JPH07122488B2 - Reheater steam temperature control method - Google Patents
Reheater steam temperature control methodInfo
- Publication number
- JPH07122488B2 JPH07122488B2 JP1156143A JP15614389A JPH07122488B2 JP H07122488 B2 JPH07122488 B2 JP H07122488B2 JP 1156143 A JP1156143 A JP 1156143A JP 15614389 A JP15614389 A JP 15614389A JP H07122488 B2 JPH07122488 B2 JP H07122488B2
- Authority
- JP
- Japan
- Prior art keywords
- reheater
- furnace
- opening
- signal
- heat collection
- 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
Links
- 238000000034 method Methods 0.000 title claims description 12
- 239000007789 gas Substances 0.000 description 25
- 239000003245 coal Substances 0.000 description 14
- 238000005192 partition Methods 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000004043 responsiveness Effects 0.000 description 3
- 239000000567 combustion gas Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は再熱器の蒸気温度制御方法に関するものであ
る。The present invention relates to a steam temperature control method for a reheater.
[従来の技術] 第1図は石炭焚ボイラの一例を示すもので、火炉1の微
粉炭バーナ2により燃焼を行った高温の燃焼ガスは、火
炉1の炉壁部3及び火炉1内上部の分割壁4等を加熱し
た後、後部伝熱部5に導かれるようになっている。後部
伝熱部5は、仕切壁6により再熱器7を有した再熱器側
流路8と過熱器9を有した過熱器側流路10とに分割され
ており、且つ各流路8,10の下部には両流路8,10の特に再
熱器側流路8を流れる燃焼ガスの流量の制御を行う再熱
器ガスダンパ11が備えられている。[Prior Art] FIG. 1 shows an example of a coal-fired boiler. High-temperature combustion gas burned by a pulverized coal burner 2 of a furnace 1 is generated in a furnace wall portion 3 of the furnace 1 and an upper part of the inside of the furnace 1. After heating the partition wall 4 and the like, the partition wall 4 and the like are guided to the rear heat transfer section 5. The rear heat transfer section 5 is divided by a partition wall 6 into a reheater side flow path 8 having a reheater 7 and a superheater side flow path 10 having a superheater 9, and each flow path 8 A reheater gas damper 11 for controlling the flow rate of the combustion gas flowing through the flow passages 8 and 10, particularly the reheater side flow passage 8, is provided below the and 10.
スプレイ装置等を有する過熱器9に比し、タービン駆動
後の蒸気を再加熱する再熱器7は、蒸気温度を制御する
ための手段を殆んど有しておらず、このために再熱器7
出口の蒸気温度を検出する再熱器出口温度検出器12の検
出温度が一定に保たれるように再熱器側流路8に流れる
ガス量をダンパ駆動部13を介して再熱器ガスダンパ11に
より制御し、残りのガスを過熱器9側に流すようにして
いる。Compared to the superheater 9 having a spray device or the like, the reheater 7 for reheating the steam after driving the turbine has almost no means for controlling the steam temperature, and therefore, the reheat is performed. Bowl 7
The amount of gas flowing through the reheater-side flow path 8 is controlled by the reheater gas damper 11 via the damper drive unit 13 so that the temperature detected by the reheater outlet temperature detector 12 for detecting the outlet steam temperature is kept constant. The remaining gas is made to flow to the superheater 9 side.
従来の前記再熱器ガスダンパ11の開度制御は、第3図に
示す如く負荷指令等に対するプログラムによって制御し
ており、又再熱器ガスダンパ11は再熱器7側と過熱器9
側の開閉が逆作動となるようにしてある。The conventional opening control of the reheater gas damper 11 is controlled by a program for a load command or the like as shown in FIG. 3, and the reheater gas damper 11 includes a reheater 7 side and a superheater 9
The opening and closing of the side is designed to be the reverse operation.
[発明が解決しようとする課題] しかし、前記したような石炭焚ボイラの燃料となる原炭
は、その性状が産地等によって大きく異なり、又同一炭
種でも湿分等の影響により、火炉1内での収熱状況に大
きな差異を生じる。[Problems to be Solved by the Invention] However, the properties of the raw coal, which serves as a fuel for the coal-fired boiler as described above, differ greatly depending on the place of origin, etc., and even within the same coal type due to the influence of moisture etc. It makes a big difference in the heat collection situation.
