 5, respectively.

第1供給管3の補助蒸気流の上流側から下流側
にかけて、すなわち1号他缶2から補助蒸気ヘツ
ダ1にかけて第1流量計10、上流側第1減圧弁
6a、第1圧力調節計7、下流側第1減圧弁6b
が順次付設されている。一方、第2供給管5の補
助蒸気流の上流側から下流側にかけて、すなわち
2号他缶4から補助蒸気ヘツダ1にかけて第2流
量計11、上流側第2減圧弁8a、第2圧力調節
計9、下流側第2減圧弁8bが順次付設されてい
る。
From the upstream side to the downstream side of the auxiliary steam flow of the first supply pipe 3, that is, from the No. 1 other can 2 to the auxiliary steam header 1, a first flow meter 10, a first upstream pressure reducing valve 6a, a first pressure regulator 7, Downstream first pressure reducing valve 6b
are being added sequentially. On the other hand, from the upstream side to the downstream side of the auxiliary steam flow of the second supply pipe 5, that is, from the No. 2 canister 4 to the auxiliary steam header 1, there is a second flow meter 11, a second upstream pressure reducing valve 8a, and a second pressure regulator. 9. Second downstream pressure reducing valves 8b are sequentially provided.

従つて、第1供給管3を流通する補助蒸気流
は、上流側第1減圧弁6aと下流側第1減圧弁6
bとによつて2段に減圧され、一方、第2供給管
5を流通する補助蒸気流は、上流側第2減圧弁8
aと下流側第2減圧弁8bとによつて2段に減圧
される。
Therefore, the auxiliary steam flow flowing through the first supply pipe 3 flows through the first pressure reducing valve 6a on the upstream side and the first pressure reducing valve 6 on the downstream side.
On the other hand, the auxiliary steam flow flowing through the second supply pipe 5 is depressurized in two stages by the upstream second pressure reducing valve 8.
The pressure is reduced in two stages by a and the downstream second pressure reducing valve 8b.

第1供給管3と第2供給管5との接合点から補
助蒸気ヘツダ1にかけて配管された合流管12に
は、補助蒸気ヘツダ1に供給される全補助蒸気流
の圧力を検出する圧力計13が付設されている。
A pressure gauge 13 is installed in the confluence pipe 12 that runs from the junction of the first supply pipe 3 and the second supply pipe 5 to the auxiliary steam header 1 to detect the pressure of the entire auxiliary steam flow supplied to the auxiliary steam header 1. is attached.

第1圧力調節計7は上流側第1減圧弁6aの出
口側に、第2圧力調節計9は上流側第2減圧弁8
aの出口側にそれぞれ配置され、第1圧力調節計
7および第2圧力調節弁9の検出信号に基づい
て、上流側第1減圧弁6aおよび上流側第2減圧
弁8aの出口側圧力が一定になるように制御され
る。
The first pressure regulator 7 is located at the outlet side of the upstream first pressure reducing valve 6a, and the second pressure regulator 9 is located at the upstream second pressure reducing valve 8.
Based on the detection signals of the first pressure regulator 7 and the second pressure regulating valve 9, the outlet side pressure of the upstream first pressure reducing valve 6a and the upstream second pressure reducing valve 8a is constant. controlled so that

また、第1流量計10ならびに圧力計13の検
出信号に基づく制御信号は下流側第1減圧弁6b
に、第2流量計11ならびに圧力計13の検出信
号に基づく制御信号は下流側第2減圧弁8bにそ
れぞれ入力されて開度制御がなされる。
Further, a control signal based on the detection signals of the first flow meter 10 and the pressure gauge 13 is transmitted to the downstream first pressure reducing valve 6b.
Control signals based on the detection signals of the second flow meter 11 and the pressure gauge 13 are respectively input to the downstream second pressure reducing valve 8b to control the opening.

この下流側第1減圧弁6bならびに下流側第2
減圧弁8bの開度制御について、第3図を用いて
説明する。
This first downstream pressure reducing valve 6b and the second downstream pressure reducing valve 6b
The opening degree control of the pressure reducing valve 8b will be explained using FIG. 3.

第1流量計10によつて第1供給管3の補助蒸
気流量が、第2流量計11によつて第2供給管5
の補助蒸気流量がそれぞれ検出され、それらの検
出値は加算器14で加算されて合計補助蒸気流量
が演算される。
The auxiliary steam flow rate of the first supply pipe 3 is determined by the first flow meter 10, and the auxiliary steam flow rate of the second supply pipe 3 is determined by the second flow meter 11.
auxiliary steam flow rates are detected, and the detected values are added by an adder 14 to calculate a total auxiliary steam flow rate.

