JPH09303710A - Auxiliary steam equipment of natural circulation boiler - Google Patents

Auxiliary steam equipment of natural circulation boiler

Info

Publication number
JPH09303710A
JPH09303710A JP14357596A JP14357596A JPH09303710A JP H09303710 A JPH09303710 A JP H09303710A JP 14357596 A JP14357596 A JP 14357596A JP 14357596 A JP14357596 A JP 14357596A JP H09303710 A JPH09303710 A JP H09303710A
Authority
JP
Japan
Prior art keywords
steam
auxiliary
pipe
natural circulation
auxiliary steam
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP14357596A
Other languages
Japanese (ja)
Inventor
Shigemi Kobayashi
繁美 小林
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP14357596A priority Critical patent/JPH09303710A/en
Publication of JPH09303710A publication Critical patent/JPH09303710A/en
Pending legal-status Critical Current

Links

Landscapes

  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable easy lowering of the temperature of superheater outlet steam by cooling to the demanded upper limit temperature of auxiliary steam by a simple construction. SOLUTION: This equipment is so constructed that superheater outlet steam 17 of a superheater 10 provided in a natural circulation boiler 1 is supplied as auxiliary steam 17a to a preheating device H of the natural circulation boiler 1 through a superheated auxiliary steam pipe 18 equipped with a pressure reducing orifice 19 (or a pressure reducing valve). A saturated steam mixing pipe 35 so designed as to take out saturated steam 3a of a drum 3 of the natural. circulation boiler 1 and to make it join the superheated auxiliary stem pipe 18 is provided and a temperature detector 36 is disposed on the downstream side of the pressure reducing orifice 19 in the superheated auxiliary steam pipe 18. Moreover, a flow control valve 37 provided for the saturated steam mixing pipe 35 regulates the flow rate of the saturated steam 3a on the basis of a detected temperature of the temperature detector 36.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、自然循環形ボイラ
の補助蒸気装置に関するものである。
TECHNICAL FIELD The present invention relates to an auxiliary steam device for a natural circulation boiler.

【0002】[0002]

【従来の技術】図2は、従来の自然循環形ボイラの主要
構成の一例を示すフローチャートであり、図中1は火炉
2とドラム3とからなる自然循環形ボイラであり、該自
然循環形ボイラ1の火炉炉壁には、給水ポンプ4からの
水5が節炭器6を介して供給されており、図示しないバ
ーナによる燃料と空気の燃焼により水5が加熱されてド
ラム3に供給されて蒸気3a(飽和蒸気)が分離される
ようになっている。
2. Description of the Related Art FIG. 2 is a flow chart showing an example of the main configuration of a conventional natural circulation boiler, in which 1 is a natural circulation boiler consisting of a furnace 2 and a drum 3. Water 5 from a water supply pump 4 is supplied to the furnace wall of No. 1 through a economizer 6, and the water 5 is heated by combustion of fuel and air by a burner (not shown) and supplied to the drum 3. The steam 3a (saturated steam) is separated.

【0003】前記ドラム3にて分離された飽和蒸気3a
は、火炉後伝部に備えた横置過熱器7、火炉2内に設け
られる放射形過熱器8、吊下式過熱器9等の過熱器10
により過熱された後、タービン入口弁11を介して高圧
タービン12に供給されて該高圧タービン12を駆動
し、その後タービン出口管13を介して火炉後伝部の横
置再熱器14に導かれて再度過熱された後、中圧或いは
低圧のタービン15に供給されて該タービン15を駆動
するようになっている。
Saturated steam 3a separated by the drum 3
Is a superheater 10 such as a horizontal superheater 7 provided in the post-furnace transmission section, a radial superheater 8 provided in the furnace 2, a suspension type superheater 9, and the like.
After being superheated by the turbine, it is supplied to the high-pressure turbine 12 via the turbine inlet valve 11 to drive the high-pressure turbine 12, and then is guided via the turbine outlet pipe 13 to the horizontal reheater 14 in the post-fired part of the furnace. After being overheated again, it is supplied to the turbine 15 of medium pressure or low pressure to drive the turbine 15.

【0004】前記過熱器10における放射形過熱器8の
出口には、抽気点16から過熱器出口蒸気17の一部を
取り出すようにした過熱補助蒸気管18を接続すると共
に、該過熱補助蒸気管18に減圧オリフィス19(或い
は減圧弁)を設けて例えば196kg/cm2程度の圧
力を有している過熱器出口蒸気17を28kg/cm2
程度の圧力まで減圧し、この減圧した蒸気を補助蒸気1
7aとして空気、水、燃料等の予熱を行う予熱装置Hに
供給するようにしている。
A superheat auxiliary steam pipe 18 for taking out a part of the superheater outlet steam 17 from the extraction point 16 is connected to the outlet of the radial superheater 8 in the superheater 10, and the superheat auxiliary steam pipe is also connected. 18 to a vacuum orifice 19 (or pressure reducing valve) the superheater outlet steam 17 having a provided example 196kg / cm 2 of about pressure of 28 kg / cm 2
Reduce the pressure to a level of about 1 and use this reduced pressure steam as auxiliary steam 1
7a is supplied to a preheating device H for preheating air, water, fuel and the like.