このため、前記したように再熱器ガスダンパ11の開度制
御を単に負荷指令に対するプログラムとした方式では、
炭種が性状の異なるものに変化した場合、火炉1内燃焼
状態等によるボイラ各部の収熱状況が変化して再熱器ガ
スダンパ11の最適開度も変化することになるため、設定
値とずれを生じることになり、よって即応性の高い再熱
器蒸気温度制御が実現できない問題を生じていた。Therefore, as described above, in the method in which the opening degree control of the reheater gas damper 11 is simply a program for the load command,
When the type of coal changes to one with different properties, the heat collection status of each part of the boiler changes due to the combustion state in the furnace 1, etc., and the optimum opening of the reheater gas damper 11 also changes. Therefore, there is a problem that reheater steam temperature control with high responsiveness cannot be realized.
本発明は、火炉部伝熱面等のボイラ各部の収熱状況から
炭種に応じた再熱器ガスダンパの最適開度を推定し、そ
の推定開度信号により基本開度設定信号を修正して再熱
器ガスダンパの開度を調整することにより、即応性の高
い再熱器蒸気温度制御を実現することを目的としてい
る。The present invention estimates the optimum opening degree of the reheater gas damper according to the coal type from the heat collection state of each part of the boiler such as the heat transfer surface of the furnace part, and corrects the basic opening setting signal by the estimated opening signal. By adjusting the opening of the reheater gas damper, the objective is to realize highly responsive reheater steam temperature control.
[課題を解決するための手段] 本発明は負荷指令に基づく基本開度設定信号とフィード
バック制御信号とにより再熱器ガスダンパの開度を調整
して再熱器蒸気温度を制御する方法において、ボイラ炉
壁部の入口と出口の温度及び圧力と、分割壁の入口と出
口の温度及び圧力とを少なくとも検出して火炉部収熱演
算回路に入力することにより比炉部の収熱を検出し、そ
の火炉部収熱信号を開度演算回路に導くことにより前記
火炉部収熱信号に応じた再熱器ガスダンパの最適開度を
推定し、その推定開度信号により前記基本開度設定信号
を修正し、修正した修正開度信号とフィードバック制御
信号とにより再熱器ガスダンパの開度を調整して再熱器
の蒸気温度を制御することを特徴とする再熱器の蒸気温
度制御方法にかかるものである。[Means for Solving the Problem] The present invention provides a method for controlling the reheater steam temperature by adjusting the opening of a reheater gas damper by a basic opening setting signal and a feedback control signal based on a load command. The temperature and pressure of the inlet and outlet of the furnace wall portion, the temperature and pressure of the inlet and outlet of the dividing wall at least detected and input to the furnace heat collection heat calculation circuit to detect the heat collection of the specific furnace portion, The optimum opening of the reheater gas damper corresponding to the furnace heat collection signal is estimated by introducing the furnace heat collection signal to the opening calculation circuit, and the basic opening setting signal is corrected by the estimated opening signal. A method for controlling the steam temperature of the reheater, characterized in that the steam temperature of the reheater is controlled by adjusting the opening of the reheater gas damper by the modified corrected opening signal and the feedback control signal. Is.
[作用] 火炉内の燃焼状態等により、ボイラ各部、特に火炉部の
収熱が変化すると、それに応じた再熱器ガスダンパの最
適開度が推定され、その推定開度信号により基本開度設
定信号が修正されるので、原炭性状の変化に応じて再熱
器ガスダンパの開度が修正される。[Operation] When the heat collection of each part of the boiler, especially the furnace part, changes due to the combustion state in the furnace, the optimal opening of the reheater gas damper is estimated accordingly, and the estimated opening signal is used to set the basic opening setting signal. Is corrected, the opening degree of the reheater gas damper is corrected according to the change in raw coal properties.
[実 施 例] 以下、本発明の実施例を図面を参照しつつ説明する。[Examples] Examples of the present invention will be described below with reference to the drawings.
前記第1図のボイラにおける火炉1の炉壁部3の入口
(上流側)と出口(下流側)の夫々の温度と圧力を検出
する検出器14,15、及び分割壁4の入口と出口の温度と
圧力を検出する検出器16,17を設けて、各検出器14,15,1
6,17の検出温度と圧力から火炉1部の収熱状況を把握で
きるようにする。このとき、他の吊り下げ伝熱面18等の
収熱も火炉1部として考慮する場合には、その入口と出
口の温度と圧力も検出する。図中12は再熱器7出口の蒸
気温度を検出する再熱器出口温度検出部、13はダンパ駆
動部である。Detectors 14 and 15 for detecting the temperature and pressure of the inlet (upstream side) and the outlet (downstream side) of the furnace wall portion 3 of the furnace 1 in the boiler of FIG. The detectors 16 and 17 for detecting temperature and pressure are provided so that the detectors 14, 15 and 1
The heat collection status of the furnace part 1 can be grasped from the detected temperature and pressure of 6,17. At this time, when the heat collection of the other suspended heat transfer surface 18 and the like is also considered as the part of the furnace 1, the temperature and pressure of its inlet and outlet are also detected. In the figure, 12 is a reheater outlet temperature detection unit that detects the steam temperature at the reheater 7 outlet, and 13 is a damper drive unit.
