JPH11304101A - Waste heat recovery boiler and operating method thereof - Google Patents
Waste heat recovery boiler and operating method thereofInfo
- Publication number
- JPH11304101A JPH11304101A JP10943598A JP10943598A JPH11304101A JP H11304101 A JPH11304101 A JP H11304101A JP 10943598 A JP10943598 A JP 10943598A JP 10943598 A JP10943598 A JP 10943598A JP H11304101 A JPH11304101 A JP H11304101A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- superheater
- pipe
- superheater outlet
- drum
- 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.)
- Granted
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 43
- 239000002918 waste heat Substances 0.000 title claims abstract description 12
- 238000011017 operating method Methods 0.000 title claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000007789 gas Substances 0.000 claims description 38
- 239000012530 fluid Substances 0.000 claims description 12
- 238000011144 upstream manufacturing Methods 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims description 2
- 238000001514 detection method Methods 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 12
- 238000000034 method Methods 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
Landscapes
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は排熱回収ボイラの保
護方法に関わり、特に、蒸気ドラムで発生した蒸気を主
蒸気管を経て蒸気タービンに供給する排熱回収ボイラに
おいて発生するウオーターハンマーを防止するのに最適
なドレンの排出に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for protecting an exhaust heat recovery boiler, and more particularly, to preventing a water hammer generated in an exhaust heat recovery boiler supplying steam generated in a steam drum to a steam turbine through a main steam pipe. It is related to the optimal drain discharge to perform.
【0002】[0002]
【従来の技術】図8に従来技術における排熱回収ボイラ
の系統図を示す。まず、給水ポンプ1により供給された
給水は節炭器2を通り、蒸気ドラム3へと供給される。
蒸気ドラム3の水は降水管4と蒸発器5を通り、蒸気ド
ラム3へと戻る。蒸気ドラム3より発生した蒸気は、蒸
気ドラム出口連絡管6、過熱器入口寄せ7、過熱器8、
過熱器出口寄せ9、過熱器出口蒸気管10及び過熱器出
口止弁11を通り、図示していない蒸気タービンへ供給
される。2. Description of the Related Art FIG. 8 shows a system diagram of an exhaust heat recovery boiler according to the prior art. First, water supplied by the water supply pump 1 passes through the economizer 2 and is supplied to the steam drum 3.
The water of the steam drum 3 passes through the downcomer 4 and the evaporator 5 and returns to the steam drum 3. The steam generated from the steam drum 3 is connected to a steam drum outlet connecting pipe 6, a superheater inlet port 7, a superheater 8,
The steam is supplied to a steam turbine (not shown) through a superheater outlet shifter 9, a superheater outlet steam pipe 10, and a superheater outlet stop valve 11.
【0003】一方、図示していないガスタービンからの
高温排ガスは煙道13の中に設置された過熱器8、蒸発
器5及び節炭器2でそれぞれ熱交換し、蒸気を発生させ
る。On the other hand, high-temperature exhaust gas from a gas turbine (not shown) exchanges heat with a superheater 8, an evaporator 5 and a economizer 2 installed in a flue 13 to generate steam.
【0004】ところで、バンキング中にはタービン側が
停止しており、過熱器出口蒸気管10にはドレンが凝縮
する。このドレンを排出する目的でドレン弁12が設置
されている。By the way, during banking, the turbine side is stopped, and drain condenses in the superheater outlet steam pipe 10. A drain valve 12 is provided for discharging the drain.
【0005】ドレン排出は従来はタービン起動時にドレ
ン弁12を開くことにより行われていたが、ボイラ起動
時、特に長い停止時間の後に行うコールドスタート時に
はドレンが多量に溜まっており、またドラム圧が小さく
なることから十分にドレン排出ができなかった。そのた
め、特開平6−101802号公報や特開平6−249
402号公報記載のように、ホットバンキング中に残圧
が高いうちに一定時間ドレン弁を全開してドレンを抜い
ていた。しかし、バンキング効果を高めるため、過熱器
8の出口蒸気管10に過熱器出口止弁11を設置する場
合が近年多くなり、しかも過熱器出口止弁11の補修を
考えて比較的高所にある歩道等に止弁11を設置するた
め過熱器8の出口蒸気管10はU字管構成となる場合が
ある。Conventionally, drainage is performed by opening the drain valve 12 when the turbine is started up. However, when the boiler is started up, especially when cold start is performed after a long stoppage, a large amount of drainage is accumulated and the drum pressure is increased. Drainage could not be sufficiently discharged because of the small size. For this reason, Japanese Patent Application Laid-Open Nos. 6-101802 and 6-249
As described in Japanese Patent Publication No. 402, while the residual pressure is high during hot banking, the drain valve is fully opened for a certain period of time to drain the drain. However, in order to enhance the banking effect, the superheater outlet stop valve 11 is often installed in the outlet steam pipe 10 of the superheater 8 in recent years. In order to install the stop valve 11 on the sidewalk or the like, the outlet steam pipe 10 of the superheater 8 may have a U-shaped pipe configuration.
【0006】[0006]
【発明が解決しようとする課題】この場合、図9に示す
ように、過熱器出口蒸気管10の第1垂直部10a、第
1水平部10b及び第2垂直部10cの内部と第2水平
部10dに設けられた過熱器出口止弁11の前までの第
2水平部10d内にドレンが溜まっている場合、第2水
平部10dに設けられる過熱器出口止弁11は閉じられ
ているため、第1水平部10bに接続した配管に設けら
れたドレン弁12を開いても、図10(a)に示すよう
にU字管構成となっている過熱器出口蒸気管10内に滞
留している過熱器8側のドレンが先に抜け、過熱器8側
と過熱器止弁11側にヘッド差Hが生じる。In this case, as shown in FIG. 9, the interior of the first vertical portion 10a, the first horizontal portion 10b and the second vertical portion 10c of the superheater outlet steam pipe 10 and the second horizontal portion are provided. When the drain is accumulated in the second horizontal portion 10d before the superheater outlet stop valve 11 provided in 10d, the superheater outlet stop valve 11 provided in the second horizontal portion 10d is closed, Even if the drain valve 12 provided in the pipe connected to the first horizontal portion 10b is opened, the drain valve 12 stays in the superheater outlet steam pipe 10 having a U-shaped pipe configuration as shown in FIG. The drain on the superheater 8 side comes off first, and a head difference H is generated between the superheater 8 side and the superheater stop valve 11 side.