【0005】一方、前記過熱器10からの過熱器出口蒸
気17は例えば420℃程度の高温となっており、更
に、自然循環形ボイラ1の起動時には、自然循環形ボイ
ラ1に供給される燃料と水と空気のバランスが変化する
こと等によって過渡的に過熱器出口蒸気17の温度が変
化し450℃前後の高温になる場合も生じる。
On the other hand, the superheater outlet steam 17 from the superheater 10 has a high temperature of, for example, about 420 ° C. Further, when the natural circulation boiler 1 is started, the fuel supplied to the natural circulation boiler 1 is The temperature of the superheater outlet steam 17 may change transiently due to changes in the balance between water and air, and the temperature may rise to around 450 ° C.

【0006】しかし、前記補助蒸気17aの供給を受け
る予熱装置Hは、その構成材料に基づいた制限によって
補助蒸気17aの温度350℃を要求上限温度としてお
り、このために、前記過熱器出口蒸気17の温度を35
0℃程度以下に下げる必要がある。
However, the preheater H receiving the supply of the auxiliary steam 17a has a temperature of 350 ° C. of the auxiliary steam 17a as the required upper limit temperature due to the restriction based on the constituent material thereof. The temperature of 35
It is necessary to lower the temperature to about 0 ° C or lower.

【0007】このために、従来においては、図2に示す
ように給水ポンプ4出口にスプレー給水管21を分岐し
て設け、該スプレー給水管21の端部を、前記過熱補助
蒸気管18の減圧オリフィス19の下流にスプレー混合
器20を介して接続することにより、前記給水ポンプ4
からの水5の一部を前記過熱器出口蒸気17に混合して
前記過熱器出口蒸気17の温度を低下させることが行わ
れている。
For this reason, conventionally, as shown in FIG. 2, a spray water supply pipe 21 is provided at the outlet of the water supply pump 4 in a branched manner, and the end portion of the spray water supply pipe 21 is decompressed by the superheat auxiliary steam pipe 18. By connecting the downstream side of the orifice 19 through the spray mixer 20, the water supply pump 4
A part of the water 5 is mixed with the superheater outlet steam 17 to lower the temperature of the superheater outlet steam 17.

【0008】しかし、前記給水ポンプ4から供給される
水5の圧力は通常205kg/cm 2と高くなってお
り、この圧力を混合する先の補助蒸気17aの圧力(2
8kg/cm2程度)の圧力に合せて42kg/cm2
度に下げる必要があり、しかも前記過熱器出口蒸気17
の温度を例えば420℃程度から350℃程度まで下げ
るのに必要な水5の量が少ないために、調節計22を備
えた2段式の減圧弁23をスプレー給水管21に設ける
ようにしている。
However, it is supplied from the water supply pump 4.
Water 5 pressure is usually 205kg / cm TwoAnd getting higher
The pressure of the auxiliary steam 17a (2
8kg / cmTwo42kg / cm according to the pressure)TwoAbout
It is necessary to lower the temperature gradually, and the superheater outlet steam 17
Lower the temperature from about 420 ℃ to about 350 ℃
Since the amount of water 5 required for the
The two-stage pressure reducing valve 23 is installed in the spray water supply pipe 21.
Like that.

【0009】また、前記補助蒸気17aの温度を350
℃以下に保持するために、前記過熱補助蒸気管18のス
プレー混合器20の下流に温度検出器24を設置し、更
にスプレー給水管21における減圧弁23の下流に、前
記温度検出器24の検出温度に基づいて水の流量を調節
するようにした流量調節弁25を配置している。
Further, the temperature of the auxiliary steam 17a is set to 350
In order to keep the temperature below ℃, a temperature detector 24 is installed downstream of the spray mixer 20 of the superheat auxiliary steam pipe 18, and further, the temperature detector 24 detects downstream of the pressure reducing valve 23 in the spray water supply pipe 21. A flow rate adjusting valve 25 is arranged to adjust the flow rate of water based on the temperature.

【0010】図中26は、別個に設けられた補助ボイラ
であり、自然循環形ボイラ1の起動時の初期には、過熱
器10からの過熱器出口蒸気17の温度が低いために予
熱装置Hの予熱源に利用することができず、そのために
補助ボイラ26を駆動して該補助ボイラ26からの補助
蒸気17bを前記予熱装置Hに供給して空気、水、燃料
の予熱を行うようにしている。
In the figure, reference numeral 26 is a separately provided auxiliary boiler, and the temperature of the superheater outlet steam 17 from the superheater 10 is low at the initial stage of startup of the natural circulation boiler 1, so that the preheater H is used. Therefore, the auxiliary boiler 26 is driven to supply the auxiliary steam 17b from the auxiliary boiler 26 to the preheating device H to preheat air, water and fuel. There is.