第2図において、負荷指令19を関数発生器20により関数
変換して再熱器ガスダンパの基本開度設定信号21を得、
該基本開度設定信号21によりダンパ駆動部13の制御を行
うようにし、且つ前記温度検出器12による再熱器7出口
の検出蒸気温度信号と蒸気温度設定器からの設定温度信
号22とを引算器23によって引算し、その差信号24をPIコ
ントローラ25に導き、そのフィードバック制御信号33を
加算器26に導き、前記基本開度設定信号21に加算してダ
ンパ駆動部13の調整を行うようにしている。In FIG. 2, the load command 19 is function-converted by the function generator 20 to obtain the basic opening setting signal 21 of the reheater gas damper,
The basic drive setting signal 21 is used to control the damper drive unit 13, and the temperature detector 12 subtracts the detected steam temperature signal at the outlet of the reheater 7 and the set temperature signal 22 from the steam temperature setter. The difference signal 24 is subtracted by the calculator 23, the difference signal 24 is guided to the PI controller 25, the feedback control signal 33 is guided to the adder 26, which is added to the basic opening setting signal 21 to adjust the damper drive unit 13. I am trying.
上記制御回路は従来から実施されているものであるが、
この方式では、炭種の変化による火炉収熱の変化によっ
て再熱器ガスダンパの最適開度が変化した場合、基本開
度設定信号21とのずれ分をすべてPIコントローラ25によ
る調整によってカバーすることになるため、即応性の点
で問題がある。Although the control circuit has been conventionally implemented,
In this method, if the optimum opening of the reheater gas damper changes due to a change in furnace heat collection due to a change in coal type, all deviations from the basic opening setting signal 21 are covered by adjustment by the PI controller 25. Therefore, there is a problem in terms of responsiveness.
このため、前記検出器14,15,16,17によるボイラ各部の
検出部35からの各検出温度、圧力を火炉部収熱演算回路
27に入力して炉壁部3及び分割壁4等の火炉部収熱を演
算し、その火炉部収熱信号28を開度演算回路29に導いて
再熱器ガスダンパの最適開度を推定し、その推定開度信
号30を関数発生器31を介して修正演算回路32に導き、前
記負荷指令19に基づく基本開度設定信号21の修正を行う
ようにする。34は修正開度信号を示す。Therefore, the temperature and pressure detected by the detectors 14, 15, 16 and 17 from the detector 35 of each part of the boiler are calculated by the furnace heat collection heat calculation circuit.
It inputs to 27 to calculate the furnace part heat collection of the furnace wall part 3 and the dividing wall 4 etc., and guides the furnace part heat collection signal 28 to the opening calculation circuit 29 to estimate the optimum opening of the reheater gas damper. The estimated opening degree signal 30 is led to the correction calculation circuit 32 via the function generator 31, and the basic opening degree setting signal 21 is corrected based on the load command 19. Reference numeral 34 represents a corrected opening signal.
上記において、燃料炭種の変更などによって原炭の性状
が変わると、炉壁部3の入口と出口の温度と圧力、及び
分割壁4の入口と出口の温度と圧力を検出している検出
器14,15,16,17の信号が変化し、その信号が火炉部収熱
演算回路27に導かれて火炉部収熱が演算されているの
で、火炉部収熱信号28の変化として把握される。In the above, a detector that detects the temperature and pressure at the inlet and outlet of the furnace wall 3 and the temperature and pressure at the inlet and outlet of the dividing wall 4 when the properties of the raw coal change due to changes in the fuel coal type and the like. The signals of 14, 15, 16 and 17 change, and the signals are guided to the furnace part heat collection calculation circuit 27 to calculate the furnace part heat collection, so it is understood as a change in the furnace part heat collection signal 28. .
開度演算回路29は前記火炉部収熱信号28に応じた最適の
再熱器ガスダンパ開度を推定してその信号30を出力する
ようにしているので、火炉部収熱信号28が変化するとそ
れに応じて推定開度信号30も変化し、修正演算回路32に
おいて基本開度設定信号21を修正する修正量が変化す
る。The opening degree calculation circuit 29 estimates the optimum reheater gas damper opening degree according to the furnace part heat collection signal 28 and outputs the signal 30, so that when the furnace part heat collection signal 28 changes, Accordingly, the estimated opening degree signal 30 also changes, and the correction amount for correcting the basic opening degree setting signal 21 in the correction calculation circuit 32 changes.