【0007】過熱器8側のドレンが第1水平部10bに
達すると、上記ヘッド差Hがあるため、止弁11側のド
レンが、急激に過熱器8側に流れ、第1水平部10b内
に過熱器8側の蒸気を巻き込むことになり、巻き込まれ
た蒸気がドレンにより冷却され、急激にドレン化する。
このとき、図10(b)に示すように、蒸気が急激にド
レン化してできた空間をドレン水が埋めようとしてドレ
ン水が衝突し、激しい衝撃(ウオーターハンマーと称す
ることとする。)が生じる。When the drain on the side of the superheater 8 reaches the first horizontal portion 10b, the drain on the side of the stop valve 11 suddenly flows to the side of the superheater 8 due to the above-mentioned head difference H. The steam on the side of the superheater 8 is entrained in the air, and the entrained steam is cooled by the drain and rapidly drained.
At this time, as shown in FIG. 10B, the drain water collides with the drain water in an attempt to fill the space formed by the rapid drainage of steam, and a strong impact (referred to as a water hammer) occurs. .
【0008】U字管水平部10bにおいてウオーターハ
ンマーが発生した場合、振動や衝撃により過熱器出口蒸
気管10が破損するという問題があった。If a water hammer occurs in the U-tube horizontal section 10b, there is a problem that the steam pipe 10 at the outlet of the superheater is damaged by vibration or impact.
【0009】本発明の課題は上記課題を解決するため
に、排熱回収ボイラのバンキング中および再起動時など
のドレン排出時にウオーターハンマーが起こらないよう
に、ドレンを抜く制御、及び配管系統構成を提供するこ
とである。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, it is an object of the present invention to control draining and to configure a piping system so that a water hammer does not occur during draining of a waste heat recovery boiler during banking and restarting. To provide.
【0010】[0010]
【課題を解決するための手段】上記本発明の課題は次の
各構成により解決される。 (1)排ガス流路内に配置された蒸発器と、該蒸発器で
加熱された水と蒸気からなる流体から蒸気を分離する蒸
気ドラムと、該蒸気ドラムからの蒸気を過熱するための
排ガス流路内に配置された過熱器と、該過熱器からの蒸
気を排ガス流路外部に導く過熱器出口蒸気管とを備えた
排熱回収ボイラにおいて、過熱器出口蒸気管には、該蒸
気管内の蒸気の流通を止める止弁と、該止弁より前流側
に過熱器出口蒸気圧力を計測する過熱器出口圧力計を設
け、また、過熱器出口蒸気管にはドレン弁を接続し、さ
らに、蒸気ドラムには、該ドラム内の蒸気圧力を計測す
るドラム圧力計を設け、過熱器出口蒸気管のドレン排出
時における過熱器出口圧力計とドラム圧力計の計測値か
ら、過熱器出口蒸気圧力と蒸気ドラム圧力との差圧を演
算し、該演算して得られた差圧が設定値に達すると過熱
器出口蒸気管のドレン弁を開く制御装置を設けた排熱回
収ボイラ。The object of the present invention is solved by the following constitutions. (1) An evaporator disposed in an exhaust gas channel, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and an exhaust gas flow for superheating the steam from the steam drum In a waste heat recovery boiler provided with a superheater disposed in a passage and a superheater outlet steam pipe for guiding steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe includes A stop valve for stopping the flow of steam, and a superheater outlet pressure gauge for measuring the superheater outlet steam pressure upstream of the stop valve are provided, and a drain valve is connected to the superheater outlet steam pipe. The steam drum is provided with a drum pressure gauge for measuring the steam pressure in the drum.From the measured values of the superheater outlet pressure gauge and the drum pressure gauge at the time of drain discharge of the superheater outlet steam pipe, the superheater outlet steam pressure and Calculate the pressure difference from the steam drum pressure, Heat recovery boiler provided with a control device which is differential pressure opens the drain valve of the superheater outlet steam pipe reaches the set value.
【0011】(2)排ガス流路内に配置された蒸発器
と、該蒸発器で加熱された水と蒸気からなる流体から蒸
気を分離する蒸気ドラムと、該蒸気ドラムからの蒸気を
過熱するための排ガス流路内に配置された過熱器と、該
過熱器からの蒸気を排ガス流路外部に導く過熱器出口蒸
気管とを備えた排熱回収ボイラにおいて、過熱器出口蒸
気管は過熱器出口の第1垂直部と該第1垂直部に続く第
1水平部と該第1水平部に続く第2垂直部と該第2垂直
部に続く第2水平部とからなる略U字状管からなり、過
熱器出口蒸気管内の蒸気の流通を止める止弁を過熱器出
口蒸気管の第2水平部又は第2垂直部に設置し、ドレン
弁を第1水平部の下部に接続し、第1水平部と止弁前流
側の第2水平部又は第2垂直部との蒸気圧の差圧を計測
する差圧計を設け、過熱器出口蒸気管内のドレン排出時
において、前記差圧計の検出値が設定差圧に達するとド
レン弁を開く制御装置を設けた排熱回収ボイラ。(2) An evaporator disposed in the exhaust gas channel, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a device for superheating the steam from the steam drum In a waste heat recovery boiler provided with a superheater disposed in the exhaust gas flow path of the above and a superheater outlet steam pipe for guiding steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe is connected to the superheater outlet. From a substantially U-shaped tube comprising a first vertical portion, a first horizontal portion following the first vertical portion, a second vertical portion following the first horizontal portion, and a second horizontal portion following the second vertical portion. A stop valve for stopping the flow of steam in the superheater outlet steam pipe is installed at the second horizontal portion or the second vertical portion of the superheater outlet steam pipe, and a drain valve is connected to a lower portion of the first horizontal portion; A differential pressure gauge for measuring a differential pressure of the vapor pressure between the horizontal portion and the second horizontal portion or the second vertical portion on the upstream side of the stop valve is provided, During draining of the heat outlet steam pipe, when the detected value of the differential pressure gauge reaches the target pressure difference heat recovery steam control device provided for opening the drain valve.