【0011】また、自然循環形ボイラ1が通常運転状態
にはいると、前記高圧タービン12からタービン出口管
13に補助蒸気17aの温度条件に合致した蒸気が吐出
されるようになるので、これを補助蒸気17cとして予
熱装置Hに供給するようにした補助蒸気抽出管27を設
けるようにしている。また、この補助蒸気抽出管27
は、前記予熱装置Hの要求蒸気温度に合致した蒸気が取
り出せる種々の取出位置に接続されている。
Further, when the natural circulation boiler 1 is in a normal operation state, steam which matches the temperature condition of the auxiliary steam 17a comes to be discharged from the high pressure turbine 12 to the turbine outlet pipe 13, An auxiliary steam extraction pipe 27 adapted to be supplied to the preheating device H as the auxiliary steam 17c is provided. In addition, this auxiliary steam extraction pipe 27
Are connected to various take-out positions where the steam that matches the required steam temperature of the preheating device H can be taken out.

【0012】図中28は、自然循環形ボイラ1の新設時
に、ドラム3の飽和蒸気3aを取り出して横置再熱器1
4に送って横置再熱器14の図示しない安全弁のテスト
を行うための再熱器安全弁テスト蒸気管であり、安全弁
のテスト終了後は、遮断弁29を閉じて、フランジ部3
0を切り離すようにしており、従って前記再熱器安全弁
テスト蒸気管28は通常時は使用されないものである。
図中31,32,33は開閉弁、34は排出管を示す。
Reference numeral 28 in the figure indicates that the saturated steam 3a from the drum 3 is taken out and the horizontal reheater 1 is installed when the natural circulation type boiler 1 is newly installed.
4 is a reheater safety valve test steam pipe for sending to 4 to test a safety valve (not shown) of the horizontal reheater 14, and after the safety valve test is completed, the shutoff valve 29 is closed and the flange portion 3
Therefore, the reheater safety valve test steam pipe 28 is not normally used.
In the figure, reference numerals 31, 32 and 33 denote open / close valves, and 34 denotes a discharge pipe.

【0013】上記した従来の自然循環形ボイラ1の起動
時は、給水ポンプ4を作動して節炭器6から火炉2に水
5を供給すると共に、燃料と空気とを図示しないバーナ
で燃焼させる。この時、タービン入口弁11は閉とし、
また開閉弁31,32を閉、開閉弁33を開としてお
く。
When the conventional natural circulation boiler 1 is started, the water supply pump 4 is operated to supply water 5 from the economizer 6 to the furnace 2, and the fuel and air are burned by a burner (not shown). . At this time, the turbine inlet valve 11 is closed,
Further, the open / close valves 31 and 32 are closed and the open / close valve 33 is opened.

【0014】自然循環形ボイラ1の起動初期は、過熱器
出口蒸気17は温度が低く、量も少ないために利用する
ことができず、そのためにタービン入口弁11、開閉弁
32は閉じられて開閉弁33が開けられており、温度が
低い過熱器出口蒸気17は排出管34から排出される。
At the initial stage of starting the natural circulation boiler 1, the superheater outlet steam 17 cannot be used because it has a low temperature and a small amount. Therefore, the turbine inlet valve 11 and the opening / closing valve 32 are closed and opened / closed. The valve 33 is opened, and the superheater outlet steam 17 having a low temperature is discharged from the discharge pipe 34.

【0015】この時、水、空気、燃料の予熱を行って自
然循環形ボイラ1の起動時間(立上げ時間)を短縮する
ために、補助ボイラ26を駆動して、補助ボイラ26か
らの補助蒸気17bを予熱装置Hに供給している。
At this time, in order to preheat water, air, and fuel to shorten the start-up time (start-up time) of the natural circulation boiler 1, the auxiliary boiler 26 is driven and the auxiliary steam from the auxiliary boiler 26 is driven. 17b is supplied to the preheating device H.

【0016】前記ドラム3に導入される蒸気量が増加し
てドラム3内圧力が例えば10kg/cm2程度になり
ドラム3出口の蒸気温度が190℃程度になると、開閉
弁33を閉じると共に開閉弁32を開けて、過熱補助蒸
気管18からの過熱器出口蒸気17を補助蒸気17aと
して予熱装置Hに供給するようにし、同時に補助ボイラ
26からの補助蒸気17bの供給を停止して、補助ボイ
ラ26によるエネルギの消費量を節約する。
When the amount of steam introduced into the drum 3 increases and the internal pressure of the drum 3 reaches, for example, about 10 kg / cm 2 and the steam temperature at the outlet of the drum 3 reaches about 190 ° C., the on-off valve 33 is closed and the on-off valve is closed. 32 is opened so that the superheater outlet steam 17 from the superheat auxiliary steam pipe 18 is supplied to the preheating device H as the auxiliary steam 17a, and at the same time, the supply of the auxiliary steam 17b from the auxiliary boiler 26 is stopped, and the auxiliary boiler 26 Save energy consumption by.

