JPH0117041B2 - - Google Patents

Info

Publication number
JPH0117041B2
JPH0117041B2 JP54135297A JP13529779A JPH0117041B2 JP H0117041 B2 JPH0117041 B2 JP H0117041B2 JP 54135297 A JP54135297 A JP 54135297A JP 13529779 A JP13529779 A JP 13529779A JP H0117041 B2 JPH0117041 B2 JP H0117041B2
Authority
JP
Japan
Prior art keywords
steam
fluidized bed
heat transfer
tube
cooling water
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
JP54135297A
Other languages
Japanese (ja)
Other versions
JPS5661501A (en
Inventor
Kimya Sakamoto
Hiroyuki Kako
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 JP13529779A priority Critical patent/JPS5661501A/en
Publication of JPS5661501A publication Critical patent/JPS5661501A/en
Publication of JPH0117041B2 publication Critical patent/JPH0117041B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 この発明は流動層ボイラの層内伝熱管の温度制
御に関し、詳しくは流動層ボイラの緊急停止の際
伝熱管の焼損を防止する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to temperature control of interbed heat exchanger tubes in a fluidized bed boiler, and more particularly to a method for preventing burnout of heat exchanger tubes during emergency shutdown of a fluidized bed boiler.

流動層の熱を利用して蒸気を発生させ、この蒸
気を蒸気タービン等の蒸気を使用する機器に対し
て供給する流動層ボイラは、層内の熱を有効に利
用するため、蒸発管、過熱器管等の伝熱管を流動
層内に配置している。この流動層ボイラにおい
て、蒸気を使用する機器、例えば前記蒸気タービ
ントリツプの場合、タービンに対する蒸気の供給
をただちに主蒸気弁閉とし停止すると共に、流動
層に対する燃料の供給も停止して不要の蒸気の発
生を少なくする必要がある。この場合、流動層内
は運転中約850℃の高温となつており、かつ流動
媒体の保有熱量が大であるため炉の運転停止後相
当の時間高温を保つことになる。このため、蒸発
管に対する給水の供給量を運転中のままにしてお
くと、層内の余熱により大量の蒸気が発生し、こ
の蒸気を蒸気溜または系外に排出する必要が生ず
る。また反対に蒸発管に対する給水の供給を停止
すると管内の残溜給水は蒸発し管内の給水が比熱
の低い蒸気となり流れもほとんどなくなり管壁が
過度に昇温して管を焼損する虞れがある。以上の
問題点は層内過熱器管についても同様である。こ
れらの問題点は層内伝熱管の構成材料をステンレ
ス系の金属とすることにより一応の解決を見るこ
とができるが、材料費が非常に高価となるという
問題がある。
A fluidized bed boiler uses the heat of the fluidized bed to generate steam and supplies this steam to equipment that uses steam such as a steam turbine. Heat transfer tubes such as vessels are placed in the fluidized bed. In this fluidized bed boiler, in the case of equipment that uses steam, such as the above-mentioned steam turbine trip, the supply of steam to the turbine is immediately stopped by closing the main steam valve, and the supply of fuel to the fluidized bed is also stopped to remove unnecessary steam. It is necessary to reduce the occurrence of In this case, the inside of the fluidized bed is at a high temperature of about 850° C. during operation, and the fluidized medium has a large amount of heat, so the high temperature is maintained for a considerable time after the furnace is stopped. For this reason, if the amount of water supplied to the evaporator tube remains unchanged during operation, a large amount of steam will be generated due to residual heat within the layer, and this steam will need to be discharged to the steam reservoir or outside the system. On the other hand, if the supply of water to the evaporator pipe is stopped, the residual water in the pipe will evaporate, and the water in the pipe will turn into steam with a low specific heat, resulting in almost no flow, and there is a risk that the pipe wall will become excessively heated, causing the pipe to burn out. . The above problems also apply to the intralayer superheater tube. These problems can be solved to some extent by using a stainless steel metal as the constituent material of the interlayer heat exchanger tube, but there is a problem in that the material cost is extremely high.

この発明の目的は上述の従来技術の欠点をなく
し、流動層ボイラの緊急停止時に系外に排出する
蒸気の量が少なく、かつ通常の鋼管で層内伝熱管
を構成しても焼損の虞れがない方法を提供するこ
とにある。
The purpose of this invention is to eliminate the above-mentioned drawbacks of the prior art, to reduce the amount of steam discharged outside the system during emergency shutdown of a fluidized bed boiler, and to eliminate the risk of burnout even if the intrabed heat exchanger tubes are constructed of ordinary steel pipes. There is no way to provide that.