【0012】(3)排ガス流路内に配置された蒸発器
と、該蒸発器で加熱された水と蒸気からなる流体から蒸
気を分離する蒸気ドラムと、該蒸気ドラムからの蒸気を
過熱するための排ガス流路内に配置された過熱器と、蒸
気ドラムと過熱器との間に設けられる蒸気流路となる蒸
気ドラム出口連絡管と、過熱器からの蒸気を排ガス流路
外部に導く過熱器出口蒸気管とを備えた排熱回収ボイラ
において、過熱器出口蒸気管は過熱器出口の第1垂直部
と該第1垂直部に続く第1水平部と該第1水平部に続く
第2垂直部と該第2垂直部に続く第2水平部とからなる
略U字状管からなり、過熱器出口蒸気管内の蒸気の流通
を止める止弁を過熱器出口蒸気管の第2水平部に設置
し、ドレン弁を第1水平部の下部に接続し、蒸気ドラム
又は蒸気ドラム出口連絡管あるいは過熱器出口蒸気管の
いずれかと止弁の前流側の第2水平部を連絡するバラン
ス配管を設置し排熱回収ボイラ。(3) An evaporator disposed in the exhaust gas channel, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a device for heating the steam from the steam drum A superheater disposed in the exhaust gas flow path of the steam drum, a steam drum outlet connecting pipe serving as a vapor flow path provided between the steam drum and the superheater, and a superheater for guiding the steam from the superheater to the outside of the exhaust gas flow path In an exhaust heat recovery boiler provided with an outlet steam pipe, the superheater outlet steam pipe has a first vertical portion of the superheater outlet, a first horizontal portion following the first vertical portion, and a second vertical portion following the first horizontal portion. And a second horizontal portion following the second vertical portion, a substantially U-shaped tube, and a stop valve for stopping the flow of steam in the superheater outlet steam pipe is installed at the second horizontal portion of the superheater outlet steam pipe. And a drain valve connected to the lower portion of the first horizontal portion, and connected to a steam drum or a steam drum outlet. Tube or superheater installed heat recovery steam balance pipe to contact the second horizontal portion of the upstream side of any and check valve of the outlet steam pipe.
【0013】(4)排ガス流路内に配置された蒸発器
と、該蒸発器で加熱された水と蒸気からなる流体から蒸
気を分離する蒸気ドラムと、該蒸気ドラムからの蒸気を
過熱するための排ガス流路内に配置された過熱器と、該
過熱器からの蒸気を排ガス流路外部に導く過熱器出口蒸
気管とを備えた排熱回収ボイラにおいて、過熱器出口蒸
気管は過熱器出口の第1垂直部と該第1垂直部に続く第
1水平部と該第1水平部に続く第2垂直部と該第2垂直
部に続く第2水平部とからなる略U字状管からなり、ま
た、ドレン弁を第1水平部の下部に接続し、過熱器出口
蒸気管内の蒸気の流通を止める止弁をドレン弁の接続位
置より後流側の過熱器出口蒸気管の第2水平部に設置
し、過熱器出口近傍の過熱器蒸気管の第1垂直部と止弁
設置位置より前流側の第2水平部との間に蒸気流路とな
る連絡管を設けた排熱回収ボイラ。(4) An evaporator disposed in the exhaust gas channel, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a device for superheating the steam from the steam drum In a waste heat recovery boiler provided with a superheater disposed in the exhaust gas flow path of the above and a superheater outlet steam pipe for guiding steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe is connected to the superheater outlet. From a substantially U-shaped tube comprising a first vertical portion, a first horizontal portion following the first vertical portion, a second vertical portion following the first horizontal portion, and a second horizontal portion following the second vertical portion. The drain valve is connected to a lower portion of the first horizontal portion, and a stop valve for stopping the flow of steam in the superheater outlet steam pipe is connected to the second horizontal portion of the superheater outlet steam pipe downstream of the connection position of the drain valve. The first vertical section of the superheater steam pipe near the superheater outlet and the upstream side of the stop valve installation position Heat recovery boiler provided with a communication pipe serving as a steam flow path between the two horizontal portions.
【0014】(5)排ガス流路内に配置された蒸発器
と、該蒸発器で加熱された水と蒸気からなる流体から蒸
気を分離する蒸気ドラムと、該蒸気ドラムからの蒸気を
過熱するための排ガス流路内に配置された過熱器と、該
過熱器からの蒸気を排ガス流路外部に導く過熱器出口蒸
気管とを備えた排熱回収ボイラにおいて、過熱器出口蒸
気管は過熱器出口の第1垂直部と該第1垂直部に続く第
1水平部と該第1水平部に続く第2垂直部と該第2垂直
部に続く第2水平部とからなる略U字状管からなり、ド
レン弁を第1水平部の下部に接続し、過熱器出口蒸気管
内の蒸気の流通を止める止弁を過熱器出口蒸気管の第1
水平部のドレン弁接続位置より後流側に設置した排熱回
収ボイラ。(5) An evaporator disposed in the exhaust gas channel, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a device for heating the steam from the steam drum In a waste heat recovery boiler provided with a superheater disposed in the exhaust gas flow path of the above and a superheater outlet steam pipe for guiding steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe is connected to the superheater outlet. From a substantially U-shaped tube comprising a first vertical portion, a first horizontal portion following the first vertical portion, a second vertical portion following the first horizontal portion, and a second horizontal portion following the second vertical portion. The drain valve is connected to the lower part of the first horizontal portion, and a stop valve for stopping the flow of steam in the superheater outlet steam pipe is connected to the first superheater outlet steam pipe.