【0017】過熱器出口蒸気17の温度が徐々に上昇し
て350℃を越えるようになると、温度検出器24の検
出温度が要求上限温度の例えば350℃になるように流
量調節弁25が開けられてその開度が調節され、これに
より350℃上限に調節された補助蒸気17aが予熱装
置Hに供給されるようになる。
When the temperature of the superheater outlet steam 17 gradually rises and exceeds 350 ° C., the flow rate control valve 25 is opened so that the temperature detected by the temperature detector 24 becomes the required upper limit temperature, for example, 350 ° C. The opening degree of the auxiliary steam 17a is adjusted so that the auxiliary steam 17a adjusted to the upper limit of 350 ° C. is supplied to the preheating device H.

【0018】過熱器出口蒸気17の温度が400℃程度
に達すると、タービン入口弁11が開けられて過熱器出
口蒸気17が高圧タービンに供給されることにより高圧
タービン12のウォーミングが開始され、またタービン
出口管13の蒸気が横置再熱器14に導かれて再度過熱
された後、中圧或いは低圧のタービン15に導かれるこ
とにより該タービン15もウォーミングされるようにな
る。
When the temperature of the superheater outlet steam 17 reaches about 400 ° C., the turbine inlet valve 11 is opened and the superheater outlet steam 17 is supplied to the high pressure turbine to start warming of the high pressure turbine 12, Further, the steam in the turbine outlet pipe 13 is guided to the horizontal reheater 14 to be superheated again, and then is guided to the intermediate or low pressure turbine 15, so that the turbine 15 is also warmed.

【0019】高圧タービン12及びタービン15のウォ
ーミング終了後、高圧タービン12及びタービン15に
徐々に負荷が掛けられ(発電機接続)、負荷が50パー
セント(ハーフロード)程度になると、前記開閉弁32
が閉じられて開閉弁31が開けられ、これにより以後は
過熱器出口蒸気17による補助蒸気17aに代えて、タ
ービン出口管13からの蒸気が補助蒸気抽出管27によ
り補助蒸気17cとして予熱装置Hに供給されるように
なる。
After the warming of the high-pressure turbine 12 and the turbine 15, the high-pressure turbine 12 and the turbine 15 are gradually loaded (connected to the generator), and when the load reaches about 50% (half load), the on-off valve 32 is opened.
Is closed and the on-off valve 31 is opened, and thereafter, instead of the auxiliary steam 17a by the superheater outlet steam 17, the steam from the turbine outlet pipe 13 is supplied to the preheater H as the auxiliary steam 17c by the auxiliary steam extraction pipe 27. Will be supplied.

【0020】[0020]

【発明が解決しようとする課題】しかし、前記図2に示
した従来の自然循環形ボイラの補助蒸気装置において
は、給水ポンプ4からの給水の一部をスプレー給水管2
1に備えた2段式の減圧弁23によって減圧した後、ス
プレー混合器20により過熱器出口蒸気17を減圧した
後の補助蒸気17aに混合して冷却し、予熱装置Hに供
給する補助蒸気17aの温度を設定上限温度以下に調節
するようにしているため、給水ポンプ4からの高い圧力
(205kg/cm2程度)の水5を低い圧力(42k
g/cm2程度)まで減圧する必要があり、しかも補助
蒸気17aの冷却のために使用する水5の量は少ないた
めに、2段式の減圧弁23は非常に大きな減圧幅を要求
される厳しい条件で使用されることになり、そのために
減圧弁23がエロージョンにより短時間で使用できなく
なったり、また減圧弁23のエロージョンの影響によっ
て流量調節弁25も苛酷な条件で使用されることになっ
て寿命が短縮されてしまう等の問題があり、更に近年で
は電力の要求量の変動に応じて自然循環形ボイラ1の起
動、停止が頻繁に繰返されるようになってきており、こ
のために前記減圧弁23、流量調節弁25が更に苛酷に
使用されることになり、よって減圧弁23、流量調節弁
25を短期間で交換する必要が生じたり、この減圧弁2
3、流量調節弁25の製作、選定が大変であると共に、
高価であるためにコストが増加するといった問題を有し
ていた。
However, in the conventional auxiliary steam apparatus of the natural circulation boiler shown in FIG. 2, a part of the water supply from the water supply pump 4 is sprayed into the water supply pipe 2.
After decompressing by the two-stage decompression valve 23 provided in 1, the superheater outlet steam 17 is mixed with the decompressed auxiliary steam 17a by the spray mixer 20 to be cooled and supplied to the preheating device H. Since the temperature of the water is adjusted to be equal to or lower than the set upper limit temperature, the water 5 having a high pressure (about 205 kg / cm 2 ) from the water supply pump 4 is supplied to the low pressure (42 k).
g / cm 2 or so) until it is necessary to reduce the pressure, yet for the amount of water 5 to be used for the cooling of the auxiliary steam 17a is small, the pressure reducing valve 23 of the two-stage is required a very large pressure decrease The pressure reducing valve 23 cannot be used for a short time due to erosion due to strict conditions, and the erosion of the pressure reducing valve 23 also causes the flow rate control valve 25 to be used under severe conditions. However, in recent years, the natural circulation boiler 1 has been frequently started and stopped in response to fluctuations in the required amount of electric power. Since the pressure reducing valve 23 and the flow rate adjusting valve 25 are used more severely, it becomes necessary to replace the pressure reducing valve 23 and the flow rate adjusting valve 25 in a short period of time.
3. It is difficult to manufacture and select the flow rate control valve 25.
Since it is expensive, there is a problem that the cost increases.