従って、負荷指令19に基づく基本開度設定信号21が原炭
性状によって修正され、その修正された修正開度信号34
とフィードバック制御信号33とが加算器26にて加算され
た信号により、ダンパ駆動部13が作動されて再熱器ガス
ダンパの開度が調整されることになるので、PIコントロ
ーラ25による制御が減少し、よって即応性の高い再熱器
蒸気温度制御が実現される。Therefore, the basic opening setting signal 21 based on the load command 19 is modified by the raw coal property, and the modified modified opening signal 34
The feedback control signal 33 and the feedback control signal 33 are added by the adder 26 to operate the damper drive unit 13 to adjust the opening degree of the reheater gas damper, which reduces the control by the PI controller 25. Therefore, highly responsive reheater steam temperature control is realized.
上記実施例においては、原炭の性状変化による火炉内燃
焼状態の変化の影響が最も出易い火炉部の収熱を検出す
る場合について説明したが、火炉部以外の収熱も検出し
て考慮するようにしても良い。In the above embodiment, the case of detecting the heat collection of the furnace part where the influence of the change of the combustion state in the furnace due to the change of the property of the raw coal is most likely has been described, but the heat collection of the parts other than the furnace part is also detected and considered. You may do it.
尚、本発明の再熱器の蒸気温度制御方法は、上述の実施
例にのみ限定されるものではなく、本発明の要旨を逸脱
しない範囲内において種々変更を加え得ることは勿論で
ある。The steam temperature control method for the reheater according to the present invention is not limited to the above-described embodiment, and it goes without saying that various modifications can be made without departing from the scope of the present invention.
[発明の効果] 以上説明したように、本発明の再熱器の蒸気温度制御方
法によれば、石炭の性状が変った際に最も早く収熱の変
化として現われるボイラ炉壁部の入口と出口の温度と圧
力、及び分割壁の入口と出口の温度と圧力を少なくとも
検出して、その検出値が火炉部収熱演算回路に入力され
ることによりボイラ火炉部の収熱が検出され、ボイラ火
炉部の収熱に応じた再熱器ガスダンパの最適開度が推定
され、その推定開度信号により基本開度設定信号を修正
して再熱器ガスダンパの開度を調整するようにしている
ので、原炭性状の変化に応じた最適な再熱器ガスダンパ
の開度が得られ、よって即応性の高い再熱器の蒸気温度
制御が可能になる優れた効果を奏し得る。[Effects of the Invention] As described above, according to the steam temperature control method for a reheater of the present invention, the inlet and outlet of the boiler furnace wall portion, which appear as the fastest change in heat absorption when the property of coal changes. Temperature and pressure of the partition wall, and the temperature and pressure of the inlet and outlet of the dividing wall, and the detected values are input to the furnace heat collection calculation circuit to detect the heat collection of the boiler furnace part, and the boiler furnace Since the optimum opening of the reheater gas damper is estimated according to the heat collection of the part, and the opening of the reheater gas damper is adjusted by correcting the basic opening setting signal with the estimated opening signal. An optimum opening of the reheater gas damper can be obtained according to changes in the properties of the raw coal, and thus an excellent effect that the steam temperature of the reheater can be controlled with high responsiveness can be obtained.
