JPS5929765B2 - Heat exchanger temperature control method and device - Google Patents

Heat exchanger temperature control method and device

Info

Publication number
JPS5929765B2
JPS5929765B2 JP14220076A JP14220076A JPS5929765B2 JP S5929765 B2 JPS5929765 B2 JP S5929765B2 JP 14220076 A JP14220076 A JP 14220076A JP 14220076 A JP14220076 A JP 14220076A JP S5929765 B2 JPS5929765 B2 JP S5929765B2
Authority
JP
Japan
Prior art keywords
heat exchanger
fluid
temperature
temperature control
heat transfer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP14220076A
Other languages
Japanese (ja)
Other versions
JPS5367002A (en
Inventor
和彦 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP14220076A priority Critical patent/JPS5929765B2/en
Publication of JPS5367002A publication Critical patent/JPS5367002A/en
Publication of JPS5929765B2 publication Critical patent/JPS5929765B2/en
Expired legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 この発明は熱交換器の温度制御方法とその装置の構造に
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a temperature control method for a heat exchanger and a structure of the device.

一般に熱交換器においては、定格時における有効な伝熱
をする伝熱面積と排出される受熱流体の熱交換器出口温
度等を設定し熱交換管の面積を設計している。
Generally, in a heat exchanger, the area of the heat exchange tube is designed by setting the heat transfer area for effective heat transfer at the rated time, the heat exchanger outlet temperature of the heat receiving fluid to be discharged, etc.

しかし実際の運転状態においてはその運転状態のバラン
ス等から予定する流体出口条件例えば蒸気温度が得られ
ず、有効伝熱面積を調整するために熱交換管にバッフル
プレートラ設ケたり、熱交換器の伝熱管の一部を切断し
たり増加させたり等する対策手段が講ぜられている。
However, in actual operating conditions, due to the balance of operating conditions, the expected fluid outlet conditions, such as steam temperature, cannot be obtained, and in order to adjust the effective heat transfer area, baffle plates are installed on the heat exchange tubes, and heat exchangers are installed. Countermeasures have been taken, such as cutting off or increasing the number of heat exchanger tubes.

しかしこれKは作業の時間もかかるしまた費用もかがり
望ましい手段ではない。
However, this is not a desirable method as it takes time and costs.

この発明は流体を熱交換器前に噴出させ流体膜を形成し
熱交換器の有効伝熱面積を変更し熱交換器を通す流体例
えば蒸気等の熱交換器出口における温度を制御する方法
とその装置の提案をすることを目的とする。
This invention relates to a method of ejecting fluid in front of a heat exchanger to form a fluid film, changing the effective heat transfer area of the heat exchanger, and controlling the temperature of a fluid such as steam passing through the heat exchanger at the outlet of the heat exchanger. The purpose is to propose equipment.

この発明の一実施例を以下図面により説明する。An embodiment of this invention will be described below with reference to the drawings.

第1図は蒸気発生装置にこの発明にかかる装置を設けた
場合の構造を示すものである。
FIG. 1 shows the structure of a steam generator equipped with a device according to the present invention.

火炉1で燃焼した燃焼ガスは二次過熱器2、再熱器3、
一次過熱器4、節炭器5、で熱交換し、空気予熱器(図
示せず)を通り排出される。
The combustion gas burned in the furnace 1 is transferred to a secondary superheater 2, a reheater 3,
It exchanges heat with the primary superheater 4 and the economizer 5, and is discharged through an air preheater (not shown).

また窒素酸化物(NOx)の発生防止、火炉温度制御の
目的から燃焼ガスの一部は再循環ガスとして再循環ファ
ン6により導管1経由火炉に供給されるものである。
Further, for the purpose of preventing the generation of nitrogen oxides (NOx) and controlling the furnace temperature, a part of the combustion gas is supplied to the furnace via the conduit 1 by the recirculation fan 6 as recirculation gas.

このような蒸気発生装置につきこの発明を実施するため
に導管7より管路8を分岐して設け、二次過熱器2と再
熱器3の間でかつ高温ガス通路9の底板部に位置したガ
ス注入装置10と導管8とを接続するものである。
In order to implement the present invention in such a steam generator, a pipe line 8 is branched from the pipe line 7 and is located between the secondary superheater 2 and the reheater 3 and at the bottom plate of the high-temperature gas passage 9. It connects the gas injection device 10 and the conduit 8.

この場合にわいて管路8には調整ダンパ11、要すれば
昇圧用のブーストファン12を設は注入装置10に供給
するガス量とそのガス圧力の制御を行なうものである。
In this case, an adjustment damper 11 and, if necessary, a boost fan 12 for boosting the pressure are provided in the conduit 8 to control the amount of gas supplied to the injection device 10 and the gas pressure.

管路8より供給される再循環ガスは開口の絞られたノズ
ル13を有する注入装置10から噴出し第2図に示すよ
うに流体膜を形成するので、再熱器3については斜線で
囲む範囲が無効伝熱面積Bとなり再熱器3の出口蒸気温
度は低下することとなる。
The recirculating gas supplied from the pipe line 8 is ejected from the injection device 10 having a nozzle 13 with a constricted opening and forms a fluid film as shown in FIG. becomes the ineffective heat transfer area B, and the outlet steam temperature of the reheater 3 will decrease.