【0021】また、従来の装置は、減圧後の補助蒸気1
7aに水5を混合することによって補助蒸気17aの温
度を要求上限温度以下に下げるようにしているために、
蒸気と水との混合であって均一な混合が行われにくく、
且つ振動も発生しやすく、このためにスプレー混合器2
0を設置するようにしているが、このスプレー混合器2
0は高価であり、しかもエロージョンを生じやすくメン
テナンスが大変であるといった問題がある。
In the conventional apparatus, the auxiliary steam 1 after depressurization is used.
Since the temperature of the auxiliary steam 17a is lowered below the required upper limit temperature by mixing the water 5 with 7a,
As it is a mixture of steam and water, it is difficult to mix it uniformly,
Moreover, vibration is also likely to occur, which is why the spray mixer 2
0 is installed, but this spray mixer 2
There is a problem that 0 is expensive, and moreover, erosion is likely to occur and maintenance is difficult.

【0022】本発明は、斯かる実情に鑑みてなしたもの
で、過熱器出口蒸気の温度を、簡単な構成で容易に補助
蒸気の要求上限温度まで冷却することができるようにし
た自然循環形ボイラの補助蒸気装置を提供することを目
的としている。
The present invention has been made in view of such circumstances, and is a natural circulation type in which the temperature of the superheater outlet steam can be easily cooled to the required upper limit temperature of the auxiliary steam with a simple structure. It is intended to provide an auxiliary steam device for a boiler.

【0023】[0023]

【課題を解決するための手段】本発明の自然循環形ボイ
ラの補助蒸気装置は、自然循環形ボイラに備える過熱器
の過熱器出口蒸気を、減圧オリフィスを備えた過熱補助
蒸気管を介して当該自然循環形ボイラの予熱装置に補助
蒸気として供給するようにしている自然循環形ボイラの
補助蒸気装置であって、自然循環形ボイラのドラムの飽
和蒸気を取り出して前記過熱補助蒸気管に合流させるよ
うにした飽和蒸気混合管を配設し、且つ前記過熱補助蒸
気管における減圧オリフィスより下流側に温度検出器を
配置し、更に前記飽和蒸気混合管に、前記温度検出器の
検出温度に基づいて飽和蒸気の流量を調節する流量調節
弁を備えたことを特徴とするものである。
According to the auxiliary steam apparatus for a natural circulation boiler of the present invention, the superheater outlet steam of the superheater provided in the natural circulation boiler is passed through a superheat auxiliary steam pipe provided with a pressure reducing orifice. It is an auxiliary steam device for a natural circulation boiler that is supplied as an auxiliary steam to a preheating device for a natural circulation boiler, and takes out saturated steam from a drum of the natural circulation boiler and joins it with the superheat auxiliary steam pipe. The saturated steam mixing pipe, and a temperature detector is arranged downstream of the pressure reducing orifice in the superheat auxiliary steam pipe, and the saturated steam mixing pipe is saturated based on the temperature detected by the temperature detector. It is characterized in that a flow control valve for controlling the flow rate of steam is provided.

【0024】また、ドラムの飽和蒸気を取り出す飽和蒸
気混合管を、ドラムに接続されている再熱器安全弁テス
ト蒸気管に接続したことを特徴とするものである。
Further, the present invention is characterized in that the saturated steam mixing pipe for taking out the saturated steam of the drum is connected to the reheater safety valve test steam pipe connected to the drum.

【0025】本発明では、過熱器出口蒸気をドラム出口
の飽和蒸気で冷却することにより補助蒸気を得るように
しているので、飽和蒸気の圧力を調節するための手段を
何等必要とせず、簡単な構成とすることができ、更に蒸
気同士の混合であるために単に過熱補助蒸気管に飽和蒸
気混合管を直交させて接続するのみで、振動等を生じる
ことなく容易且つ均一に混合させることができる。
In the present invention, since the auxiliary steam is obtained by cooling the steam at the outlet of the superheater with the saturated steam at the outlet of the drum, any means for adjusting the pressure of the saturated steam is not required, and it is simple. In addition, since the vapors are mixed with each other, the saturated steam mixing pipe is simply connected to the superheating auxiliary steam pipe so as to be orthogonal to each other, so that the mixture can be easily and uniformly mixed without causing vibration or the like. .

【0026】また、ドラムに接続されている再熱器安全
弁テスト蒸気管に飽和蒸気混合管を接続してドラムの飽
和蒸気の一部を取り出すようにすると、自然循環形ボイ
ラの新設時にしか使用されない再熱器安全弁テスト蒸気
管を有効に利用することができ、ドラムの改造を行う必
要がない。
If a saturated steam mixing pipe is connected to the reheater safety valve test steam pipe connected to the drum so that a part of the saturated steam in the drum is taken out, it is used only when a natural circulation boiler is newly installed. Reheater safety valve test The steam pipe can be effectively used and the drum need not be modified.