Exhaust heat recovery boiler installed downstream from the drain valve connection position in the horizontal section.
【0015】(6)排ガス流路内に配置された蒸発器
と、該蒸発器で加熱された水と蒸気からなる流体から蒸
気を分離する蒸気ドラムと、該蒸気ドラムからの蒸気を
過熱するための排ガス流路内に配置された過熱器と、該
過熱器からの蒸気を排ガス流路外部に導く過熱器出口蒸
気管とを備えた排熱回収ボイラにおいて、過熱器出口蒸
気管内のドレン排出時に、過熱器出口蒸気管内の蒸気の
流通を止めた状態で、過熱器出口蒸気管内の蒸気圧と蒸
気ドラム圧力の差圧が設定値に達すると過熱器出口蒸気
管からドレンを排出する排熱回収ボイラの運転方法。(6) An evaporator disposed in the exhaust gas channel, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a device for superheating the steam from the steam drum In a waste heat recovery boiler provided with a superheater disposed in an exhaust gas flow path of the superheater and a superheater outlet steam pipe for guiding steam from the superheater to the outside of the exhaust gas flow path, when drain in the superheater outlet steam pipe is discharged. When the pressure difference between the steam pressure in the superheater outlet steam pipe and the steam drum pressure reaches a set value while the flow of steam in the superheater outlet steam pipe is stopped, the exhaust heat recovery drains the drain from the superheater outlet steam pipe. How to operate the boiler.
【0016】以上の各解決手段により、バンキング中又
はボイラ再起動時のドレン排出時に水平配管内への蒸気
の巻き込みが発生せず、ウオーターハンマーを防止でき
る。[0016] According to the above-mentioned respective solutions, steam is not entrained in the horizontal pipe during draining during banking or when the boiler is restarted, so that a water hammer can be prevented.
【0017】[0017]
【発明の実施の形態】本発明の実施の形態について説明
する。図1に、圧力計の差圧からドレン弁を制御し、ウ
オーターハンマーの生じない制御装置を設置した排熱回
収ボイラの例について示す。図1に示す排熱回収ボイラ
において、図8で説明したボイラと同一機能を奏する構
成部分については同一番号を付して、その説明は省略す
る。Embodiments of the present invention will be described. FIG. 1 shows an example of an exhaust heat recovery boiler provided with a control device that controls a drain valve based on a differential pressure of a pressure gauge and does not generate a water hammer. In the exhaust heat recovery boiler shown in FIG. 1, components having the same functions as those of the boiler described in FIG. 8 are denoted by the same reference numerals, and description thereof will be omitted.
【0018】ドラム3内の圧力を計測するドラム圧力計
14と過熱器出口蒸気管10内の圧力を計測する過熱器
出口圧力計15を設け、前記2つの圧力計14、15で
得られた圧力値は制御装置19内にそれぞれ設けられた
圧力発信器16で電気信号に変換され、この電気信号に
基づき圧力計14、15の圧力差が圧力比較装置17で
比較される。前記圧力差に基づく信号は制御装置19の
出力としてドレン弁12の開閉制御に用いられる。例え
ば、圧力計14、15の圧力差が約1.5mH2Oとな
ったときにドレン弁12を10〜20%開度とし、ドレ
ンを排出する。A drum pressure gauge 14 for measuring the pressure in the drum 3 and a superheater outlet pressure gauge 15 for measuring the pressure in the superheater outlet steam pipe 10 are provided, and the pressure obtained by the two pressure gauges 14 and 15 is provided. The values are converted into electric signals by pressure transmitters 16 provided in the control device 19, and the pressure difference between the pressure gauges 14 and 15 is compared by the pressure comparator 17 based on the electric signals. The signal based on the pressure difference is used as an output of the control device 19 to control the opening and closing of the drain valve 12. For example, the drain valve 12 and 10-20% opening when the pressure difference between the pressure gauge 14 and 15 were approximately 1.5mH 2 O, to discharge the drain.
【0019】図4にドレン弁12を開くタイミングにつ
いて示す。ドラム圧力計14により測定されるドラム3
の圧力と過熱器出口圧力計15により測定される過熱器
8の出口圧力は、バンキング中にドレンが溜まることか
ら、両者の圧力には時間経過と共にドレンがU字状の過
熱器出口蒸発管10の垂直部10cに達し、水頭に相当
する圧力差を生じる。前記圧力差が設定した圧力になる
と圧力比較装置17から、ドレン弁12を10〜20%
開放する電気信号が伝わり、ドレン弁12をゆっくり開
放する。ドレンが抜けるに従って、水頭より生じた圧力
差が緩和され、ドラム3の圧力と過熱器8の出口圧力の
圧力差が小さくなり、ドレンがすべて、過熱器出口蒸気
管10から抜け出ると圧力差はほとんど0となる。この
時ドレン弁12を全閉する制御信号が与えられ、ドレン
弁12が閉まる。さらに、時間経過と共にドレンが溜ま
るため、圧力差が生じてくるが、上記のような制御装置
19を組み込むことにより、ウオーターハンマーを起こ
すことなくドレンの効果的な排出が可能となる。FIG. 4 shows the timing at which the drain valve 12 is opened. Drum 3 measured by drum pressure gauge 14
And the outlet pressure of the superheater 8 measured by the superheater outlet pressure gauge 15, the drain accumulates during the banking. Therefore, the drain pressure of the superheater 8 in the U-shaped superheater outlet evaporating pipe 10 increases with the passage of time. And a pressure difference corresponding to the head is generated. When the pressure difference reaches the set pressure, the drain valve 12 is set to 10-20% from the pressure comparison device 17.
An electric signal to be opened is transmitted, and the drain valve 12 is slowly opened. As the drain comes off, the pressure difference generated from the water head is alleviated, the pressure difference between the pressure of the drum 3 and the outlet pressure of the superheater 8 becomes small, and when all the drain comes out of the superheater outlet steam pipe 10, the pressure difference becomes almost zero. It becomes 0. At this time, a control signal for completely closing the drain valve 12 is given, and the drain valve 12 is closed. Further, since the drain accumulates with the passage of time, a pressure difference is generated. By incorporating the control device 19 as described above, the drain can be effectively discharged without causing a water hammer.
