JPS62141407A - Controller for injection quantity of cooling water for steamdesuperheater - Google Patents

Controller for injection quantity of cooling water for steamdesuperheater

Info

Publication number
JPS62141407A
JPS62141407A JP28153285A JP28153285A JPS62141407A JP S62141407 A JPS62141407 A JP S62141407A JP 28153285 A JP28153285 A JP 28153285A JP 28153285 A JP28153285 A JP 28153285A JP S62141407 A JPS62141407 A JP S62141407A
Authority
JP
Japan
Prior art keywords
steam
cooling water
flow rate
temperature
injection amount
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
Application number
JP28153285A
Other languages
Japanese (ja)
Other versions
JPH0555762B2 (en
Inventor
泡田 秀美
周防 幸夫
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.)
Kanebo Ltd
Original Assignee
Kanebo Ltd
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 Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP28153285A priority Critical patent/JPS62141407A/en
Publication of JPS62141407A publication Critical patent/JPS62141407A/en
Publication of JPH0555762B2 publication Critical patent/JPH0555762B2/ja
Granted legal-status Critical Current

Links

Landscapes

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

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は蒸気減温器の冷却水噴射量制御装置に関し、
特に、過熱蒸気に冷却水を噴射して、過熱蒸気の温度を
所定の温度に低下させるような蒸気減温器の冷却水噴射
量制御装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] This invention relates to a cooling water injection amount control device for a steam desuperheater.
In particular, the present invention relates to a cooling water injection amount control device for a steam desuperheater that injects cooling water into superheated steam to lower the temperature of the superheated steam to a predetermined temperature.

[従来の技術1 蒸気を用いて物質を加熱りる場合、飽和蒸気にすること
が望ましい。第3図Li過熱蒸気を飽和蒸気にするため
の従来の蒸気減4,51器の冷7J]水噴射!H制御装
而の制御系を示J図であり、第4図は蒸気の状態図であ
る。
[Prior art 1] When heating a substance using steam, it is desirable to use saturated steam. Figure 3. Conventional steam reducer 4,51 cooling 7J for converting Li superheated steam to saturated steam] Water injection! The control system of the H control system is shown in diagram J, and FIG. 4 is a state diagram of steam.

第3図において、過熱蒸気配管1には過熱蒸気が供給さ
れ、過熱蒸気配管1内の蒸気圧は圧力検出器2によって
検出される。圧力検出器2の検出出力は蒸気圧力調節器
3にl、Jえられ、蒸気圧力調節器3は圧力検出器2に
J、って検出された蒸気圧に基づいて、予めaシ定され
た蒸気圧となるにうに圧力調節弁4を制す11する。そ
れによって、過熱蒸気配管1内の圧ノJ GJニ一定に
保たれる。過熱蒸気配管1には、冷却水噴射装置7が設
けられている。
In FIG. 3, superheated steam is supplied to a superheated steam pipe 1, and the steam pressure inside the superheated steam pipe 1 is detected by a pressure detector 2. The detection output of the pressure detector 2 is sent to the steam pressure regulator 3, and the steam pressure regulator 3 is set in advance based on the steam pressure detected by the pressure detector 2. Pressure regulating valve 4 is controlled 11 until the steam pressure is reached. Thereby, the pressure inside the superheated steam pipe 1 is kept constant. The superheated steam pipe 1 is provided with a cooling water injection device 7 .

そして、過熱蒸気配管1の出「1側にL;L 、温石検
出器5が設けられ、過熱蒸気の温度が検出される。
A hot stone detector 5 is provided on the output 1 side of the superheated steam pipe 1 to detect the temperature of the superheated steam.