第1図は本発明の方法を実施するボイラの一例を示す正
面図、第2図は本発明の制御ブロック図、第3図は従来
の再熱器ガスダンパ開度の制御方法を示す線図である。 1は火炉、2は微粉炭バーナ、3は炉壁部、4は分割
壁、5は後部伝熱部、7は再熱器、8は再熱器側流路、
9は過熱器、10は過熱器側流路、11は再熱器ガスダン
パ、12は再熱器出口温度検出器、13はダンパ駆動部、14
は炉壁入口温度圧力検出器、15は炉壁出口温度圧力検出
器、16は分割壁入口温度圧力検出器、17は分割壁出口温
度圧力検出器、19は負荷指令、21は基本開度設定信号、
27は火炉部収熱演算回路、28は火炉部収熱信号、29は開
度演算回路、30は推定開度信号、32は修正演算回路、33
はフィードバック制御信号、34は修正開度信号、35はボ
イラ各部の検出部を示す。FIG. 1 is a front view showing an example of a boiler for carrying out the method of the present invention, FIG. 2 is a control block diagram of the present invention, and FIG. 3 is a diagram showing a conventional reheater gas damper opening control method. is there. 1 is a furnace, 2 is a pulverized coal burner, 3 is a furnace wall part, 4 is a dividing wall, 5 is a rear heat transfer part, 7 is a reheater, 8 is a reheater side passage,
9 is a superheater, 10 is a superheater side flow path, 11 is a reheater gas damper, 12 is a reheater outlet temperature detector, 13 is a damper drive unit, 14
Is a furnace wall inlet temperature and pressure detector, 15 is a furnace wall outlet temperature and pressure detector, 16 is a dividing wall inlet temperature and pressure detector, 17 is a dividing wall outlet temperature and pressure detector, 19 is a load command, 21 is a basic opening setting signal,
27 is a furnace part heat collection calculation circuit, 28 is a furnace part heat collection signal, 29 is an opening calculation circuit, 30 is an estimated opening signal, 32 is a correction calculation circuit, 33
Is a feedback control signal, 34 is a corrected opening signal, and 35 is a detector of each part of the boiler.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 中山 信弥 東京都江東区豊洲3丁目2番16号 石川島 播磨重工業株式会社豊洲総合事務所内 (72)発明者 大石 伸也 東京都江東区豊洲3丁目2番16号 石川島 播磨重工業株式会社豊洲総合事務所内 (56)参考文献 特開 昭61−99001(JP,A) 特開 昭55−160201(JP,A) 特開 昭58−200907(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shinya Nakayama 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawajima Harima Heavy Industries Ltd. Toyosu General Office (72) Inventor Shinya Oishi 3-2, Toyosu, Koto-ku, Tokyo No. 16 Ishikawajima Harima Heavy Industries Co., Ltd. Toyosu General Office (56) Reference JP 61-99001 (JP, A) JP 55-160201 (JP, A) JP 58-200907 (JP, A)
Claims (1)
ードバック制御信号とにより再熱器ガスダンパの開度を
調整して再熱器蒸気温度を制御する方法において、ボイ
ラ炉壁部の入口と出口の温度及び圧力と、分割壁の入口
と出口の温度及び圧力とを少なくとも検出して火炉部収
熱演算回路に入力することにより火炉部の収熱を検出
し、その火炉部収熱信号を開度演算回路に導くことによ
り前記火炉収熱信号に応じた再熱器ガスダンパの最適開
度を推定し、その推定開度信号により前記基本開度設定
信号を修正し、修正した修正開度信号とフィードバック
制御信号とにより再熱器ガスダンパの開度を調整して再
熱器の蒸気温度を制御することを特徴とする再熱器の蒸
気温度制御方法。1. A method for controlling the reheater steam temperature by adjusting the opening of a reheater gas damper according to a basic opening setting signal and a feedback control signal based on a load command, the inlet and outlet of a boiler furnace wall. Temperature and pressure of the dividing wall and the temperature and pressure of the inlet and outlet of the dividing wall are input to the furnace part heat collection calculation circuit to detect the heat collection of the furnace part and open the furnace part heat collection signal. To estimate the optimum opening of the reheater gas damper according to the furnace heat collection signal by correcting the basic opening setting signal by the estimated opening signal, A steam temperature control method for a reheater, comprising: controlling a steam temperature of a reheater by adjusting an opening of a reheater gas damper with a feedback control signal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1156143A JPH07122488B2 (en) | 1989-06-19 | 1989-06-19 | Reheater steam temperature control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1156143A JPH07122488B2 (en) | 1989-06-19 | 1989-06-19 | Reheater steam temperature control method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0320502A JPH0320502A (en) | 1991-01-29 |
| JPH07122488B2 true JPH07122488B2 (en) | 1995-12-25 |
Family
ID=15621268
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1156143A Expired - Lifetime JPH07122488B2 (en) | 1989-06-19 | 1989-06-19 | Reheater steam temperature control method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07122488B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002243102A (en) * | 2001-02-21 | 2002-08-28 | Ishikawajima Harima Heavy Ind Co Ltd | Reheater gas damper opening control device using change of superheater spray flow rate |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55160201A (en) * | 1979-05-30 | 1980-12-13 | Ishikawajima Harima Heavy Ind | Steam temperature controller for boiler |
| JPS58200907A (en) * | 1982-05-18 | 1983-11-22 | 株式会社日立製作所 | Boiler reheat steam temperature control device |
| JPH0658163B2 (en) * | 1984-10-19 | 1994-08-03 | 株式会社日立製作所 | Steam temperature control device and control method for thermal power generation boiler |
-
1989
- 1989-06-19 JP JP1156143A patent/JPH07122488B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0320502A (en) | 1991-01-29 |
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