要するにこの発明は、流動層ボイラの緊急停止
時に層内伝熱管に対する給水もしくは蒸気の供給
を停止し、気胴とは別系統の冷却水系から前記層
内伝熱管に対し伝熱管の焼損を防止し得る量の冷
却水を供給し、層内の余熱により発生した蒸気は
管内の圧力を検知しながら徐々に系外に排出する
ようにしたものである。
In short, this invention stops the supply of water or steam to the intrabed heat exchanger tubes during an emergency stop of a fluidized bed boiler, and prevents the heat exchanger tubes from burning out from a cooling water system that is separate from the gas cylinder. The amount of cooling water to be obtained is supplied, and the steam generated by residual heat in the layer is gradually discharged to the outside of the system while the pressure inside the pipes is detected.

なおこの発明の出願日と同日に、伝熱管の焼損
防止をボイラの気胴内のボイラ水を伝熱管の冷却
媒体として使用しかつボイラ水を過熱器にも送る
方法を提案している。(特願昭54−135299号)そ
のボイラ水の供給量は過熱器管の管壁温度を検知
し、その検知した温度信号を制御箱に送り、制御
箱の指令により供給するボイラ水の量を制御して
いる、蒸発管については運転中と変りなく気胴か
ら供給され蒸発管が流動媒体から受ける熱量に応
じ蒸気となり気胴に送られ、格別の制御はされて
いない。
On the same day as the filing date of this invention, a method was proposed to prevent burnout of heat transfer tubes by using boiler water in the gas cylinder of the boiler as a cooling medium for the heat transfer tubes and also sending the boiler water to the superheater. (Patent Application No. 54-135299) The amount of boiler water supplied is determined by detecting the temperature of the tube wall of the superheater tube, sending the detected temperature signal to the control box, and controlling the amount of boiler water supplied according to the command from the control box. The evaporator tube, which is being controlled, is supplied from the gas cylinder as during operation, and is converted into steam and sent to the gas cylinder according to the amount of heat that the evaporator tube receives from the fluidized medium, and is not particularly controlled.

従つて緊急停止時に過剰な蒸気を生ずるおそれ
があり、その際は安全弁又は他の逃がし手段で放
出する。
Therefore, in the event of an emergency shutdown, there is a risk of excessive steam being generated, which should be vented via a safety valve or other relief means.

これに対し本願発明では、飽和蒸気圧力(即ち
飽和蒸気温度)伝熱管の管壁温度と対応すること
に着目し蒸気放出管路の圧出検知器を利用し、か
つヘツドタンクを別に設け温度の低いかつ潜熱の
利用できる冷却水をこのヘツドタンクより伝熱管
に供給量を制御して供給する。冷却水はボイラ水
より温度低くかつ潜熱を利用できるので冷却効果
が大きいこと、既に加熱されたボイラ水を無駄に
消費し放出し熱エネルギーを損失しないようにす
るものである。
On the other hand, the present invention focuses on the fact that the saturated steam pressure (that is, the saturated steam temperature) corresponds to the tube wall temperature of the heat transfer tube, and utilizes a pressure detector in the steam discharge pipeline, and also provides a separate head tank to maintain low temperature. Cooling water, in which latent heat can be utilized, is supplied from this head tank to the heat exchanger tubes by controlling the supply amount. Cooling water has a lower temperature than boiler water and can utilize latent heat, so it has a large cooling effect, and it prevents already heated boiler water from being wasted and released, thereby preventing loss of thermal energy.

先ずこの発明に係る方法を実施するための流動
層ボイラについて説明する。
First, a fluidized bed boiler for carrying out the method according to the present invention will be explained.

