JPH0555762B2 - - Google Patents

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Publication number
JPH0555762B2
JPH0555762B2 JP28153285A JP28153285A JPH0555762B2 JP H0555762 B2 JPH0555762 B2 JP H0555762B2 JP 28153285 A JP28153285 A JP 28153285A JP 28153285 A JP28153285 A JP 28153285A JP H0555762 B2 JPH0555762 B2 JP H0555762B2
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.)
Expired - Lifetime
Application number
JP28153285A
Other languages
Japanese (ja)
Other versions
JPS62141407A (en
Inventor
Hidemi Awata
Yukio Suo
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

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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] The present invention relates to a cooling water injection amount control device for a steam desuperheater, and in particular, it injects cooling water into superheated steam to control the temperature of the superheated steam to a predetermined temperature. The present invention relates to a cooling water injection amount control device for a steam desuperheater that reduces the amount of water to be injected.

[従来の技術] 蒸気を用いて物質を過熱する場合、飽和蒸気に
することが望ましい。第3図は過熱蒸気を飽和蒸
気にするための従来の蒸気減温器の冷却水噴射量
制御装置の制御系を示す図であり、第4図は蒸気
の状態図である。
[Prior Art] When using steam to superheat a substance, it is desirable to use saturated steam. FIG. 3 is a diagram showing a control system of a conventional cooling water injection amount control device for a steam desuperheater for converting superheated steam into saturated steam, and FIG. 4 is a steam state diagram.

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によつて検出される。圧力検出器2の検出
力は蒸気圧力調節器3に与えられ、蒸気圧力調節
器3は圧力検出器2によつて検出された蒸気圧に
基づいて、予め設定された蒸気圧となるように圧
力調節弁4を制御する。それによつて、過熱蒸気
配管1内の圧力は一定に保たれる。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。そ
して、過熱蒸気配管1の出口側には、温度検出器
5が設けられ、過熱蒸気の温度が検出される。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度とな
るように、冷却水噴射装置7に供給する冷却水の
流量を制御する。この冷却水噴射装置7によつて
過熱蒸気に冷却が噴射され、過熱蒸気配管1の出
口側には減温された過熱蒸気が得られる。すなわ
ち、過熱蒸気配管1の出口側は、蒸気温度が一定
となるように調節される。
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 power of the pressure detector 2 is given to the steam pressure regulator 3, and the steam pressure regulator 3 adjusts the pressure to a preset steam pressure based on the steam pressure detected by the pressure detector 2. Control valve 4. Thereby, the pressure within the superheated steam pipe 1 is kept constant. The superheated steam pipe 1 is provided with a cooling water injection device 7 . A temperature detector 5 is provided on the exit side of the superheated steam pipe 1 to detect the temperature of the superheated steam. The temperature detected by this temperature detector 5 is provided to a steam temperature controller 6. The steam temperature controller 6 controls the flow rate of cooling water supplied to the cooling water injection device 7 so that the temperature detected by the temperature detector 5 becomes a preset temperature. Cooling is injected into the superheated steam by the cooling water injection device 7, and superheated steam whose temperature has been reduced is obtained at the outlet side of the superheated steam pipe 1. That is, the outlet side of the superheated steam pipe 1 is adjusted so that the steam temperature is constant.

[発明が解決しようとする問題点] ところで、飽和蒸気は、第4図に示すように、
温度が一定であつても、エンタルピーの大きさに
よつて乾き度が異なる。このため、上述のごと
く、過熱蒸気の温度を検出して、一定の温度とな
るように冷却水の噴射量を制御する場合、使用す
る蒸気の流量が安定していなければ減温後の過熱
度を0にすることは困難になる。一般に、過熱蒸
気を用いた系においては、蒸気の流量が刻々変化
しているため、減温後の過熱度を0にするため
に、若千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] By the way, saturated steam has the following problems as shown in FIG.
Even if the temperature is constant, the degree of dryness varies depending on the amount of enthalpy. Therefore, as mentioned above, when detecting the temperature of superheated steam and controlling the injection amount of cooling water to maintain a constant temperature, if the flow rate of the steam used is not stable, the degree of superheating after temperature reduction will increase. It becomes difficult to reduce to 0. Generally, in a system using superheated steam, the flow rate of the steam changes from moment to moment, so in order to reduce the degree of superheat to 0 after cooling, the superheated steam is heated to a slightly higher degree of superheat. I was adjusting.

しかしながら、こ調整は困難であり、物体を加
熱用の蒸気として使用するには不適切であつた。
However, this adjustment was difficult and the object was unsuitable for use as heating steam.

それゆえ、この発明に主たる目的は、減温後の
蒸気が乾き飽和蒸気となるように、過熱蒸気、冷
却水のそれぞれのエンタルピから過熱蒸気流量に
見合う冷却水を噴射し、加熱用蒸気として適切な
ものに加工し得る蒸気減温器の冷却水噴射量制御
装置を提供することである。
Therefore, the main purpose of this invention is to inject cooling water that matches the flow rate of superheated steam from the respective enthalpies of superheated steam and cooling water, so that the steam after temperature reduction becomes dry and saturated steam, and is suitable for use as heating steam. An object of the present invention is to provide a cooling water injection amount control device for a steam desuperheater that can be processed into a steam desuperheater.