この温度検出器5で検出された温度は蒸気温度調節器6
に与えられる。蒸気温度調節器6は温度検出器5で検出
された温度が予め設定された温1立となるJこうに、冷
却水噴射装u7に供給する冷却水の流量を制御する。こ
の冷)J)J水噴射装置7によって過熱蒸気に冷iJI
水が噴射され、過熱蒸気配管1の出]二1側には減温さ
れた過熱蒸気が19られる。すなわち、過熱蒸気F!i
! ’i′X1の出口側は、蒸気温度が=一定となるJ
、うに調節される。
The temperature detected by this temperature detector 5 is determined by the steam temperature controller 6.
given to. The steam temperature regulator 6 controls the flow rate of the cooling water supplied to the cooling water injection device u7 so that the temperature detected by the temperature detector 5 reaches a preset temperature. This cooled iJI into superheated steam by J)J water injection device 7
Water is injected, and superheated steam 19 whose temperature has been reduced is supplied to the outlet 21 side of the superheated steam pipe 1. In other words, superheated steam F! i
! On the exit side of 'i'X1, the steam temperature is constant J
, adjusted to sea urchins.

[発明が解決しJ:うとする問題点] ところで、飽和蒸気は、第4図に示すように、温度が一
定であってら、エンタルピーの大きさにJ、って乾き度
が異なる。このため、土述のごとく、過熱蒸気の温石を
検出して、一定の温度となるように冷却水のq1射h1
を制6Il′?Iる場合、使用する蒸気の流量が安定し
ていなりれば減温後の過熱度をOにすることは困難にな
る。=般に、過熱蒸気を用いIζ系にJ3いては、蒸気
の流量が刻々変化しているため、減温後の過熱度をOに
するために、若干の過熱度を持たせた過熱蒸気となるよ
うに調節していた。
[Problems to be Solved by the Invention] Incidentally, as shown in FIG. 4, even if the temperature of saturated steam is constant, the degree of dryness of saturated steam differs by the amount of enthalpy. For this reason, as mentioned above, the hot stone of superheated steam is detected and the cooling water q1 is injected h1 to maintain a constant temperature.
Control 6Il'? In this case, if the flow rate of the steam used is not stable, it becomes difficult to achieve a superheat degree of O after temperature reduction. =Generally, when superheated steam is used in the Iζ system J3, the flow rate of the steam changes from moment to moment, so in order to make the degree of superheating after temperature reduction O, superheated steam with a slight degree of superheating and I adjusted it accordingly.

しかし4L:がら、この調整は困荊であり、物体を加熱
用の蒸気として使用するには不適切であった。
However, this adjustment was difficult and unsuitable for use as steam for heating objects.

それゆえに、この発明の主たる目的は、減温後の蒸気が
乾き飽和蒸気と4Tる。1.うに、過熱蒸気。
Therefore, the main object of the present invention is to dry the steam after cooling to a temperature equal to 4T of saturated steam. 1. Sea urchin, superheated steam.

冷却水のそれぞれの−[ンタルピから過熱蒸気流量に見
合う冷却水を唱CIJ L、1J11熱用蒸気として適
切なものに加工しv、する蒸気減記器の冷7JI水噴射
量制御装置を提供することである。
To provide a cold 7JI water injection amount control device for a steam subtractor that processes cooling water corresponding to the superheated steam flow rate from each of the cooling water into a suitable steam for heating. That's true.

[問題点を解決づ−るための手段] この発明にかかる蒸気減滉器の冷却水噴射量制御装置は
、過熱蒸気の温度4検出づるための温度検出手段と、過
熱蒸気の流量を検出でるだめの蒸気流量検出手段と、検
出された温度と流出とに基づいて、予め設定された乾き
飽和蒸気にづるための冷却水の噴射量を演算づる1I(
I咋制御手段と、演算された噴射量に基づいて冷却水を
過熱蒸気に噴射する冷却水噴射手段とから措成される。
[Means for Solving the Problems] A cooling water injection amount control device for a steam attenuator according to the present invention includes a temperature detection means for detecting the temperature 4 of superheated steam and a flow rate of the superheated steam. 1I(
It consists of an I-temperature control means and a cooling water injection means for injecting cooling water into the superheated steam based on the calculated injection amount.