【0020】また、図2に示すように過熱器出口止弁1
1前流側の過熱器出口蒸気管10の第2水平部10d及
び過熱器出口蒸気管10の第1水平部10bの圧力差を
差圧計18により計測し、この差圧値から制御装置19
によりドレン量を推定し、上記した図4に示す制御手順
と同様な方法によりドレン弁12の開度を制御すること
によっても同様にウオーターハンマーを防止することが
できる。Also, as shown in FIG.
The pressure difference between the second horizontal portion 10d of the superheater outlet steam pipe 10 and the first horizontal portion 10b of the superheater outlet steam pipe 10 on the upstream side is measured by a differential pressure gauge 18, and the control device 19 is determined from the differential pressure value.
The water hammer can be similarly prevented by estimating the drain amount by controlling the opening degree of the drain valve 12 by a method similar to the control procedure shown in FIG. 4 described above.
【0021】また、図3に示すように、過熱器出口止弁
11が第1水平部10bの後流側の垂直部10cに設置
してある場合にも、その前流側の垂直部10cに差圧計
18を設置し、第1水平部10bと垂直部10cとの圧
力差を差圧計18で計測し、この差圧値からドレン量を
推定し、上記した図4に示す制御手順と同様な方法によ
りドレン弁12の開度を制御することによっても同様に
ウオーターハンマーを防止することができる。As shown in FIG. 3, even when the superheater outlet stop valve 11 is installed in the vertical portion 10c on the downstream side of the first horizontal portion 10b, the vertical stop portion 10c on the upstream side is also provided. A differential pressure gauge 18 is installed, a pressure difference between the first horizontal portion 10b and the vertical portion 10c is measured by the differential pressure gauge 18, a drain amount is estimated from the differential pressure value, and the same as the control procedure shown in FIG. 4 described above. The water hammer can be similarly prevented by controlling the opening of the drain valve 12 by a method.
【0022】このような制御システムを設置することに
より、バンキング中の過熱器出口蒸気管10内でのウオ
ーターハンマーを防止できる。By installing such a control system, it is possible to prevent water hammer in the superheater outlet steam pipe 10 during banking.
【0023】図5に示す本発明の実施の形態は、バラン
ス配管20を蒸気ドラム出口連絡管6と過熱器出口止弁
11前流側の間に設置した場合の配管系統を有する排熱
回収ボイラの例について示す。図5に示す排熱回収ボイ
ラにおいて、図8で説明したボイラと同一機能を奏する
構成部分については同一番号を付して、その説明は省略
する。The embodiment of the present invention shown in FIG. 5 has an exhaust heat recovery boiler having a piping system when the balance pipe 20 is installed between the steam drum outlet connection pipe 6 and the superheater outlet stop valve 11 upstream side. An example will be described. In the heat recovery steam generator shown in FIG. 5, components having the same functions as those of the boiler described with reference to FIG. 8 are denoted by the same reference numerals, and description thereof will be omitted.
【0024】バランス配管20を蒸気ドラム出口連絡管
6と過熱器出口止弁11前流側にある過熱器出口蒸気配
管10との間に設置した場合、通常運転中に蒸気が過熱
器8をバイパスするため、そのバイパス蒸気の流量を調
節するか又は流さないようにする事が必要である。その
目的で、バランス配管20にはオリフィス22あるいは
弁(図示せず)を設置することもある。バンキング中に
ドレンを抜く場合、垂直部10a、10cのドレンはほ
ぼ同時に低下するため、U字管水平部10b、10dに
おいてバランス配管20を設置していない場合のように
蒸気の巻き込みが生じないため、ウオーターハンマーは
起こらない。なお、バランス配管20の取り出し位置を
蒸気ドラム出口連絡管6でなく、蒸気ドラム3とするこ
ともできる。When the balance pipe 20 is installed between the steam drum outlet connection pipe 6 and the superheater outlet steam pipe 10 on the upstream side of the superheater outlet stop valve 11, the steam bypasses the superheater 8 during normal operation. Therefore, it is necessary to adjust the flow rate of the bypass steam or not to flow the bypass steam. For this purpose, the balance pipe 20 may be provided with an orifice 22 or a valve (not shown). When draining is performed during banking, since the drains of the vertical portions 10a and 10c decrease almost at the same time, steam is not involved in the U-tube horizontal portions 10b and 10d unlike the case where the balance pipe 20 is not installed. , No water hammer. Note that the take-out position of the balance pipe 20 may be the steam drum 3 instead of the steam drum outlet connection pipe 6.
【0025】図5に示した配管系統と同様に図6に示す
構成からなる配管系統でも、上記と同様な作用が得られ
るためウオーターハンマーを生じない。この場合は過熱
器出口管寄せ9近傍付近の過熱器出口蒸気配管10の第
1垂直管10aと第2水平管10dを接続するバイパス
管23を設けると、バンキング中にドレンを抜く場合、
垂直部10a、10cのドレンはほぼ同時に低下するた
め、U字管水平部10b、10dにおいてバイパス配管
23を設置していない場合のように蒸気の巻き込みが生
じないため、ウオーターハンマーは起こらない。Similar to the piping system shown in FIG. 5, a piping system having the configuration shown in FIG. 6 does not generate a water hammer because the same operation as described above is obtained. In this case, if a bypass pipe 23 connecting the first vertical pipe 10a and the second horizontal pipe 10d of the superheater outlet steam pipe 10 near the superheater outlet header 9 is provided, when draining is performed during banking,
Since the drains of the vertical portions 10a and 10c decrease almost at the same time, steam is not involved in the U-tube horizontal portions 10b and 10d unlike the case where the bypass pipe 23 is not installed, so that no water hammer occurs.
