JPS5837405A - Method of controlling once-through boiler with circulator - Google Patents
Method of controlling once-through boiler with circulatorInfo
- Publication number
- JPS5837405A JPS5837405A JP13501781A JP13501781A JPS5837405A JP S5837405 A JPS5837405 A JP S5837405A JP 13501781 A JP13501781 A JP 13501781A JP 13501781 A JP13501781 A JP 13501781A JP S5837405 A JPS5837405 A JP S5837405A
- Authority
- JP
- Japan
- Prior art keywords
- amount
- load
- boiler
- water
- once
- 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
Links
Landscapes
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
- Regulation And Control Of Combustion (AREA)
- Control Of Combustion (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) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 本発明は、循環装置付貫流ボイラの制御方法に関する。[Detailed description of the invention] The present invention relates to a method for controlling a once-through boiler with a circulation device.
貫流ボイラの蒸発器に於いては、低負荷となって貫流す
る水量が少なくなると、流れの不均衡や流れの振動が生
じる。これは並列管から成る蒸発器の1本の管の流量が
少なくなると、蒸発が盛んKなる為、その管の流れの抵
抗が増え、流量が一層少−なくなるからである。この現
象は通常軸負荷以下の低負荷で生じるから、この低負荷
でボイ2を使用する時には、循環装置を設けて蒸発器を
流れる水量を偽負荷以上に相当する流量としている。循
環装置に気水分離器1分離タンク、循環ポンプなどから
成り、i負荷以下の低負荷で分離タンクに水位が出現し
て循環ポンプが稼動し、偽負荷を超える高負荷でに分離
タンクの水位が消滅して循環ポンプが停止するようにな
っている。In the evaporator of a once-through boiler, when the load is low and the amount of water flowing through decreases, flow imbalance and flow vibration occur. This is because when the flow rate in one tube of an evaporator consisting of parallel tubes decreases, evaporation becomes more active, so the flow resistance in that tube increases and the flow rate decreases even more. Since this phenomenon occurs at a low load below the normal shaft load, when the boiler 2 is used at this low load, a circulation device is provided to set the amount of water flowing through the evaporator to a flow rate corresponding to the false load or higher. The circulation system consists of a steam/water separator, a separation tank, a circulation pump, etc. At a low load below the i load, the water level appears in the separation tank and the circulation pump operates, and at a high load exceeding the false load, the water level in the separation tank rises. disappears and the circulation pump stops.
然し、前記分離タンクの水位の特性は、ボイラの負荷が
変化しない時の静的特性であって、負荷が急激に変化す
る時は分離タンクの水位が負荷に応じて出現、消滅しな
いことがある。例えば偽負荷を超える高負荷から晃負荷
以下の低負荷へ急激に変化すると、分離タンクの水位は
蒸発器の熱容量の為直ぐには現れず、従って循環ポンプ
を稼動できず、給水tは前述の理由によりi負荷相当量
より下げられない。However, the characteristics of the water level in the separation tank are static characteristics when the load on the boiler does not change, and when the load changes rapidly, the water level in the separation tank may not appear or disappear depending on the load. . For example, when a high load that exceeds the false load suddenly changes to a low load that is below the light load, the water level in the separation tank does not appear immediately due to the heat capacity of the evaporator, and therefore the circulation pump cannot be operated, and the water supply t is reduced due to the reasons mentioned above. Therefore, the load cannot be lowered below the i load equivalent amount.
然るに従来のボイラ制御方法では、給水量と燃料量を常
に一定の比率でもって供給するように制御しているので
、この場合燃料量も給水量と同じ偽負荷に相当する値と
なり、従って負荷域の要求に応じられず、この状態は分
離タンクに水位が現れ、循環ポンプが稼動し始めるまで
続くことになる。However, in conventional boiler control methods, the amount of water and fuel are always supplied at a constant ratio, so in this case, the amount of fuel also becomes a value equivalent to the same false load as the amount of water, and therefore the load range This situation will continue until the water level reaches the separation tank and the circulation pump starts operating.