[作用] この発明にかかる蒸気減?flA器の冷却水噴射量制御
装置は、過熱蒸気の温度と蒸気流量とに基づいて、予め
設定された乾き飽和蒸気にするための冷却水の噴射量を
演算し、イの演算結果に基づいて冷t’、n水の噴射量
を制御づるようにしたので、蒸気流量の変動が大きい系
においても、過熱蒸気を加熱用蒸気として適した状態の
乾き飽和蒸気に加工Jることがで′きる。
[Operation] Does this invention reduce steam? The cooling water injection amount control device of the flA unit calculates the injection amount of cooling water to make the preset dry saturated steam based on the temperature of the superheated steam and the steam flow rate, and based on the calculation result of (a) Since the injection amount of cold water can be controlled, superheated steam can be processed into dry saturated steam suitable as heating steam even in systems where the steam flow rate fluctuates greatly. .

[発明の実施例] 第1図はこの発明の一実施例の制御系を示す概要図であ
り、第2図は第1図に示した冷却水流量設定器の貝体的
イ1ブロック図である。
[Embodiment of the Invention] FIG. 1 is a schematic diagram showing a control system of an embodiment of the present invention, and FIG. 2 is a schematic block diagram of the cooling water flow rate setting device shown in FIG. 1. be.

まず、第1図J3よび第2図を参照して、この発明の一
実施例の描或について説明覆る。第1図において、過熱
熱気配管1と圧力検出器2と蒸気圧力調節器3と圧力調
節弁1は前述の第3図に示したものと同じらのが用いら
れる。さらに、過熱蒸気配管1には、この過熱蒸気配管
1内の過熱蒸気の流量を検出する蒸気流量検出器8と、
過熱蒸気の湿度を検出器る温度検出器5とが設けられる
First, an embodiment of the present invention will be described with reference to FIG. 1 J3 and FIG. 2. In FIG. 1, the same superheated air piping 1, pressure detector 2, steam pressure regulator 3, and pressure regulating valve 1 as shown in FIG. 3 are used. Furthermore, the superheated steam pipe 1 includes a steam flow rate detector 8 that detects the flow rate of superheated steam in the superheated steam pipe 1,
A temperature detector 5 is provided to detect the humidity of the superheated steam.

蒸気流量検出器8によって検出されlζ流量と温度検出
器5によって検出された温度は冷却水流量設定器9に与
えられる。冷却水流量設定器9は入力された流量a3よ
び温度と予め設定された情報と任意の関数に基づいて、
蒸気流量に対応覆る冷却水の流量を演算し、冷7J1水
流員調節器11の流量を調節する。冷却水流h′)調1
1i′i器11には冷月1水の流量を検出する水流量検
出器10からの検出出力が与えられていて、この水流量
検出器10で検出された流量が冷却水流I’ll設定器
9【・演陣された流量となるように、冷ノ、0水噴θ=
I 装置7を制御する。それによって、冷却水噴射装置
7からは、蒸気流量に対応する冷却水が噴射され、乾き
飽和蒸気に加工されて出力される。
The lζ flow rate detected by the steam flow rate detector 8 and the temperature detected by the temperature detector 5 are provided to a cooling water flow rate setting device 9. Based on the input flow rate a3 and temperature, preset information, and an arbitrary function, the cooling water flow rate setting device 9
The flow rate of cooling water corresponding to the steam flow rate is calculated, and the flow rate of the cold 7J1 water flow controller 11 is adjusted. Cooling water flow h') control 1
1i'i device 11 is given a detection output from a water flow rate detector 10 that detects the flow rate of cold moon 1 water, and the flow rate detected by this water flow rate detector 10 is applied to the cooling water flow I'll setting device. 9 [・Cold water jet, 0 water jet θ=
I Control the device 7. Thereby, cooling water corresponding to the steam flow rate is injected from the cooling water injection device 7, processed into dry saturated steam, and output.