【0026】図7に示す実施の形態は過熱器出口蒸気配
管10の水平部10bにドレン弁12を設け、ドレン弁
12の後流側の水平部10bに過熱器出口弁11を設置
した場合の配管系統図を示す。この場合、図10(a)
及び図10(b)で説明したような蒸気巻き込みを起こ
すことのない配管系統であるため、ウオーターハンマー
を起こすことなくドレンの排出が可能である。さらに、
上記各図に示した構成を併用することにより、ウオータ
ーハンマーを未然に防止できる。In the embodiment shown in FIG. 7, a drain valve 12 is provided in a horizontal portion 10b of a superheater outlet steam pipe 10, and a superheater outlet valve 11 is provided in a horizontal portion 10b downstream of the drain valve 12. The piping system diagram is shown. In this case, FIG.
And since it is a piping system which does not cause steam entrainment as described in FIG. 10 (b), drain can be discharged without causing a water hammer. further,
The water hammer can be prevented beforehand by using the configurations shown in the above drawings together.
【0027】[0027]
【発明の効果】本発明によれば、蒸気巻き込みを起こす
ことのない配管系統であるため、バンキング時などにウ
オーターハンマーを起こすことなく、蒸気配管からドレ
ンの排出が可能である。According to the present invention, since the piping system does not cause entrainment of steam, the drain can be discharged from the steam piping without causing a water hammer at the time of banking or the like.
【図1】 本発明の実施の形態の圧力計の差圧からドレ
ン弁の開度を制御する排熱回収ボイラの概略図である。FIG. 1 is a schematic diagram of an exhaust heat recovery boiler that controls an opening of a drain valve from a differential pressure of a pressure gauge according to an embodiment of the present invention.
【図2】 本発明の実施の形態の過熱器出口蒸気管の差
圧計の差圧値からドレン弁の開度を制御する排熱回収ボ
イラの概略図である。FIG. 2 is a schematic diagram of an exhaust heat recovery boiler that controls an opening degree of a drain valve based on a differential pressure value of a differential pressure gauge of a superheater outlet steam pipe according to an embodiment of the present invention.
【図3】 本発明の実施の形態の過熱器出口蒸気管の差
圧計の差圧値からドレン弁の開度を制御する排熱回収ボ
イラの概略図である。FIG. 3 is a schematic diagram of an exhaust heat recovery boiler that controls an opening degree of a drain valve based on a differential pressure value of a differential pressure gauge of a superheater outlet steam pipe according to an embodiment of the present invention.
【図4】 本発明の実施の形態のドレン弁を開けるタイ
ミングについて示す図である。FIG. 4 is a diagram illustrating a timing of opening a drain valve according to the embodiment of the present invention.
【図5】 本発明の実施の形態のバランス配管を設置し
た場合の配管系統を示す排熱回収ボイラの概略図であ
る。FIG. 5 is a schematic diagram of an exhaust heat recovery boiler showing a piping system when the balance piping according to the embodiment of the present invention is installed.
【図6】 本発明の実施の形態のバイパス配管を設置し
た場合の配管系統を示す排熱回収ボイラの概略図であ
る。FIG. 6 is a schematic diagram of an exhaust heat recovery boiler showing a piping system when a bypass pipe according to an embodiment of the present invention is installed.
【図7】 本発明の実施の形態の配管系統を示す排熱回
収ボイラの概略図である。FIG. 7 is a schematic diagram of an exhaust heat recovery boiler showing a piping system according to an embodiment of the present invention.
【図8】 従来技術における排熱回収ボイラの系統を示
す図である。FIG. 8 is a diagram showing a system of an exhaust heat recovery boiler according to a conventional technique.
【図9】 従来技術における排熱回収ボイラのバンキン
グ時のドレン滞留状態を示す図である。FIG. 9 is a diagram showing a drain retention state during banking of an exhaust heat recovery boiler according to a conventional technique.
【図10】 従来技術における排熱回収ボイラのドレン
弁開によりドレン排出状況およびハンマー発生時の状態
を示す図である。FIG. 10 is a diagram showing a drain discharge state and a state when a hammer occurs due to opening of a drain valve of a waste heat recovery boiler according to a conventional technique.
1 給水ポンプ 2 節炭器 3 蒸気ドラム 4 降水管 5 蒸発器 6 蒸気ドラム
出口連絡管 7 過熱器入口寄せ 8 過熱器 9 過熱器出口管寄せ 10 過熱器出
口蒸気管 10a 第1垂直管 10b 第1水
平部 10c 第2垂直管 10d 第2水
平部 11 過熱器出口止弁 12 ドレン弁 13 煙道 14 ドラム圧
力計 15 過熱器出口圧力計 16 圧力発信
器 17 圧力比較装置 18 差圧計 19 制御装置 20 バランス
配管 22 オリフィス 23 バイパス
配管REFERENCE SIGNS LIST 1 feedwater pump 2 economizer 3 steam drum 4 downcomer 5 evaporator 6 steam drum outlet connecting pipe 7 superheater inlet 8 superheater 9 superheater outlet header 10 superheater outlet steam pipe 10 a first vertical pipe 10 b first Horizontal part 10c Second vertical pipe 10d Second horizontal part 11 Superheater outlet stop valve 12 Drain valve 13 Flue 14 Drum pressure gauge 15 Superheater outlet pressure gauge 16 Pressure transmitter 17 Pressure comparison device 18 Differential pressure gauge 19 Control device 20 Balance Piping 22 Orifice 23 Bypass piping
フロントページの続き (72)発明者 下野 展雄 広島県呉市宝町6番9号 バブコック日立 株式会社呉工場内 (72)発明者 重中 利則 広島県呉市宝町6番9号 バブコック日立 株式会社呉工場内Continued on the front page (72) Inventor Norio Shimono 6-9 Takara-cho, Kure City, Hiroshima Prefecture Inside Babcock Hitachi Kure Factory (72) Inventor Toshinori Shigenaka 6-9 Takara-cho Kure City, Hiroshima Prefecture Babcock Hitachi Kure Factory Inside
Claims (6)
蒸発器で加熱された水と蒸気からなる流体から蒸気を分
離する蒸気ドラムと、該蒸気ドラムからの蒸気を過熱す
るための排ガス流路内に配置された過熱器と、該過熱器
からの蒸気を排ガス流路外部に導く過熱器出口蒸気管と
を備えた排熱回収ボイラにおいて、 過熱器出口蒸気管には、該蒸気管内の蒸気の流通を止め
る止弁と、該止弁より前流側に過熱器出口蒸気圧力を計
測する過熱器出口圧力計を設け、また、過熱器出口蒸気