第1図において、1は流動層ボイラ本体、2は
気胴である。給水は給水ポンプ3によりエコノマ
イザ4を経由して気胴2に供給される。本体1の
下部には空気室5が形成され多孔板6を通して流
動層8に対して空気が供給される。流動層8には
層内伝熱管として蒸発管9および過熱器管10が
配置してある。過熱器管10内の蒸気は蒸気配管
30を経由して蒸気タービン31に送られる。こ
の流動層に対しては、石炭があらかじめ分級され
て供給され、粗粒炭ホツパ20、スクリユーフイ
ーダ24を経て流動層に供給され、一方微粉炭は
微粉炭供給管21a,21bを経て空気Aにより
気流輸送されバーナ22a,22bに至り層内で
燃焼する。なお符号23a,23bは燃焼ガスと
熱交換を行なう蒸発管群である。
In FIG. 1, 1 is the main body of the fluidized bed boiler, and 2 is the gas cylinder. Water is supplied to the gas cylinder 2 by a water pump 3 via an economizer 4. An air chamber 5 is formed in the lower part of the main body 1, and air is supplied to the fluidized bed 8 through a perforated plate 6. An evaporator tube 9 and a superheater tube 10 are arranged in the fluidized bed 8 as intrabed heat transfer tubes. Steam in the superheater tube 10 is sent to a steam turbine 31 via a steam pipe 30. Coal is classified in advance and supplied to this fluidized bed, and is supplied to the fluidized bed via a coarse coal hopper 20 and a screw feeder 24, while pulverized coal is passed through pulverized coal supply pipes 21a and 21b to air. The air is transported by A and reaches the burners 22a and 22b, where it is burned within the layer. Note that reference numerals 23a and 23b represent a group of evaporator tubes that exchange heat with the combustion gas.

以上の流動層ボイラ1においてタービン31に
故障が生じた場合、タービントリツプの信号が制
御箱32に送られる。制御箱32はこの信号に基
づいて蒸気配管30に設けた主蒸気弁33を全閉
としてタービン31に対する蒸気の供給をただち
に停止すると共に蒸気管34に設けた弁35を全
閉として気胴2からの蒸気も停止する。これと同
時に蒸発管9と気胴2を接続する蒸気管36aお
よび36bに設けた弁37a,37bも全閉とし
て蒸発管9と気胴2の間の蒸気の循環流動も停止
する。この操作に続いてヘツドタンク40と過熱
器管10および蒸発管9を接続する冷却水管41
の弁42を微開として冷却水をこれら層内伝熱管
に徐々に流入させ、層内の余熱と熱交換させて伝
熱管の焼損を防止する。蒸発管9内の蒸気は蒸気
排出管43に設けた弁44を微開することにより
徐々に蒸気を蒸気排出管45に流入させる。一方
過熱器管10内の蒸気は蒸気供給管30から蒸気
排出管45に流入する。これにより蒸気排出管4
5に設けた圧力検知器46により管内圧力を検知
しつつ弁47を操作し、前記流動層の余熱により
生じた蒸気を系外に排出する。管内圧力がほぼ0
になつたら弁47を全開にして配管内の蒸気を完
全に放出し作業を完了する。
If a failure occurs in the turbine 31 in the fluidized bed boiler 1 described above, a turbine trip signal is sent to the control box 32. Based on this signal, the control box 32 completely closes the main steam valve 33 provided in the steam pipe 30 to immediately stop the supply of steam to the turbine 31, and also fully closes the valve 35 provided in the steam pipe 34 to completely close the main steam valve 33 provided in the steam pipe 30 to completely close the steam supply from the gas cylinder 2. steam also stops. At the same time, the valves 37a and 37b provided in the steam pipes 36a and 36b connecting the evaporation pipe 9 and the gas cylinder 2 are also fully closed, and the circulating flow of steam between the evaporation pipe 9 and the gas cylinder 2 is also stopped. Following this operation, the cooling water pipe 41 connecting the head tank 40, the superheater pipe 10, and the evaporator pipe 9
The valve 42 is slightly opened to allow cooling water to gradually flow into these intralayer heat transfer tubes, thereby exchanging heat with residual heat in the layer to prevent burnout of the heat transfer tubes. The steam in the evaporation pipe 9 is gradually made to flow into the steam exhaust pipe 45 by slightly opening the valve 44 provided in the steam exhaust pipe 43. On the other hand, the steam in the superheater tube 10 flows from the steam supply tube 30 into the steam exhaust tube 45. As a result, the steam exhaust pipe 4
The valve 47 is operated while detecting the pressure inside the pipe by the pressure sensor 46 provided at 5, and the steam generated by the residual heat of the fluidized bed is discharged to the outside of the system. The pressure inside the pipe is almost 0
When the temperature is reached, the valve 47 is fully opened to completely release the steam in the pipe and the work is completed.