[問題点を解決するための手段] この発明にかかる蒸気減温器の冷却水噴射量制
御装置は、過熱蒸気の温度を検出するための温度
検出手段と、過熱蒸気の流量を検出するための蒸
気流量検出手段と、検出された温度と流量とに基
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する演算制御手段と、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から構成される。
[Means for Solving the Problems] A cooling water injection amount control device for a steam desuperheater according to the present invention includes a temperature detection means for detecting the temperature of superheated steam, and a temperature detection means for detecting the flow rate of superheated steam. a steam flow rate detection means; a calculation control means for calculating an injection amount of cooling water to produce a preset dry saturated steam based on the detected temperature and flow rate; It consists of cooling water injection means that injects water into superheated steam.

[作用] この発明にかかる蒸気減温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、その演算結果に基づいて
冷却水の噴射量を制御するようにしたもので、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
工することができる。
[Operation] The cooling water injection amount control device for a steam desuperheater according to the present invention calculates the injection amount of cooling water to make dry saturated steam to a preset value based on the temperature of superheated steam and the steam flow rate. The amount of cooling water injected is then controlled based on the calculation results, making it possible to process superheated steam into dry saturated steam that is suitable as heating steam even in systems where the steam flow rate fluctuates widely. I can do it.

[発明の実施例] 第1図はこの発明で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
設定器の具体的なブロツク図である。
[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 concrete block diagram of the cooling water flow rate setting device shown in FIG. 1.

まず、第1図および第2図に参照して、この発
明の一実施例の構成について説明する。第1図に
おいて、過熱蒸気配管1と圧力検出器2と蒸気圧
力調節器3と圧力調節弁4は前述の第3図に示し
たものと同じものが用いられる。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
の温度を検出する温度検出器5とが設けられる。
蒸気流量検出器8によつて検出された流量と温度
検出器5によつ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
された流量および温度を予め設定された情報と任
意の関数に基づいて、蒸気流量に対応する冷却水
の流量を演算し、冷却水流量調節器11の流量を
調節する。冷却水流量調節器11は冷却水の流量
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
た流量が冷却水流量設定器9で演算された流量と
なるように、冷却水噴射装置7を制御する。それ
によつて、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。
First, the configuration of an embodiment of the present invention will be described with reference to FIGS. 1 and 2. FIG. In FIG. 1, the same superheated steam piping 1, pressure detector 2, steam pressure regulator 3, and pressure regulating valve 4 as shown in FIG. 3 are used. Further, the superheated steam pipe 1 is provided with a steam flow rate detector 8 that detects the flow rate of superheated steam in the superheated steam pipe 1, and a temperature detector 5 that detects the temperature of the superheated steam.
The 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. The cooling water flow rate setting device 9 calculates the cooling water flow rate corresponding to the steam flow rate based on the input flow rate and temperature, preset information and an arbitrary function, and adjusts the flow rate of the cooling water flow rate regulator 11. do. The cooling water flow rate regulator 11 is provided with a detection output from a water flow rate detector 10 that detects the flow rate of cooling water, and the flow rate detected by the water flow rate detector 10 is calculated by the cooling water flow rate setting device 9. The cooling water injection device 7 is controlled so that the flow rate becomes the same. 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、冷却水流量設定器9について詳細に説明
する。冷却水流量設定器9は第2図に示すよう
に、入力バツフア91と定数設定器92とマルチ
プレクサ93とA/D変換器94と制御部95と
出力回路96と表示器97とから構成される。入
力バツフア91には、上述の第1図に示した蒸気
流量検出器8で検出された蒸気流量と、温度検出
器5で検出された蒸気温度とが与えられる。な
お、この入力バツフア91には、圧力検出器2に
よつて検出された蒸気圧力を入力するとともに、
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
乾き飽和蒸気のエンタルピと、冷却水量の上限値
および下限値を設定するものである。入力バツフ
ア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。マルチプレクサ93は入力バツフア91から
与えられた各情報および定数設定器92で設定さ
れた設定値を順次選択してA/D変換器94に与
える。A/D変換器94はそれらの情報をデイジ
タル信号に変換し、制御部95に与える。
Next, the cooling water flow rate setting device 9 will be explained in detail. As shown in FIG. 2, the cooling water flow rate setting device 9 is composed of an input buffer 91, a constant setting device 92, a multiplexer 93, an A/D converter 94, a control section 95, an output circuit 96, and a display 97. . The input buffer 91 is supplied with the steam flow rate detected by the steam flow rate detector 8 shown in FIG. 1 described above and the steam temperature detected by the temperature detector 5. Note that the steam pressure detected by the pressure detector 2 is input to this input buffer 91, and
Alternatively, 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 enthalpy of dry saturated steam to be obtained and the upper and lower limits 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. The multiplexer 93 sequentially selects each piece of information given from the input buffer 91 and the set value set by the constant setter 92 and supplies them to the A/D converter 94 . A/D converter 94 converts the information into digital signals and provides them to control section 95.