次に、冷却水流ffi RQ定器9についてjJ細に説
明する。冷却水流量設定器9は第2図に示すように、入
力バッフ791と定数設定器92とマルチプレクサ93
とΔ/D変換器9/lと制御部95と出力回路96と表
示器97とから椙成される。入力バッファ91には、上
述の第1図に示した蒸気流量検出器8で検出されlこ蒸
気流、111と、湿IQ検出器5で検出された蒸気湿度
とが′iえられる。なお、この入力バッファ91に11
1月力検出器2によって検出された蒸気圧力を入力ηる
とともに、冷却水の温度を検出してその温度情報を与え
るようにしてもよい。定数設定器92は得ようとする乾
き飽和蒸気の■ンタルピと、冷却水量の上限値d3よび
下限値を設定づるbのである。入力バッファ91に入力
された各情報と定数設定器92で設定された設定値はマ
ルチプレクサ93に与えられる。マルチプレクリ−93
は入力バッファ91から与えられIζ各情報おにび定数
設定器92で設定された設定値を順次選択してΔ/D変
換器94に与える。
Next, the cooling water flow ffi RQ regulator 9 will be explained in detail. As shown in FIG. 2, the cooling water flow rate setting device 9 includes an input buffer 791, a constant setting device 92, and a multiplexer 93.
, a Δ/D converter 9/l, a control section 95, an output circuit 96, and a display 97. The input buffer 91 receives the steam flow 111 detected by the steam flow rate detector 8 shown in FIG. 1, and the steam humidity detected by the humidity IQ detector 5. Note that this input buffer 91 has 11
In addition to inputting the steam pressure detected by the force detector 2, the temperature of the cooling water may be detected and the temperature information may be provided. The constant setter 92 is used to set the desired dry saturated steam concentration and the upper limit value d3 and lower limit value of the amount of cooling water. Each piece of information input to the input buffer 91 and the set value set by the constant setter 92 are given to a multiplexer 93. Multiplayer Cree-93
is given from the input buffer 91 and sequentially selects the setting values set by the Iζ information and the constant setter 92 and supplies them to the Δ/D converter 94.

△/D変換器9/lはそれらの情報をディジタル信号に
変換し、制御部95に与える。
The Δ/D converter 9/l converts the information into a digital signal and provides it to the control section 95.

制御部95は入力された情報に基づいて、補正蒸気流量
J3よび冷却水量を演算する。すなわち、蒸気圧力をP
とし、蒸気温度を王とし、差圧を△pとし、注水温度を
Tvとし、補正蒸気流量をFSとし、冷却水量をFwと
すると、補正蒸気流量Fsは次式によって求められる。
The control unit 95 calculates the corrected steam flow rate J3 and the amount of cooling water based on the input information. That is, the steam pressure is P
The corrected steam flow rate Fs is determined by the following equation, where the steam temperature is expressed as Α, the differential pressure is expressed as Δp, the water injection temperature is expressed as Tv, the corrected steam flow rate is expressed as FS, and the amount of cooling water is expressed as Fw.

ただし、K1−に4は定数 また、冷却水ff)、 I−Wは次式によって求められ
る。
However, K1- and 4 are constants and cooling water ff), and I-W is determined by the following formula.

ただし、K5〜に13.Plは定数 上述のごとくして制御部95によって演算された補正蒸
気流量おJ:び冷却水量に基づいて、出力回路96は冷
入り水流ffi調11)器11に冷却水量を設定する。
However, 13. Pl is a constant. Based on the corrected steam flow rate J: and the amount of cooling water calculated by the control unit 95 as described above, the output circuit 96 sets the amount of cooling water in the cold water flow ffi adjuster 11).

冷却水流flI)調節器11は冷却水流量設定器9によ
って設定された冷J、11水吊に基づいて、冷却水噴射
装置7を制御1する。イれによって、過熱蒸気配管1の
出力側から乾き飽和蒸気が1!′lられる。
The cooling water flow flI) regulator 11 controls the cooling water injection device 7 based on the cooling water flow rate set by the cooling water flow rate setting device 9. Due to this, dry saturated steam is released from the output side of superheated steam pipe 1! 'l will be.