この発明によれば流動層ボイラ停止後、層内伝
熱管に対して冷却水を通過させることにより伝熱
管構材料を安価な鋼管で形成しても焼損が生ぜず
しかも系外に排出する蒸気の量も減少させ、冷却
効率の良いものにすることができる。なお放出蒸
気圧力の信号に代り、伝熱管に管壁用温度計測器
を取り付けその温度信号により制御することもで
きる。
According to this invention, after the fluidized bed boiler is stopped, cooling water is passed through the heat exchanger tubes in the bed, so that even if the heat exchanger tube structure is made of inexpensive steel pipes, no burnout occurs, and moreover, no steam is discharged outside the system. It is also possible to reduce the amount of heat and improve cooling efficiency. Note that instead of the signal of the released steam pressure, a tube wall temperature measuring device may be attached to the heat transfer tube and the temperature signal may be used for control.

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

第1図はこの発明に係る方法を実施するための
流動層ボイラの系統図である。 1……流動層ボイラ本体、2……気胴、9……
蒸発管、10……過熱器管、31……蒸気タービ
ン、32……制御箱、33……主蒸気弁、35,
37a,37b,42,44,47……弁、40
……ヘツドタンク、41……冷却水管、43……
蒸気排出管、45……蒸気排出管、46……圧力
検知器。
FIG. 1 is a system diagram of a fluidized bed boiler for carrying out the method according to the invention. 1... Fluidized bed boiler body, 2... Gas cylinder, 9...
Evaporation pipe, 10...Superheater tube, 31...Steam turbine, 32...Control box, 33...Main steam valve, 35,
37a, 37b, 42, 44, 47... valve, 40
...Head tank, 41...Cooling water pipe, 43...
Steam exhaust pipe, 45... Steam exhaust pipe, 46... Pressure detector.

Claims (1)

【特許請求の範囲】[Claims] 1 流動層内に伝熱管を配置して各種機器に蒸気
を供給するものにおいて、主蒸気弁の緊急遮断を
する場合、層内の伝熱管に対する気胴からの給水
を停止し、冷却水を保有するヘツドタンクから前
記伝熱管に冷却水を導入し、流動層の余熱により
発生した蒸気を、管壁温度に対応する管内飽和蒸
気圧力を検知し、その圧力信号を受ける制御箱の
指令により、冷却水量の制御と発生した蒸気を系
外に排出する管路に設けた圧力制御弁を制御する
ことを特徴とするヘツドタンク使用の層内伝熱管
焼損防止方法。
1. When heat transfer tubes are arranged in a fluidized bed to supply steam to various equipment, when the main steam valve is shut off in an emergency, the water supply from the gas cylinder to the heat transfer tubes in the bed is stopped and cooling water is stored. Cooling water is introduced from the head tank into the heat transfer tube, and the steam generated by the residual heat of the fluidized bed is controlled by the control box, which detects the saturated steam pressure inside the tube corresponding to the tube wall temperature and receives the pressure signal, to control the amount of cooling water. A method for preventing burnout of in-layer heat transfer tubes using a head tank, characterized by controlling a pressure control valve provided in a pipe line for discharging generated steam to the outside of the system.
JP13529779A 1979-10-22 1979-10-22 Method of preventing burning loss of interrlayer heat exchanger tube with heat tank Granted JPS5661501A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13529779A JPS5661501A (en) 1979-10-22 1979-10-22 Method of preventing burning loss of interrlayer heat exchanger tube with heat tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13529779A JPS5661501A (en) 1979-10-22 1979-10-22 Method of preventing burning loss of interrlayer heat exchanger tube with heat tank

Publications (2)

Publication Number Publication Date
JPS5661501A JPS5661501A (en) 1981-05-27
JPH0117041B2 true JPH0117041B2 (en) 1989-03-28

Family

ID=15148401

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13529779A Granted JPS5661501A (en) 1979-10-22 1979-10-22 Method of preventing burning loss of interrlayer heat exchanger tube with heat tank

Country Status (1)

Country Link
JP (1) JPS5661501A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57136004A (en) * 1981-02-18 1982-08-21 Babcock Hitachi Kk Fluidized bed boiler capable of preventing burning of heat exchanger tube in layer

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54135299A (en) * 1978-04-12 1979-10-20 Ajinomoto Co Inc Preparation of d-arabinitol

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54135299A (en) * 1978-04-12 1979-10-20 Ajinomoto Co Inc Preparation of d-arabinitol

Also Published As

Publication number Publication date
JPS5661501A (en) 1981-05-27

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