【0027】[0027]

【発明の実施の形態】以下、本発明の実施の形態を、図
示例と共に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings.

【0028】図1は、前記図2の従来の自然循環形ボイ
ラの補助蒸気装置に適用した本発明を実施する形態の一
例を示したもので、図中同一の符号を付したものは同一
物を表わしている。
FIG. 1 shows an example of an embodiment for carrying out the present invention applied to the conventional auxiliary steam apparatus for a natural circulation type boiler shown in FIG. 2, in which the same reference numerals are attached to the same parts. Is represented.

【0029】図1に示すように、図2における従来のス
プレー給水管21を廃止し、自然循環形ボイラ1のドラ
ム3に接続されている再熱器安全弁テスト蒸気管28に
おけるドラム3と遮断弁29との間に、ドラム3の飽和
蒸気3aの一部を取り出して過熱補助蒸気管18の過熱
器出口蒸気17に合流させるようにした飽和蒸気混合管
35を設ける。
As shown in FIG. 1, the conventional spray water supply pipe 21 in FIG. 2 is abolished, and the drum 3 and the shutoff valve in the reheater safety valve test steam pipe 28 connected to the drum 3 of the natural circulation boiler 1 are removed. A saturated steam mixing pipe 35 is provided between the saturated steam mixing pipe 35 and the saturated steam mixing pipe 29 so that a part of the saturated steam 3a of the drum 3 is taken out and merged with the superheater outlet steam 17 of the superheat auxiliary steam pipe 18.

【0030】更に、前記過熱補助蒸気管18における減
圧オリフィス19(或いは減圧弁)の下流側に温度検出
器36を配置すると共に、前記飽和蒸気混合管35に流
量調節弁37を配設し、前記温度検出器36の検出温度
が要求上限温度(例えば350℃)以上になると前記流
量調節弁37を開けて飽和蒸気混合管35を流れる飽和
蒸気3aの流量を調節することにより過熱器出口蒸気1
7を飽和蒸気3aによって冷却し、補助蒸気17aの温
度が要求上限温度以上にならないようにしている。
Further, a temperature detector 36 is arranged downstream of the pressure reducing orifice 19 (or pressure reducing valve) in the superheat auxiliary steam pipe 18, and a flow rate control valve 37 is arranged in the saturated steam mixing pipe 35. When the temperature detected by the temperature detector 36 becomes equal to or higher than the required upper limit temperature (for example, 350 ° C.), the flow rate control valve 37 is opened to adjust the flow rate of the saturated steam 3a flowing through the saturated steam mixing pipe 35, thereby the superheater outlet steam 1
7 is cooled by the saturated steam 3a so that the temperature of the auxiliary steam 17a does not exceed the required upper limit temperature.

【0031】自然循環形ボイラ1の起動初期は、従来と
同様に補助ボイラ26を駆動して、補助ボイラ26から
の補助蒸気17bを予熱装置Hに供給している。
At the initial start-up of the natural circulation boiler 1, the auxiliary boiler 26 is driven in the same manner as in the conventional case, and the auxiliary steam 17b from the auxiliary boiler 26 is supplied to the preheating device H.

【0032】ドラム3に導入される蒸気量が増加してド
ラム3内圧力が例えば10kg/cm2程度になりドラ
ム3出口の蒸気温度が190℃程度になると、開閉弁3
3を閉じると共に開閉弁32を開けて、過熱補助蒸気管
18からの過熱器出口蒸気17を補助蒸気17aとして
予熱装置Hに供給するようにし、この時補助ボイラ26
からの補助蒸気17bの供給を停止して、補助ボイラ2
6によるエネルギの消費量を節約する。
When the amount of steam introduced into the drum 3 increases and the internal pressure of the drum 3 reaches, for example, about 10 kg / cm 2 and the steam temperature at the outlet of the drum 3 reaches about 190 ° C., the on-off valve 3
3 is closed and the on-off valve 32 is opened to supply the superheater outlet steam 17 from the superheat auxiliary steam pipe 18 to the preheating device H as the auxiliary steam 17a.
Stop the supply of the auxiliary steam 17b from the auxiliary boiler 2
Save energy consumption by 6.

【0033】過熱器出口蒸気17の温度が徐々に上昇し
て350℃を越えるようになると、減圧オリフィス19
の下流に設けられた温度検出器36の検出温度が要求上
限温度の例えば350℃になるように流量調節弁37が
開けられてその開度が調節され、これにより350℃上
限に調節された補助蒸気17aが予熱装置Hに供給され
るようになる。
When the temperature of the superheater outlet steam 17 gradually rises and exceeds 350 ° C., the pressure reducing orifice 19
The flow rate control valve 37 is opened and the opening thereof is adjusted so that the temperature detected by the temperature detector 36 provided downstream of the temperature control device reaches the required upper limit temperature of, for example, 350 ° C. The steam 17a comes to be supplied to the preheating device H.