本発明は、かかる従来のボイラ制御方法の問題点を解決
すべくなされたものであり、負荷変化時給水量を循環水
量との和が所定の値になるように変化させ、燃料量を負
荷によって制御される主蒸気弁の開度によって定まる主
蒸気圧カケ所定の値になるように制御させる循環装置付
貫流ボイラの制御方法を提供せんとするものである。The present invention was made in order to solve the problems of the conventional boiler control method, and it changes the water supply amount at the time of load change so that the sum of the circulating water amount becomes a predetermined value, and controls the fuel amount depending on the load. It is an object of the present invention to provide a method for controlling a once-through boiler with a circulation device, which controls the main steam pressure drop to a predetermined value, which is determined by the opening degree of the main steam valve.
以下本発明による循環装置付貫流ボイラの制御方法の一
実施例を詳述する。図は本性を実施する循環装置付貫流
ボイラとその制御装置を示す図であって、貫流ボイラは
、直列に接続された給水ボンダ11蒸発器2、気水分離
器8、過熱器4.4′及び過熱器4.4′間の過熱低減
器5と、気水分離器8から蒸発器2の入口付近までの経
路に設けられた分離タンク6、微積ボンブフ會含む循環
装量から構成されている。この循環装置付貫流ボイラに
は制御装置が設けられ、該制御装置は給水ポンプ1の出
口側に設は念給水調節弁8及びこれを制御する給水量調
節器9と、燃料供給路10に設けた燃料調節弁11及び
これf jjtlJ御する燃料量調節器lzと、主蒸気
管115に設けた主蒸気弁14及びこれを制御する蒸気
量調節器IIsと、蒸発器急の入口(給水と循環水の合
流点よりも蒸発器2側)K設けた給水流量計16及び負
荷信号と動負荷信号の大きい方を選択する選別器1フと
、ボイラ出口圧力計18と、循環ポンプ7の出口側に設
けた循環水調節弁19及び分離タンク6の水位が一定と
なるよう圧制御する循環水調節器!IOとから構成され
ている。An embodiment of the method for controlling a once-through boiler with a circulation device according to the present invention will be described in detail below. The figure shows a once-through boiler with a circulation device and its control device, which implements the main function. It consists of a desuperheater 5 between the superheaters 4 and 4', a separation tank 6 provided in the path from the steam separator 8 to near the inlet of the evaporator 2, and a circulation charge including a microvolume bombeuf. There is. This once-through boiler with a circulation device is provided with a control device, and the control device is installed on the outlet side of the water supply pump 1, and includes a special water supply control valve 8 and a water supply amount regulator 9 that controls this, and a fuel supply path 10. the main steam valve 14 installed in the main steam pipe 115 and the steam amount regulator IIs that controls it, the evaporator sudden inlet (water supply and circulation (on the evaporator 2 side rather than the water confluence point) K equipped with a feedwater flow meter 16, a selector 1f that selects the larger of the load signal and the dynamic load signal, a boiler outlet pressure gauge 18, and the outlet side of the circulation pump 7. A circulating water regulator that controls the pressure so that the water level of the circulating water regulating valve 19 and separation tank 6 provided in the is constant! It is composed of IO.
尚、実際の制御装置は種々の補正回路、フィードフォワ
ードなどがあって複雑であるが、本発明に関係の少ない
部分は省略した。Note that although the actual control device is complicated as it includes various correction circuits, feed forwards, etc., parts that are less relevant to the present invention have been omitted.
さて、前記の如く構成された循環装置付貫流ボイラとそ
の制御装置に於いて、見負荷を超える高負荷から晃負荷
以下の低負荷に下げようとする時、要求負荷信号を蒸気
量調節器15に入れ、主蒸気弁14t−必要な開度にす
ると、タービンの出力は要求負荷に見合った値となる。Now, in the once-through boiler with a circulation device and its control device configured as described above, when it is desired to lower the load from a high load exceeding the expected load to a low load below the light load, the required load signal is sent to the steam amount controller 15. When the main steam valve 14t is opened to the required degree, the output of the turbine becomes a value commensurate with the required load.