また前記の面積Bをブーストファン12によるガス圧の
昇圧と調整ダンパ11との作動により変化させることが
できる。
Further, the above-mentioned area B can be changed by increasing the gas pressure by the boost fan 12 and by operating the adjustment damper 11.

以上蒸気発生装置を一例としてとりあげ説明したもので
、この場合熱交換をする流体は蒸気と燃焼ガスであるが
、この発明はガス体にのみ限定するものではなく、液体
と液体、液体と気体との間における熱交換装置について
も適用されうろことはいうまでもない。
The above explanation has been given by taking a steam generator as an example, and in this case, the fluids that exchange heat are steam and combustion gas, but the present invention is not limited to only gas bodies, but can also be applied to liquids, liquids, and gases. Needless to say, this also applies to the heat exchanger between the two.

また噴出流体もこの例におけるごとく排ガスを使用して
いるが別に冷空気であってもよい。
Although exhaust gas is used as the ejected fluid in this example, it may also be cold air.

また噴出気体に代り液体として加熱された圧力水例えば
ボイラ水またはブロー水等を噴出させ気化させ、または
再循環ガスと共に噴出させてもよい。
Further, instead of the ejected gas, heated liquid pressure water such as boiler water or blow water may be ejected and vaporized, or may be ejected together with the recirculated gas.

更に噴出流体は熱交換管内を流れる流体より常に低温で
ある必要はなく、ノズル口で燃焼する高温のガスであっ
てもよい。
Further, the ejected fluid does not always have to be lower than the fluid flowing in the heat exchange tube, and may be a high temperature gas combusted at the nozzle opening.

また管内を流れる流体は熱交換され冷却されるような場
合であってもよい。
Further, the fluid flowing inside the pipe may be cooled by heat exchange.

この発明は以下の特徴を有する。This invention has the following features.

(1)熱交換器の温度を制御するものにおいて、熱交換
器の与熱流体流入側前面に流体膜を形成し熱交換器の与
熱流体による有効対流伝熱面積を変更匍濁する熱交換器
の温度制御方法であること。
(1) In a device that controls the temperature of a heat exchanger, a fluid film is formed on the front surface of the heating fluid inflow side of the heat exchanger to change the effective convection heat transfer area by the heating fluid of the heat exchanger. The temperature control method of the device.

(2)熱交換器の与熱流体流入側前面に形成する流体膜
の流体を排ガス管路より採取する再循環排ガスとする熱
交換器の温度制御方法であること。
(2) A temperature control method for a heat exchanger in which the fluid of the fluid film formed on the front surface of the heating fluid inflow side of the heat exchanger is collected from the exhaust gas pipe and used as recirculated exhaust gas.

(3)熱交換器の与熱流体流入側前面に形成する流体膜
の流体を空気とする熱交換器の温度制御方法であること
(3) The heat exchanger temperature control method uses air as the fluid of the fluid film formed on the front surface of the heating fluid inflow side of the heat exchanger.

(4)熱交換器の与熱流体流入側前面に形成する流体膜
の流体を液体とする熱交換器の温度制御方法であること
(4) A temperature control method for a heat exchanger in which the fluid in the fluid film formed on the front surface of the heating fluid inflow side of the heat exchanger is a liquid.

(5)蒸気発生装置において、過熱器と再熱器の間に前
記蒸気発生装置の排ガスより温度の低い気体を噴出させ
気体膜を形成し再熱器の有効対流伝熱面積を変更して蒸
気温度を制御する熱交換器の温度制御装置であること。
(5) In a steam generator, a gas having a temperature lower than the exhaust gas of the steam generator is ejected between a superheater and a reheater to form a gas film, and the effective convection heat transfer area of the reheater is changed to generate steam. It must be a temperature control device for a heat exchanger that controls temperature.

この発明を実施することにより、バッフルプレートの設
置や熱交換管の増設又は切断等の改造作業を不用とし、
有効対流伝熱面積を変更制御することができ、再循環ガ
スを使用するときは蒸気発生装置全体としての熱吸収を
そこなうことなく過熱器、再熱器等の熱吸収の割合を変
えることができる等種々の効果を奏するものである。
By implementing this invention, modification work such as installing baffle plates, adding or cutting heat exchange tubes, etc. is unnecessary,
The effective convection heat transfer area can be changed and controlled, and when using recirculated gas, the heat absorption rate of the superheater, reheater, etc. can be changed without impairing the heat absorption of the steam generator as a whole. It has various effects such as.