管にはドレン弁を接続し、さらに、蒸気ドラムには該ド
ラム内の蒸気圧力を計測するドラム圧力計を設け、過熱
器出口蒸気管のドレン排出時における過熱器出口圧力計
とドラム圧力計の計測値から、過熱器出口蒸気圧力と蒸
気ドラム圧力との差圧を演算し、該演算して得られた差
圧が設定値に達すると過熱器出口蒸気管のドレン弁を開
く制御装置を設けたことを特徴とする排熱回収ボイラ。1. An evaporator disposed in an exhaust gas passage, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a steam drum for superheating steam from the steam drum. In an exhaust heat recovery boiler provided with a superheater arranged in an exhaust gas flow path and a superheater outlet steam pipe for guiding steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe includes the steam A stop valve for stopping the flow of steam in the pipe, and a superheater outlet pressure gauge for measuring the superheater outlet steam pressure on the upstream side of the stop valve, and a drain valve connected to the superheater outlet steam pipe, Further, the steam drum is provided with a drum pressure gauge for measuring the steam pressure in the drum, and the superheater outlet steam pressure is measured based on the measured values of the superheater outlet pressure gauge and the drum pressure gauge when the drain of the superheater outlet steam pipe is discharged. Calculate the differential pressure between the Heat recovery steam differential pressure obtained by, characterized in that the control device is provided to open the drain valve of the superheater outlet steam pipe reaches the set value.
蒸発器で加熱された水と蒸気からなる流体から蒸気を分
離する蒸気ドラムと、該蒸気ドラムからの蒸気を過熱す
るための排ガス流路内に配置された過熱器と、該過熱器
からの蒸気を排ガス流路外部に導く過熱器出口蒸気管と
を備えた排熱回収ボイラにおいて、 過熱器出口蒸気管は過熱器出口の第1垂直部と該第1垂
直部に続く第1水平部と該第1水平部に続く第2垂直部
と該第2垂直部に続く第2水平部とからなる略U字状管
からなり、過熱器出口蒸気管内の蒸気の流通を止める止
弁を過熱器出口蒸気管の第2水平部又は第2垂直部に設
置し、ドレン弁を第1水平部の下部に接続し、第1水平
部と止弁前流側の第2水平部又は第2垂直部との蒸気圧
の差圧を計測する差圧計を設け、過熱器出口蒸気管内の
ドレン排出時において、前記差圧計の検出値が設定差圧
に達するとドレン弁を開く制御装置を設けたことを特徴
とする排熱回収ボイラ。2. An evaporator disposed in an exhaust gas passage, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a steam drum for heating the steam from the steam drum. In an exhaust heat recovery boiler provided with a superheater disposed in an exhaust gas flow path and a superheater outlet steam pipe that guides steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe is connected to the superheater outlet. The U-shaped tube comprises a first vertical portion, a first horizontal portion following the first vertical portion, a second vertical portion following the first horizontal portion, and a second horizontal portion following the second vertical portion. Installing a stop valve for stopping the flow of steam in the superheater outlet steam pipe at the second horizontal portion or the second vertical portion of the superheater outlet steam pipe, connecting the drain valve to a lower portion of the first horizontal portion, Pressure gauge to measure the differential pressure of the vapor pressure between the second part and the second vertical part or the second vertical part upstream of the stop valve, During draining of the outlet steam pipe, the exhaust heat recovery boiler, characterized in that the detection value of the differential pressure gauge is provided with a control device to open the drain valve reaches the set pressure differential.
蒸発器で加熱された水と蒸気からなる流体から蒸気を分
離する蒸気ドラムと、該蒸気ドラムからの蒸気を過熱す
るための排ガス流路内に配置された過熱器と、蒸気ドラ
ムと過熱器との間に設けられる蒸気流路となる蒸気ドラ
ム出口連絡管と、過熱器からの蒸気を排ガス流路外部に
導く過熱器出口蒸気管とを備えた排熱回収ボイラにおい
て、 過熱器出口蒸気管は過熱器出口の第1垂直部と該第1垂
直部に続く第1水平部と該第1水平部に続く第2垂直部
と該第2垂直部に続く第2水平部とからなる略U字状管
からなり、過熱器出口蒸気管内の蒸気の流通を止める止
弁を過熱器出口蒸気管の第2水平部に設置し、ドレン弁
を第1水平部の下部に接続し、蒸気ドラム又は蒸気ドラ
ム出口連絡管あるいは過熱器出口蒸気管のいずれかと止
弁の前流側の第2水平部を接続するバランス配管を設置
したことを特徴とする排熱回収ボイラ。3. An evaporator disposed in an exhaust gas passage, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a steam drum for heating the steam from the steam drum. A superheater arranged in the exhaust gas passage, a steam drum outlet connecting pipe serving as a steam passage provided between the steam drum and the superheater, and a superheater outlet for guiding steam from the superheater to the outside of the exhaust gas passage In a waste heat recovery boiler provided with a steam pipe, a superheater outlet steam pipe has a first vertical portion at a superheater outlet, a first horizontal portion following the first vertical portion, and a second vertical portion following the first horizontal portion. And a second horizontal portion following the second vertical portion, and a stop valve for stopping the flow of steam in the superheater outlet steam pipe is provided at the second horizontal portion of the superheater outlet steam pipe. , A drain valve connected to the lower part of the first horizontal portion, and a steam drum or a steam drum outlet connecting pipe Heat recovery steam Rui, characterized in that it has established a balance pipe connecting the second horizontal portion of the upstream side of any and stop valve of superheater outlet steam pipe.