比率設定器15により1号他缶2ならびに2号
他缶4の運転状態などを考慮して、下流側第1減
圧弁6bと下流側第2減圧弁8bの操作量の比率
設定、すなわち補助蒸気供給比率の設定がなされ
る。そして配分器16を介して比較器17と比較
器18にそれぞれ設定基準値として入力される。
これで前記補助蒸気供給比率が、それぞれ比較器
17と比較器18に割り当てられたことになる。
The ratio setting device 15 sets the ratio of the operation amount of the first downstream pressure reducing valve 6b and the second downstream pressure reducing valve 8b, taking into consideration the operating conditions of the No. 1 other can 2 and the No. 2 other can 4, that is, the auxiliary steam. The supply ratio is set. Then, it is inputted to the comparators 17 and 18 via the distributor 16 as set reference values, respectively.
The auxiliary steam supply ratios are now assigned to the comparators 17 and 18, respectively.

比較器17には第1流量計10の実測値が入力
された配分設定された基準値と比較されて、その
偏差量が加算器19に入力される。また、比較器
18には第2流量計11の実測値が入力され配分設
定された基準値と比較されて、その偏差量が加算
器20に入力される。
The comparator 17 compares the actual measured value of the first flow meter 10 with the input distributed reference value, and the deviation amount is input to the adder 19. Further, the actual measured value of the second flowmeter 11 is inputted to the comparator 18 and compared with the reference value for which distribution has been set, and the deviation amount is inputted to the adder 20.

一方、圧力設定器21によつて設定された目標
圧力値(必要補助蒸気流量)が基準値として比較
器22に入力されており、圧力計13によつて検
出された実際の圧力が比較器22において前記目
標圧力値と比較演算される。そしてその偏差量が
それぞれ加算器19,20に入力されて、前記比
較器17,18から出力された偏差量と加算され
ることにより、1号他缶2ならびに2号他缶4か
ら補助すべき蒸気流量が演算され、その結果がそ
れぞれ上限制限器23,24に入力される。この
上限制限器23,24には1号他缶2、2号他缶
4の負荷に応じて補助蒸気供給量の上限値がそれ
ぞれ設定されており、上限制限器23,24を通
ることにより、供給可能補助蒸気量(上限値)を
越えないように制限が加えられる。
On the other hand, the target pressure value (necessary auxiliary steam flow rate) set by the pressure setting device 21 is input to the comparator 22 as a reference value, and the actual pressure detected by the pressure gauge 13 is input to the comparator 22. A comparison calculation is made with the target pressure value. Then, the deviation amounts are inputted to adders 19 and 20, respectively, and added to the deviation amounts output from the comparators 17 and 18, so that the amount of deviation that should be assisted from the No. 1 other can 2 and the No. 2 other can 4 is The steam flow rate is calculated and the results are input to upper limit limiters 23 and 24, respectively. Upper limit values for the amount of auxiliary steam supplied are set in the upper limit limiters 23 and 24 according to the loads of the No. 1 and other cans 2 and the No. 2 and other cans 4, respectively, and by passing through the upper limit limiters 23 and 24, A restriction is placed so that the amount of auxiliary steam that can be supplied does not exceed the amount (upper limit).

上限制限器23,24から出力された信号は開
度調整器25,26にそれぞれ入力されて、各操
作量に見合つた開度調整がPI制御で行われる。
The signals output from the upper limit limiters 23 and 24 are input to the opening degree regulators 25 and 26, respectively, and the opening degree is adjusted according to each operation amount by PI control.

なお、27,28は信号設定器、29,30は
比較器であり、詳細な動作説明は省略する。
Note that 27 and 28 are signal setters, and 29 and 30 are comparators, and a detailed explanation of their operation will be omitted.

前述の比例設定器15は、1号他缶2および2
号他缶4の負荷をそれぞれ検出して、負荷に対応
した比率を自動的に設定できるようにしてもよ
く、また手動で比率が設定できるようにしても構
わない。
The above-mentioned proportional setting device 15 is used for the No. 1 and other cans 2 and 2.
The load of each can 4 may be detected and a ratio corresponding to the load may be automatically set, or the ratio may be set manually.

前記実施例では2段減圧の場合について説明し
たが、1段減圧方式を採用する場合には上流側第
1減圧弁6a、第1圧力調節計7、上流側第2減
圧弁8a、第2圧力調節計9は不要である。
In the above embodiment, the case of two-stage pressure reduction was explained, but when adopting the one-stage pressure reduction method, the upstream first pressure reducing valve 6a, the first pressure regulator 7, the upstream second pressure reducing valve 8a, the second pressure The controller 9 is not required.

〔発明の効果〕〔Effect of the invention〕

本発明は前述のような構成になつており、他の
ボイラ装置への悪影響をおよぼすことなく、適正
な補助蒸気の供給ができる。
The present invention has the above-described configuration, and can appropriately supply auxiliary steam without adversely affecting other boiler devices.