しかしボイラの発生蒸気量は減少しないので、主蒸気弁
14の入口(ボイラ出口)の蒸気圧力は高くなり過ぎる
。そこでこの圧力をボイラ出口圧力針18で測り、これ
が所定(一定又は負荷の関数)の値になるように燃料量
調節器1zによって燃料調節弁11の開度を制御し、燃
料量を減少する。この時給水量はこれまで負荷信号に見
合うよう制御されてい念が、要求負荷が軸負荷Klkる
と、選別器17が働いて殆負荷の信号を拾って蒸発器2
0入口給水量がi負荷に相当する量になるように給水流
量計16及び給水量調節器9の信号により給水調節弁8
を操作する。循環ポンプ7は分離タンク6に水位が現れ
るまでは稼動せず、水位が現れると稼動し、循環水調節
弁−19は分離タンク6の水位が一定となるように制御
される。循環水量が増えてくると、給水流量は減ってい
く。燃料量は前記のように一旦急速に減るので、蒸発器
Bの発生蒸気が少なく、従って分離タンク6に入る水量
が多くなるので、水位が急速に現れる。この時主蒸気弁
14の入口蒸気圧力が低下するので、燃料量が増え、最
終的には給水量と共に負荷に見合り素置になる。However, since the amount of steam generated by the boiler does not decrease, the steam pressure at the inlet of the main steam valve 14 (boiler outlet) becomes too high. Therefore, this pressure is measured by the boiler outlet pressure needle 18, and the opening degree of the fuel control valve 11 is controlled by the fuel amount regulator 1z so that this pressure becomes a predetermined value (constant or a function of load), thereby reducing the fuel amount. The amount of water supplied at this time has been controlled so far to match the load signal, but when the required load becomes the shaft load Klk, the separator 17 operates and picks up the almost load signal and sends it to the evaporator 2.
The water supply control valve 8 is activated by the signals from the water supply flow meter 16 and the water supply amount regulator 9 so that the water supply amount at the 0 inlet becomes the amount corresponding to the i load.
operate. The circulation pump 7 does not operate until the water level appears in the separation tank 6, and starts operating once the water level appears, and the circulating water control valve 19 is controlled so that the water level in the separation tank 6 is constant. As the amount of circulating water increases, the water supply flow rate decreases. Since the amount of fuel is once rapidly reduced as described above, the amount of steam generated by the evaporator B is small, and therefore the amount of water entering the separation tank 6 is increased, so that the water level appears rapidly. At this time, the inlet steam pressure of the main steam valve 14 decreases, so the amount of fuel increases, and eventually the amount of water and the amount of water supplied are reduced to match the load.
賞、本発明の制御方法に於いて、一時的に発生蒸気量が
多く(蒸発器2の熱容量の為発生蒸気量が減らない)、
燃料量が減り、過熱蒸気温度が低下する場合があるが、
このような場合には燃料量調節器1zの比例帯などの制
御変数を調整することによって簡単に燃料量の減少量及
び減少速度に制限を加えることができる。また同じよう
に、燃料量の下限を設けるのが良い場合に4h制御侠置
により簡単に制御できる。Prize: In the control method of the present invention, the amount of generated steam is temporarily large (the amount of generated steam does not decrease due to the heat capacity of the evaporator 2),
Although the amount of fuel may decrease and the superheated steam temperature may decrease,
In such a case, by adjusting control variables such as the proportional band of the fuel amount regulator 1z, it is possible to easily limit the amount and speed of decrease in the fuel amount. Similarly, if it is desirable to set a lower limit on the amount of fuel, it can be easily controlled using the 4-hour control mechanism.