【0034】この時、420℃程度である過熱器出口蒸
気17を、190℃程度の飽和蒸気3aで冷却するよう
にしているので、過熱器出口蒸気17の10〜20%の
飽和蒸気3aを供給するのみで350℃の補助蒸気17
aとすることができ、しかも飽和蒸気3aの圧力を調節
するための手段等を何等必要とせず、更に蒸気3a,1
7同士の混合であるために単に過熱補助蒸気管18に飽
和蒸気混合管35を直交させて接続するのみで、振動等
を生じることなく容易且つ均一に混合させることができ
る。
At this time, since the superheater outlet steam 17 of about 420 ° C. is cooled by the saturated steam 3a of about 190 ° C., 10 to 20% of the saturated steam 3a of the superheater outlet steam 17 is supplied. Auxiliary steam at 350 ℃ 17
a, and does not require any means for adjusting the pressure of the saturated steam 3a.
Since the seven steams are mixed with each other, the saturated steam mixing pipe 35 is simply connected to the superheat auxiliary steam pipe 18 so as to be orthogonal to each other, so that the superheated auxiliary steam pipe 18 can be easily and uniformly mixed without causing vibration or the like.

【0035】また、図1に示したように、ドラム3に接
続されている再熱器安全弁テスト蒸気管28に飽和蒸気
混合管35を接続してドラム3の飽和蒸気3aの一部を
取り出すようにしているので、自然循環形ボイラ1の新
設時にしか使用されない再熱器安全弁テスト蒸気管28
を有効に利用することができ、よってドラム3の改造を
行う必要がない。
Further, as shown in FIG. 1, a saturated steam mixing pipe 35 is connected to the reheater safety valve test steam pipe 28 connected to the drum 3 so that a part of the saturated steam 3a of the drum 3 is taken out. The reheater safety valve test steam pipe 28 is used only when the natural circulation boiler 1 is newly installed.
Can be effectively used, so that it is not necessary to modify the drum 3.

【0036】上記したように、過熱器出口蒸気17に飽
和蒸気3aを混合して温度が調節された補助蒸気17a
の予熱装置Hへの供給は、従来と同様に高圧タービン1
2及びタービン15がハーフロード程度になるまで続け
られ、以後は過熱器出口蒸気17による補助蒸気17a
に代えて、タービン出口管13からの蒸気が補助蒸気抽
出管27により補助蒸気17cとして予熱装置Hに供給
されるようになる。
As described above, the auxiliary steam 17a whose temperature is adjusted by mixing the saturated steam 3a with the superheater outlet steam 17
Is supplied to the preheating device H in the same manner as the conventional one.
2 and the turbine 15 are continued until about half load, and thereafter, the auxiliary steam 17a by the superheater outlet steam 17
Instead, the steam from the turbine outlet pipe 13 is supplied to the preheating device H as the auxiliary steam 17c by the auxiliary steam extraction pipe 27.

【0037】[0037]

【発明の効果】本発明の自然循環形ボイラの補助蒸気装
置によれば、過熱器出口蒸気をドラム出口の飽和蒸気で
冷却することにより補助蒸気を得るようにしているの
で、飽和蒸気の圧力を調節するための手段を何等必要と
せず、簡単な構成とすることができ、更に蒸気同士の混
合であるために単に過熱補助蒸気管に飽和蒸気混合管を
直交させて接続するのみで、振動等を生じることなく容
易且つ均一に混合させることができる。
According to the auxiliary steam device for a natural circulation type boiler of the present invention, the auxiliary steam is obtained by cooling the steam at the outlet of the superheater with the saturated steam at the outlet of the drum. It does not require any means for adjustment and can have a simple structure. Furthermore, since it is a mixture of steams, it is only necessary to connect the saturated steam mixing pipe to the superheat auxiliary steam pipe at right angles, and vibration etc. It can be mixed easily and uniformly without causing

【0038】また、ドラムに接続されている再熱器安全
弁テスト蒸気管に飽和蒸気混合管を接続してドラムの飽
和蒸気の一部を取り出すようにすると、自然循環形ボイ
ラの新設時にしか使用されない再熱器安全弁テスト蒸気
管を有効に利用することができ、ドラムの改造を行う必
要がない。
If a saturated steam mixing pipe is connected to the reheater safety valve test steam pipe connected to the drum so that a part of the saturated steam in the drum is taken out, it is used only when a natural circulation boiler is newly installed. Reheater safety valve test The steam pipe can be effectively used and the drum need not be modified.

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

【図1】本発明を実施する形態の一例を示すフローチャ
ートである。
FIG. 1 is a flowchart showing an example of an embodiment for carrying out the present invention.

【図2】従来の自然循環形ボイラの主要構成の一例を示
すフローチャートである。
FIG. 2 is a flowchart showing an example of a main configuration of a conventional natural circulation boiler.