[発明の効果] 以上のように、この発明によれば、少なくとも過熱蒸気
の流量と温度とに基づいて、過熱蒸気を乾き飽和蒸気と
するために必要な冷却水の噴射量を演算し、これを冷却
水流量調節器の設定値として冷却水の流量を調節するよ
うにしたので、蒸気流量の変動が大ぎいプロセスにL1
5いても過熱蒸気を加熱用蒸気として適した状態の乾ぎ
飽和蒸気に加工することができる。したがって、過熱蒸
気を一〇− 用いた場合の加熱装置におりる加熱表面湿度の不均一性
や大きな熱応力の発生というような問題点を解決づるこ
とができる。
[Effects of the Invention] As described above, according to the present invention, the injection amount of cooling water required to make superheated steam dry and saturated steam is calculated based on at least the flow rate and temperature of superheated steam, and Since the flow rate of the cooling water is adjusted using the set value of the cooling water flow rate controller, L1 is used in processes where the steam flow rate fluctuates greatly.
5, superheated steam can be processed into dry saturated steam suitable for use as heating steam. Therefore, it is possible to solve problems such as non-uniformity of humidity on the heating surface of the heating device and generation of large thermal stress when superheated steam is used.

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

第1図はこの発明の一実施例の制御系を示す概要図であ
る。第2図は第1図に示した冷却水流量設定器の具体的
なブロック図である。第3図は従来の蒸気減温器の冷却
水噴射量制御装置の制御系を承り概要図である。第4図
は蒸気の状態図である。 図において、1は過熱蒸気配管、2は圧力検出器、3は
蒸気圧力調節器、4は圧力調節弁、5は温度検出器、7
は冷却水噴射装置、8は蒸気流量検出器、9は冷却水流
量設定器、10は水流量検出器、11は冷却水流量調節
器を示す。
FIG. 1 is a schematic diagram showing a control system of an embodiment of the present invention. FIG. 2 is a concrete block diagram of the cooling water flow rate setting device shown in FIG. 1. FIG. 3 is a schematic diagram of a control system of a conventional steam desuperheater cooling water injection amount control device. FIG. 4 is a state diagram of steam. In the figure, 1 is a superheated steam pipe, 2 is a pressure detector, 3 is a steam pressure regulator, 4 is a pressure regulating valve, 5 is a temperature detector, and 7
8 is a cooling water injection device, 8 is a steam flow rate detector, 9 is a cooling water flow rate setting device, 10 is a water flow rate detector, and 11 is a cooling water flow rate regulator.

Claims (3)

【特許請求の範囲】[Claims] (1)過熱蒸気を乾き飽和蒸気にするために、冷却水の
噴射量を制御するための蒸気減温器の冷却水噴射量制御
装置であって、 前記過熱蒸気の温度を検出するための温度検出手段、 前記過熱蒸気の流量を検出するための蒸気流量検出手段
、 前記温度検出手段によって検出された温度と前記蒸気流
量検出手段によって検出された流量とに基づいて、予め
設定された乾き飽和蒸気にするために前記冷却水の噴射
量を演算する演算制御手段、および 前記演算制御手段によって演算された噴射量に基づいて
、前記過熱蒸気に冷却水を噴射する冷却水噴射手段を備
えた、蒸気減温器の冷却水噴射量制御装置。
(1) A cooling water injection amount control device for a steam desuperheater for controlling the injection amount of cooling water in order to turn superheated steam into dry saturated steam, the device comprising: a temperature detecting device for detecting the temperature of the superheated steam; a detection means, a steam flow rate detection means for detecting the flow rate of the superheated steam, a preset dry saturated steam based on the temperature detected by the temperature detection means and the flow rate detected by the steam flow rate detection means. steam, comprising: an arithmetic control means for calculating the injection amount of the cooling water in order to achieve the desired temperature; and a cooling water injection means for injecting the cooling water into the superheated steam based on the injection amount calculated by the arithmetic and control means. Cooling water injection amount control device for desuperheater.
(2)さらに、前記過熱蒸気の圧力を検出する蒸気圧検
出手段を含み、 前記演算制御手段は、前記蒸気圧検出手段で検出された
圧力と、前記検出された温度および流量とに基づいて、
前記冷却水の噴射間を演算するようにした、特許請求の
範囲第1項記載の蒸気減温器の冷却水噴射量制御装置。
(2) Furthermore, it includes a steam pressure detection means for detecting the pressure of the superheated steam, and the arithmetic and control means is configured to:
A cooling water injection amount control device for a steam desuperheater according to claim 1, wherein the cooling water injection amount control device calculates the cooling water injection interval.
(3)さらに、前記冷却水の流量を検出するための流量
検出手段を含み、 前記冷却水噴射手段は、前記流量検出手段によって検出
された流量が前記演算された噴射量となるように前記過
熱蒸気に噴射される冷却水の流量を調整するようにした
、特許請求の範囲第1項記載の蒸気減温器の冷却水噴射
量制御装置。
(3) The cooling water injection means further includes a flow rate detection means for detecting the flow rate of the cooling water, and the cooling water injection means is configured to control the superheating so that the flow rate detected by the flow rate detection means becomes the calculated injection amount. A cooling water injection amount control device for a steam desuperheater according to claim 1, which adjusts the flow rate of cooling water injected into the steam.
JP28153285A 1985-12-13 1985-12-13 Controller for injection quantity of cooling water for steamdesuperheater Granted JPS62141407A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28153285A JPS62141407A (en) 1985-12-13 1985-12-13 Controller for injection quantity of cooling water for steamdesuperheater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28153285A JPS62141407A (en) 1985-12-13 1985-12-13 Controller for injection quantity of cooling water for steamdesuperheater