以上詳記した通り本発明による循環装置付貫流ボイラの
制御方法は、負荷変化時給水量を循環水量との和が所定
の値となるように変化させ、燃料量を負荷によって制御
される主蒸気弁の開度によって定まる主蒸気圧力を所定
の値になるように制御するのであるから、燃料量と給水
量を負荷に見合った値に増減できて蒸発器の水位を負荷
費化に追従させることができる。従って蒸発器に於いて
流れの不均衡や振動が生じることがなく、ま念ボイラ各
部で蒸気温度の低下が無く、トラブルの発生も無い。As described in detail above, the control method for a once-through boiler with a circulation device according to the present invention changes the water supply amount at the time of load change so that the sum of the circulating water amount becomes a predetermined value, and the fuel amount is controlled by the main steam valve controlled by the load. Since the main steam pressure, which is determined by the opening of can. Therefore, there is no flow imbalance or vibration in the evaporator, no drop in steam temperature at any part of the boiler, and no troubles.
図は制御装[iを備えた循環装看付貫流ボイラの系統図
である。
1・・・給水ポンプ 2・・・蒸発器 8・・・気水分
離器4.4′・・・過熱器 5・・・過熱低減器 6・
・・分離タンク ?・・・循環ポンプ 8・・・給水調
節弁 9・・・給水量調節器 10・・・燃料供給路
11・・・燃料調節弁 12・・・燃料量調節器 18
・・・主蒸気管14・・・主蒸気弁 16・・・蒸気t
a節器 16・・・給水流量計 17・・・選別器 1
8・・・ボイラ出口圧力計 19・・・循環水調節弁
20・・・循環水調節器The figure is a system diagram of a once-through boiler with circulation system equipped with a control system [i]. 1... Water supply pump 2... Evaporator 8... Steam/water separator 4.4'... Superheater 5... Superheat reducer 6.
...Separation tank? ...Circulation pump 8...Water supply control valve 9...Water supply amount regulator 10...Fuel supply path
11...Fuel control valve 12...Fuel amount regulator 18
...Main steam pipe 14...Main steam valve 16...Steam t
a moderator 16...water supply flowmeter 17...selector 1
8... Boiler outlet pressure gauge 19... Circulating water control valve
20...Circulating water regulator
Claims (1)
量を循環水量との和が所定の値となるように変化させる
と共に1燃料量を負荷によって制御される主蒸気弁の開
度によって定まる主蒸気圧力を所定の値になるように制
御させることt−特徴とする循環装置付貫流ボイラの制
御方法。In a once-through boiler with circulating capacity, the amount of water supplied at the time of load change is changed so that the sum of the amount of circulating water becomes a predetermined value, and one fuel amount is changed to the main amount determined by the opening degree of the main steam valve controlled by the load. A method for controlling a once-through boiler with a circulation device, characterized in that the steam pressure is controlled to a predetermined value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13501781A JPS5837405A (en) | 1981-08-28 | 1981-08-28 | Method of controlling once-through boiler with circulator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13501781A JPS5837405A (en) | 1981-08-28 | 1981-08-28 | Method of controlling once-through boiler with circulator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5837405A true JPS5837405A (en) | 1983-03-04 |
Family
ID=15141981
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13501781A Pending JPS5837405A (en) | 1981-08-28 | 1981-08-28 | Method of controlling once-through boiler with circulator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5837405A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59195003A (en) * | 1983-04-19 | 1984-11-06 | 株式会社荏原製作所 | Method of controlling water level |
US4648826A (en) * | 1984-03-19 | 1987-03-10 | Toray Industries, Inc. | Melt-spinning apparatus |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5636910B2 (en) * | 1974-07-17 | 1981-08-27 |
-
1981
- 1981-08-28 JP JP13501781A patent/JPS5837405A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5636910B2 (en) * | 1974-07-17 | 1981-08-27 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59195003A (en) * | 1983-04-19 | 1984-11-06 | 株式会社荏原製作所 | Method of controlling water level |
US4648826A (en) * | 1984-03-19 | 1987-03-10 | Toray Industries, Inc. | Melt-spinning apparatus |
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