【符号の説明】[Explanation of symbols]

1 自然循環形ボイラ 3 ドラム 3a 飽和蒸気 10 過熱器 17 過熱器出口蒸気 17a 補助蒸気 18 過熱補助蒸気管 19 減圧オリフィス(或いは減圧弁) 28 再熱器安全弁テスト蒸気管 35 飽和蒸気混合管 36 温度検出器 37 流量調節弁 H 予熱装置 1 Natural circulation boiler 3 Drum 3a Saturated steam 10 Superheater 17 Superheater outlet steam 17a Auxiliary steam 18 Superheat auxiliary steam pipe 19 Pressure reducing orifice (or pressure reducing valve) 28 Reheater safety valve test steam pipe 35 Saturated steam mixing pipe 36 Temperature detection 37 Flow control valve H Preheating device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 自然循環形ボイラに備える過熱器の過熱
器出口蒸気を、減圧オリフィスを備えた過熱補助蒸気管
を介して当該自然循環形ボイラの予熱装置に補助蒸気と
して供給するようにしている自然循環形ボイラの補助蒸
気装置であって、自然循環形ボイラのドラムの飽和蒸気
を取り出して前記過熱補助蒸気管に合流させるようにし
た飽和蒸気混合管を配設し、且つ前記過熱補助蒸気管に
おける減圧オリフィスより下流側に温度検出器を配置
し、前記飽和蒸気混合管に、前記温度検出器の検出温度
に基づいて飽和蒸気の流量を調節する流量調節弁を備え
たことを特徴とする自然循環形ボイラの補助蒸気装置。
1. A superheater outlet steam of a superheater provided in a natural circulation boiler is supplied as auxiliary steam to a preheater of the natural circulation boiler via a superheat auxiliary steam pipe provided with a pressure reducing orifice. An auxiliary steam device for a natural circulation type boiler, wherein a saturated steam mixing tube is arranged to take out saturated steam from a drum of the natural circulation type boiler and join the superheated auxiliary steam tube. A temperature detector is arranged on the downstream side of the decompression orifice in, and the saturated vapor mixing pipe is provided with a flow rate control valve for adjusting the flow rate of saturated vapor based on the temperature detected by the temperature detector. Auxiliary steam equipment for circulating boilers.
【請求項2】 ドラムの飽和蒸気を取り出す飽和蒸気混
合管を、ドラムに接続されている再熱器安全弁テスト蒸
気管に接続したことを特徴とする請求項1記載の自然循
環形ボイラの補助蒸気装置。
2. Auxiliary steam for a natural circulation boiler according to claim 1, wherein the saturated steam mixing pipe for extracting saturated steam from the drum is connected to a reheater safety valve test steam pipe connected to the drum. apparatus.
JP14357596A 1996-05-14 1996-05-14 Auxiliary steam equipment of natural circulation boiler Pending JPH09303710A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14357596A JPH09303710A (en) 1996-05-14 1996-05-14 Auxiliary steam equipment of natural circulation boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14357596A JPH09303710A (en) 1996-05-14 1996-05-14 Auxiliary steam equipment of natural circulation boiler

Publications (1)

Publication Number Publication Date
JPH09303710A true JPH09303710A (en) 1997-11-28

Family

ID=15341937

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14357596A Pending JPH09303710A (en) 1996-05-14 1996-05-14 Auxiliary steam equipment of natural circulation boiler

Country Status (1)

Country Link
JP (1) JPH09303710A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008506918A (en) * 2004-07-13 2008-03-06 チャンミョン シーエス カンパニー リミテッド Once-through boiler

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008506918A (en) * 2004-07-13 2008-03-06 チャンミョン シーエス カンパニー リミテッド Once-through boiler

Similar Documents

Publication Publication Date Title
US5540045A (en) Steam injection system for a combustion turbine gas generator
JP2000161014A (en) Combined power generator facility
JP2005534883A (en) Waste heat steam generator
JP4670707B2 (en) Control apparatus and control method for steam power plant
JP3559574B2 (en) Startup method of single-shaft combined cycle power plant
JPH09303710A (en) Auxiliary steam equipment of natural circulation boiler
JPH06323162A (en) Steam-cooled gas turbine power plant
JPH04148035A (en) Vapor cooled gas turbine system
JP3641518B2 (en) Steam temperature control method and apparatus for combined cycle plant
JP2000028102A (en) Auxiliary steam control method in boiler for thermal electric power generation
JPH0734810A (en) Method for starting of single-shaft type combined cycle generating equipment
JPS58192908A (en) Control device of combined cycle turbine plant
RU181138U1 (en) STEAM GENERATOR
JPS5847105A (en) Starting equipment for combined plant
JPH02130202A (en) Combined plant
Anisimov et al. Optimization of Start-Up of a Fully Fired Combined-Cycle Plant with GT13E2 Gas Turbine
JPH11159305A (en) Pressurized fluidized bed combined generating plant
JPH01212802A (en) Steam temperature control device for boiler
JPH01306703A (en) Starting control method for once-through boiler
JPH08121708A (en) Water spray controlling device of reheat steam system temperature decreasing device
JP3117392B2 (en) Start-up method of an exhaust gas re-combustion complex plant
JP2716442B2 (en) Waste heat recovery boiler device
JPS63230911A (en) Control device for combined cycle power plant
Anisimov et al. Development and Implementation of Automatic Conversion of Steam-Gas Power Unit from Compound Cycle Mode to Steam-Power Mode Without Shutdown of the Unit
JPH08135405A (en) High pressure turbine bypass steam temperature control method and its device