制御部95は入力された情報に基づいて、補正
蒸気流量お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Tとし、差圧を
Δpとし、注水温度をTw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は次式によつて求められる。
The control unit 95 calculates the corrected steam flow rate and cooling water amount based on the input information. In other words, the steam pressure is P, the steam temperature is T, the differential pressure is Δp, the water injection temperature is Tw, and the corrected steam flow rate is
If Fs is the amount of cooling water and Fw is the amount of cooling water, then the corrected steam flow rate is
Fs is determined by the following formula.

ただし、K1〜K4は定数 また、冷却推量Fwは次式によつて求められる。 However, K1 to K4 are constants. Also, the estimated cooling amount Fw is obtained by the following formula.

Fw=K5・T−K6・P−K7・P1+K8/K9・P1−K10・Tw+K
11 ・Fs/K12−K13・Tw ただし、K5〜K13、P1は定数 上述のごとくして制御部95によつて演算され
た補正蒸気流量および冷却水量に基づいて、出力
回路96は冷却水流量調節器11に冷却水量を設
定する。冷却水流量調節器11は冷却水流量設定
器9によつて設定された冷却水量に基づいて、冷
却水噴射装置7を制御する。それによつて、過熱
蒸気配管1の出力側から乾き飽和蒸気が得られ
る。
Fw=K5・T−K6・P−K7・P1+K8/K9・P1−K10・Tw+K
11 ・Fs/K12−K13・Tw However, K5 to K13 and P1 are constants Based on the corrected steam flow rate and cooling water amount calculated by the control unit 95 as described above, the output circuit 96 adjusts the cooling water flow rate. Set the amount of cooling water in the container 11. The cooling water flow rate regulator 11 controls the cooling water injection device 7 based on the amount of cooling water set by the cooling water flow rate setting device 9. Thereby, dry saturated steam is obtained from the output side of the superheated steam pipe 1.

[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もので、蒸
気流量の変動が大きいプロセスにおいても過熱蒸
気を加熱用蒸気として適した状態の乾き飽和蒸気
に加工することができる。したがつて、過熱蒸気
を用いた場合の加熱装置における加熱表面鈍度の
付近一性や大きな熱応力の発生というような問題
点を解決することができる。
[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 The cooling water flow rate is adjusted using the setting value of the cooling water flow rate controller, and even in processes where the steam flow rate fluctuates greatly, superheated steam can be processed into dry saturated steam suitable as heating steam. I can do it. Therefore, it is possible to solve problems such as near-uniformity of heating surface dullness and generation of large thermal stress in a heating device using superheated steam.

【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ツク図である。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
系を示す概要図である。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 showing 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, 7 is a cooling water injection device, 8 is a steam flow rate detector, and 9 is a steam flow rate detector. A cooling water flow rate setting device, 10 a water flow rate detector, and 11 a cooling water flow rate regulator.

Claims (1)

【特許請求の範囲】 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つて、 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つて検出された温度と前
記蒸気流量検出手段によつ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つ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。 2 さらに、前記過熱蒸気の圧力を検出する蒸気
圧力検出手段を含み、 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、前記冷却水の噴射量を演算するよ
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。 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
つ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。
[Scope of Claims] 1. A cooling water injection amount control device for a steam desuperheater for controlling the injection amount of cooling water in order to convert superheated steam into dry saturated steam, the device comprising: detecting the temperature of the superheated steam; temperature detection means for detecting the flow rate of the superheated steam, steam flow rate detection means for detecting the flow rate of the superheated steam, based on the temperature detected by the temperature detection means and the flow rate detected by the steam flow rate detection means. , an arithmetic control means for calculating an injection amount of the cooling water in order to produce a preset dry saturated steam; and an arithmetic control means for injecting cooling water into the superheated steam based on the injection amount calculated by the arithmetic and control means. A cooling water injection amount control device for a steam desuperheater, which is equipped with a cooling water injection means. 2 further includes steam pressure detection means for detecting the pressure of the superheated steam, and the arithmetic control means is configured to detect the cooling temperature based on the pressure detected by the steam pressure detection means and the detected temperature and flow rate. A cooling water injection amount control device for a steam attemperator according to claim 1, which calculates an injection amount of water. 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 controls the overheating 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 JPS62141407A (en) 1987-06-24
JPH0555762B2 true 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)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2873640B2 (en) * 1991-11-15 1999-03-24 株式会社テイエルブイ Steam quality control equipment
JPH0694211A (en) * 1992-09-14 1994-04-05 Tlv Co Ltd Steam pressure reducing and temperature reducing apparatus
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
JPS62141407A (en) 1987-06-24

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