蒸発器で加熱された水と蒸気からなる流体から蒸気を分
離する蒸気ドラムと、該蒸気ドラムからの蒸気を過熱す
るための排ガス流路内に配置された過熱器と、該過熱器
からの蒸気を排ガス流路外部に導く過熱器出口蒸気管と
を備えた排熱回収ボイラにおいて、 過熱器出口蒸気管は過熱器出口の第1垂直部と該第1垂
直部に続く第1水平部と該第1水平部に続く第2垂直部
と該第2垂直部に続く第2水平部とからなる略U字状管
からなり、また、ドレン弁を第1水平部の下部に接続
し、過熱器出口蒸気管内の蒸気の流通を止める止弁をド
レン弁の接続位置より後流側の過熱器出口蒸気管の第2
水平部に設置し、過熱器出口近傍の過熱器蒸気管の第1
垂直部と止弁設置位置より前流側の第2水平部との間に
蒸気流路となる連絡管を設けたことを特徴とする排熱回
収ボイラ。4. An evaporator disposed in an exhaust gas passage, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a steam drum for superheating steam from the steam drum. In an exhaust heat recovery boiler provided with a superheater disposed in an exhaust gas flow path and a superheater outlet steam pipe that guides steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe is connected to the superheater outlet. The U-shaped tube comprises a first vertical portion, a first horizontal portion following the first vertical portion, a second vertical portion following the first horizontal portion, and a second horizontal portion following the second vertical portion. Also, a drain valve is connected to a lower portion of the first horizontal portion, and a stop valve for stopping the flow of steam in the superheater outlet steam pipe is connected to a second end of the superheater outlet steam pipe downstream of the connection position of the drain valve.
Installed in a horizontal section, the first of the superheater steam pipe near the superheater outlet
An exhaust heat recovery boiler, wherein a communication pipe serving as a steam flow path is provided between a vertical portion and a second horizontal portion upstream of the stop valve installation position.
蒸発器で加熱された水と蒸気からなる流体から蒸気を分
離する蒸気ドラムと、該蒸気ドラムからの蒸気を過熱す
るための排ガス流路内に配置された過熱器と、該過熱器
からの蒸気を排ガス流路外部に導く過熱器出口蒸気管と
を備えた排熱回収ボイラにおいて、 過熱器出口蒸気管は過熱器出口の第1垂直部と該第1垂
直部に続く第1水平部と該第1水平部に続く第2垂直部
と該第2垂直部に続く第2水平部とからなる略U字状管
からなり、ドレン弁を第1水平部の下部に接続し、過熱
器出口蒸気管内の蒸気の流通を止める止弁を過熱器出口
蒸気管の第1水平部のドレン弁接続位置より後流側に設
置したことを特徴とする排熱回収ボイラ。5. An evaporator disposed in an exhaust gas passage, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a steam drum for superheating steam from the steam drum. In an exhaust heat recovery boiler provided with a superheater disposed in an exhaust gas flow path and a superheater outlet steam pipe that guides steam from the superheater to the outside of the exhaust gas flow path, the superheater outlet steam pipe is connected to the superheater outlet. The U-shaped tube comprises a first vertical portion, a first horizontal portion following the first vertical portion, a second vertical portion following the first horizontal portion, and a second horizontal portion following the second vertical portion. The drain valve was connected to the lower portion of the first horizontal portion, and a stop valve for stopping the flow of steam in the superheater outlet steam pipe was installed on the downstream side of the drain valve connection position of the first horizontal portion of the superheater outlet steam pipe. An exhaust heat recovery boiler characterized in that:
蒸発器で加熱された水と蒸気からなる流体から蒸気を分
離する蒸気ドラムと、該蒸気ドラムからの蒸気を過熱す
るための排ガス流路内に配置された過熱器と、該過熱器
からの蒸気を排ガス流路外部に導く過熱器出口蒸気管と
を備えた排熱回収ボイラにおいて、 過熱器出口蒸気管内のドレン排出時に、過熱器出口蒸気
管内の蒸気の流通を止めた状態で、過熱器出口蒸気管内
の蒸気圧と蒸気ドラム圧力の差圧が設定値に達すると過
熱器出口蒸気管からドレンを排出することを特徴とする
排熱回収ボイラの運転方法。6. An evaporator disposed in an exhaust gas passage, a steam drum for separating steam from a fluid consisting of water and steam heated by the evaporator, and a steam drum for superheating steam from the steam drum. In a waste heat recovery boiler provided with a superheater arranged in an exhaust gas flow path and a superheater outlet steam pipe for guiding steam from the superheater to the outside of the exhaust gas flow path, at the time of drain discharge in the superheater outlet steam pipe, With the flow of steam in the superheater outlet steam pipe stopped, when the pressure difference between the steam pressure in the superheater outlet steam pipe and the steam drum pressure reaches a set value, drain is discharged from the superheater outlet steam pipe. Operating method of waste heat recovery boiler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10943598A JP4072837B2 (en) | 1998-04-20 | 1998-04-20 | Waste heat recovery boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10943598A JP4072837B2 (en) | 1998-04-20 | 1998-04-20 | Waste heat recovery boiler |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH11304101A true JPH11304101A (en) | 1999-11-05 |
| JP4072837B2 JP4072837B2 (en) | 2008-04-09 |
Family
ID=14510183
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10943598A Expired - Lifetime JP4072837B2 (en) | 1998-04-20 | 1998-04-20 | Waste heat recovery boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4072837B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6237542B1 (en) * | 1999-01-29 | 2001-05-29 | Kabushiki Kaisha Toshiba | Heat recovery boiler and hot banking releasing method thereof |
-
1998
- 1998-04-20 JP JP10943598A patent/JP4072837B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6237542B1 (en) * | 1999-01-29 | 2001-05-29 | Kabushiki Kaisha Toshiba | Heat recovery boiler and hot banking releasing method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4072837B2 (en) | 2008-04-09 |
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