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

第1図は従来のボイラ装置の補助蒸気系統図、
第2図は本発明の実施例に係るボイラ装置の補助
蒸気系統図、第3図はその補助蒸気の供給量制御
ブロツク図である。 1……補助蒸気ヘツダ、2……1号他缶、3…
…第1供給管、4……2号他缶、5……第2供給
管、6b……下流側第1減圧弁、8b……下流側
第2減圧弁、10……第1流量計、11……第2
流量計、15……比率設定器、23,24……上
限制限器、25,26……開度調節器。
Figure 1 is an auxiliary steam system diagram of a conventional boiler equipment.
FIG. 2 is an auxiliary steam system diagram of a boiler apparatus according to an embodiment of the present invention, and FIG. 3 is a block diagram for controlling the supply amount of auxiliary steam. 1...Auxiliary steam header, 2...No. 1 and other cans, 3...
...First supply pipe, 4...Other No. 2 cans, 5...Second supply pipe, 6b...First pressure reducing valve on the downstream side, 8b...Second pressure reducing valve on the downstream side, 10...First flow meter, 11...Second
Flow meter, 15... Ratio setter, 23, 24... Upper limit limiter, 25, 26... Opening adjuster.

Claims (1)

【特許請求の範囲】 1 他のボイラ装置から水蒸気の補給ができる補
助蒸気供給経路を備えたものにおいて、 前記水蒸気の補給ができる他のボイラ装置が複
数あり、 補助蒸気供給経路制御系に、前記各ボイラ装置
の運転状態などを考慮して各ボイラ装置からの補
助蒸気供給比率をそれぞれ割り当てることのでき
る比率設定手段と、 その比率設定手段によつて設定された補助蒸気
供給比率に基づいて求められた各ボイラ装置の補
助蒸気供給量に対して、当該ボイラ装置の負荷に
応じて補助蒸気供給上限値が設定できる制限値設
定手段とが設けられていることを特徴とするボイ
ラ装置。
[Scope of Claims] 1. In a device equipped with an auxiliary steam supply path capable of replenishing steam from another boiler device, there are a plurality of other boiler devices capable of replenishing the steam, and the auxiliary steam supply path control system includes the A ratio setting means that can allocate the auxiliary steam supply ratio from each boiler equipment in consideration of the operating status of each boiler equipment, and the auxiliary steam supply ratio set by the ratio setting means. 1. A boiler device comprising: limit value setting means for setting an auxiliary steam supply upper limit value for the auxiliary steam supply amount of each boiler device according to the load of the boiler device.
JP12003081A 1981-08-01 1981-08-01 Boiler device Granted JPS5822805A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12003081A JPS5822805A (en) 1981-08-01 1981-08-01 Boiler device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12003081A JPS5822805A (en) 1981-08-01 1981-08-01 Boiler device

Publications (2)

Publication Number Publication Date
JPS5822805A JPS5822805A (en) 1983-02-10
JPH0561521B2 true JPH0561521B2 (en) 1993-09-06

Family

ID=14776163

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12003081A Granted JPS5822805A (en) 1981-08-01 1981-08-01 Boiler device

Country Status (1)

Country Link
JP (1) JPS5822805A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0641804B2 (en) * 1984-02-24 1994-06-01 バブコツク日立株式会社 Auxiliary steam pressure controller
JPH0616242Y2 (en) * 1985-02-25 1994-04-27 バブコツク日立株式会社 Boiler load distribution control device
JP4652473B1 (en) * 2010-02-08 2011-03-16 東京電力株式会社 Steam supply control device

Also Published As

Publication number Publication date
JPS5822805A (en) 1983-02-10

Similar Documents

Publication Publication Date Title
US4798531A (en) Process and apparatus for the control of the air and fuel supply to a plurality of burners
WO2009084422A1 (en) Flow rate ratio controlling apparatus
JP3865813B2 (en) Fluid mixing device
JPH0561521B2 (en)
JPH04313107A (en) Mass flow controller
JPH02180667A (en) Coating material circulating apparatus
JPH02149369A (en) Coating circulating apparatus
JPS589920B2 (en) Temperature equilibrium control method for multiple heat exchangers
US4271673A (en) Steam turbine plant
JPS59212606A (en) Controller for temperature of steam
JPH0454489B2 (en)
JP2787369B2 (en) Automatic pressure control valve
JPH0314010A (en) Mass flow controller
JPH0616242Y2 (en) Boiler load distribution control device
JPS6384751A (en) Method for detecting clogging of spray nozzle for continuous casting
JPH02176909A (en) Control method for flow rate control valve and irrigation water use liquid manure mixing device
JPS6235605B2 (en)
JPS6129468Y2 (en)
JP2703050B2 (en) Water wall temperature controller
JPS6132403Y2 (en)
JP3768292B2 (en) Oxygen gas supply pressure control method, oxygen gas supply pressure control device, oxygen gas introduction control method, and oxygen gas introduction control device
JPS6091419A (en) Flow rate control method
JPS59213434A (en) Controlling method of fixed quantity feed of powder and particulate body
JPH1163481A (en) Method and apparatus for controlling pressure of fuel gas in gas fired boiler
JPH0339201B2 (en)