Publications (2)

Publication Number Publication Date
JPS62141407A true JPS62141407A (en) 1987-06-24
JPH0555762B2 JPH0555762B2 (en) 1993-08-17

Family

ID=17640484

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28153285A Granted JPS62141407A (en) 1985-12-13 1985-12-13 Controller for injection quantity of cooling water for steamdesuperheater

Country Status (1)

Country Link
JP (1) JPS62141407A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05141615A (en) * 1991-11-15 1993-06-08 Tlv Co Ltd Controlling device for quality of steam
JPH0694211A (en) * 1992-09-14 1994-04-05 Tlv Co Ltd Steam pressure reducing and temperature reducing apparatus
JP2005127638A (en) * 2003-10-24 2005-05-19 Toshiba Plant Systems & Services Corp Steam attemperator

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05141615A (en) * 1991-11-15 1993-06-08 Tlv Co Ltd Controlling device for quality of steam
JPH0694211A (en) * 1992-09-14 1994-04-05 Tlv Co Ltd Steam pressure reducing and temperature reducing apparatus
JP2005127638A (en) * 2003-10-24 2005-05-19 Toshiba Plant Systems & Services Corp Steam attemperator
JP4619643B2 (en) * 2003-10-24 2011-01-26 東芝プラントシステム株式会社 Steam desuperheater

Also Published As

Publication number Publication date
JPH0555762B2 (en) 1993-08-17

Similar Documents

Publication Publication Date Title
JPS62141407A (en) Controller for injection quantity of cooling water for steamdesuperheater
JPH0447416A (en) Flow rate control method
JPH0280511A (en) Method for controlling dew point of atmospheric gas in furnace
Matsumoto et al. Pre-programmed controller for a supersonic blowdown tunnel
SU1301434A1 (en) Method of automatic control for preventing hydration
JPS6227320B2 (en)
JPH0275841A (en) Multi-room type air-conditioning machine
JPS6149683B2 (en)
JPH0410361B2 (en)
JPH05172406A (en) Waste heat control device
JPS6237285B2 (en)
JPS6132403Y2 (en)
JPH02187506A (en) Control of temperature of reheating device
JPS6017609A (en) Temperature controller
JPS6050333A (en) Hot water temperature control device for instanteneous gas water heater
JPH0710404Y2 (en) Coal dryer temperature controller
JPH01174804A (en) Regulator for steam temperature
JPH0412329Y2 (en)
JPS63176605A (en) Warming controller
JPS56136213A (en) Controlling method and apparatus for water cooling for steel material in rolling process
JPS5484102A (en) Evaporator outlet steam tempeature controller
JPS6034006B2 (en) Steam temperature control device
JPH09145004A (en) Emergency shutdown control of device pressurized fluidized bed boiler
JPS6356441B2 (en)
JP2927633B2 (en) Blast furnace blast moisture control method and apparatus