【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にかかる蒸気発生装置の縦
断面図、第2図は第1図のA部詳細を示す図面である。 1・・・・・・火炉、2・・・・・・2次過熱器、3・
・・・・・再熱器、6・・・・・・再循環ファン、7・
・・・・・導管、8・・・・・・管路、9・・・・・・
高温ガス通路、10・・・・・・注入装置、11・・・
・・・調整ダンパ、12・・・・・・ブーストファン、
13・・・・・・ノズル、14・・・・・・流体膜、B
・・・・・・無効伝熱面積。
FIG. 1 is a longitudinal sectional view of a steam generator according to an embodiment of the present invention, and FIG. 2 is a drawing showing details of section A in FIG. 1. 1...Furnace, 2...Secondary superheater, 3.
... Reheater, 6 ... Recirculation fan, 7.
... Conduit, 8 ... Conduit, 9 ...
High temperature gas passage, 10... Injection device, 11...
... Adjustment damper, 12 ... Boost fan,
13...Nozzle, 14...Fluid film, B
...Ineffective heat transfer area.

Claims (1)

【特許請求の範囲】 1 熱交換器の温度を与熱流体の流れかたにより制御す
る方法において、熱交換器の与熱流体流入側前面に流体
膜を形成し熱交換器の与熱流体との有効対流伝熱面積を
変更制御することを特徴とする熱交換器の温度制御方法
。 2 熱交換器の対流伝熱をする管群の与熱流体流入側前
面に形成する流体膜の流体を排ガス管路より採取する再
循環排ガスとすることを特徴とする特許請求の範囲第1
項記載の熱交換器の温度制御方法。 3 熱交換器の対流伝熱をする管群の与熱流体流入側前
面に形成する流体膜の流体を空気とすることを特徴とす
る特許請求の範囲第1項記載の熱交換器の温度制御方法
。 4 熱交換器の対流伝熱をする管群の与熱流体流入側前
面に形成する流体膜の流体を液体とすることを特徴とす
る特許請求の範囲第1項記載の熱交換器の温度制御方法
。 5 蒸気発生装置において、過熱器と再熱器の間にそこ
を通過する前記蒸気発生装置の排ガスより温度の低い流
体を噴出させ流体膜を形成し再熱器の有効対流伝熱面積
を変更して蒸気温度を制御する装置を設けたことを特徴
とする熱交換器の温度制御装置。 6 前記排ガスより温度の低い流体を噴出する注入装置
10と導管7とを接続する管路8にブーストファン12
と調整ダンパ11を設けたことを特徴とする特許請求の
範囲第5項記載の熱交換器の温度制御装置。
[Scope of Claims] 1. A method for controlling the temperature of a heat exchanger by the flow of a heating fluid, in which a fluid film is formed on the front surface of the heating fluid inflow side of the heat exchanger, and the temperature of the heating fluid of the heat exchanger is controlled. A method for controlling the temperature of a heat exchanger, characterized in that the effective convective heat transfer area of the heat exchanger is changed and controlled. 2. Claim 1, characterized in that the fluid of the fluid film formed on the front surface of the heating fluid inflow side of the tube group for convective heat transfer of the heat exchanger is used as recirculated exhaust gas collected from the exhaust gas pipe.
A method for controlling the temperature of a heat exchanger described in Section 1. 3. Temperature control of a heat exchanger according to claim 1, characterized in that the fluid of the fluid film formed on the front surface of the heating fluid inflow side of the tube group for convective heat transfer of the heat exchanger is air. Method. 4. Temperature control of a heat exchanger according to claim 1, characterized in that the fluid of the fluid film formed on the front surface of the heating fluid inflow side of the tube group for convective heat transfer of the heat exchanger is a liquid. Method. 5. In a steam generator, a fluid having a temperature lower than the exhaust gas of the steam generator passing through the superheater and the reheater is ejected between the superheater and the reheater to form a fluid film and change the effective convection heat transfer area of the reheater. 1. A temperature control device for a heat exchanger, comprising a device for controlling steam temperature. 6 A boost fan 12 is connected to the conduit 8 that connects the conduit 7 and the injection device 10 that spouts out a fluid having a lower temperature than the exhaust gas.
6. The temperature control device for a heat exchanger according to claim 5, further comprising: and an adjustment damper 11.
JP14220076A 1976-11-29 1976-11-29 Heat exchanger temperature control method and device Expired JPS5929765B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14220076A JPS5929765B2 (en) 1976-11-29 1976-11-29 Heat exchanger temperature control method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14220076A JPS5929765B2 (en) 1976-11-29 1976-11-29 Heat exchanger temperature control method and device

Publications (2)

Publication Number Publication Date
JPS5367002A JPS5367002A (en) 1978-06-15
JPS5929765B2 true JPS5929765B2 (en) 1984-07-23

Family

ID=15309710

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14220076A Expired JPS5929765B2 (en) 1976-11-29 1976-11-29 Heat exchanger temperature control method and device

Country Status (1)

Country Link
JP (1) JPS5929765B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0510884B2 (en) * 1987-07-02 1993-02-12 Yutaka Consultant Kk

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58124106A (en) * 1982-01-21 1983-07-23 三菱重工業株式会社 Boiler reheated steam-temperature control system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0510884B2 (en) * 1987-07-02 1993-02-12 Yutaka Consultant Kk

Also Published As

Publication number Publication date
JPS5367002A (en) 1978-06-15

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