JPS58198602A - Controller for feed pump of boiler - Google Patents

Controller for feed pump of boiler

Info

Publication number
JPS58198602A
JPS58198602A JP7984482A JP7984482A JPS58198602A JP S58198602 A JPS58198602 A JP S58198602A JP 7984482 A JP7984482 A JP 7984482A JP 7984482 A JP7984482 A JP 7984482A JP S58198602 A JPS58198602 A JP S58198602A
Authority
JP
Japan
Prior art keywords
pump
flow rate
pressure
boiler
discharge pressure
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
Application number
JP7984482A
Other languages
Japanese (ja)
Inventor
正人 岡野
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP7984482A priority Critical patent/JPS58198602A/en
Publication of JPS58198602A publication Critical patent/JPS58198602A/en
Pending legal-status Critical Current

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  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Control Of The Air-Fuel Ratio Of Carburetors (AREA)
  • Jet Pumps And Other Pumps (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、給水流量制御弁とポンプ回転数制御を併用す
るボイラ給水ポンプの制御装置、特に、変圧運転プラン
ト用ボイラ給水ポンプに好適な制御!ll1lllK1
11するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a control device for a boiler feed pump that uses both a feed water flow rate control valve and pump rotation speed control, and is particularly suitable for a boiler feed pump for a variable pressure operation plant! ll1llllK1
11.

変圧運転方式による火力発電プラントにおいては、負荷
が小さい場合にボイラ給水ポンプ(以下、単にポンプと
いう。)の吐出圧力も下げて運転される。
In a thermal power plant using a variable pressure operation method, when the load is small, the discharge pressure of the boiler feed water pump (hereinafter simply referred to as pump) is also lowered and operated.

ところが、ポンプの運転¥f性から、ポンプの定格流量
以下の流量において、過流Iとなる。このことを第1図
により説明する。
However, due to the operation characteristics of the pump, excessive flow I occurs at a flow rate below the rated flow rate of the pump. This will be explained with reference to FIG.

第1図において、縦軸は圧力、横軸は流量を示しており
、図中の扇形の範囲がポンプの運転頭載である。
In FIG. 1, the vertical axis shows pressure and the horizontal axis shows flow rate, and the fan-shaped range in the figure is the operating head of the pump.

ポンプの吐出圧力は、図の実線L1に従って運転される
ため、ポンプは点P1より流量を増やすことができず、
そのため、従来は、早目に2台目のポンプを起動させる
必要がある。しかも、発電出力が高い領域では、ポンプ
の吐出圧力も高くなるので、ポンプは定格流tQ1tで
出すことができるが、運転員は発電出力やポンプ吐出出
力を監視してその状態でポンプの流量をどこまで増やせ
るか判断しなければならない。
Since the discharge pressure of the pump is operated according to the solid line L1 in the figure, the pump cannot increase the flow rate beyond point P1,
Therefore, conventionally, it is necessary to start the second pump early. Moreover, in a region where the power generation output is high, the discharge pressure of the pump is also high, so the pump can output at the rated flow tQ1t, but the operator monitors the power generation output and pump discharge output and adjusts the pump flow rate accordingly. You have to decide how much you can increase it.

本発明の目的は、ポンプの運転状部を過流量域からポン
プが運転可能な領域に制御し、ポンプ1台での運転範囲
を拡大させることができるポンプ制御装置を提供するこ
とにある。
An object of the present invention is to provide a pump control device that can control the operating state of a pump from an overflow region to a region where the pump can operate, thereby expanding the operating range of a single pump.

このような目的を達成するために、本発明では、ボイラ
への給水圧力をポンプ定格仕様より低い圧力で使用する
場合に、ポンプ定格流量以下でボイラ給水ポンプが過流
−となる領域において、ポンプの特性に応じてポンプ吐
出圧力を高くして運転を可能にしたことに特徴がある。
In order to achieve such an objective, in the present invention, when the water supply pressure to the boiler is used at a pressure lower than the pump rated specification, the pump The unique feature is that the pump can be operated by increasing the pump discharge pressure according to the characteristics of the pump.

以下、本発明の実施例を図面により詳細に説明する。Embodiments of the present invention will be described in detail below with reference to the drawings.

第2図は本発明の詳細な説明するグラフで、第1図と同
様に、縦軸は圧力、横軸はAllを示している。
FIG. 2 is a graph explaining the present invention in detail, and like FIG. 1, the vertical axis shows pressure and the horizontal axis shows All.

ボイラ給水ポンプの制御装置では、ポンプ出口側に設置
した給水流1制御弁でポンプの流1k1111Oglを
行ない、ポンプの回転数はポンプ吐出圧力で制御するよ
うになっている。
In the control device for the boiler feed water pump, the feed water flow 1 control valve installed on the pump outlet side controls the pump flow 1k1111Ogl, and the rotation speed of the pump is controlled by the pump discharge pressure.

この給水流1制御弁の差圧を一定にすると、第2図にお
いて、ポンプ吐出圧力(差圧一定)は実線L1で、給水
流量制御弁出口圧力は一点鎖線L2で示されるようにな
る。これは、給水流量制御弁を制御に必要な最小限の差
圧とすることによってポンプ吐出圧力を出来るだけ低く
し軸動力を低減するためであるが、その場合、帥述した
ような問題点がある。
When the differential pressure of the feed water flow 1 control valve is held constant, the pump discharge pressure (differential pressure constant) is shown by a solid line L1, and the feed water flow rate control valve outlet pressure is shown by a dashed line L2 in FIG. This is to reduce the pump discharge pressure as much as possible and reduce the shaft power by setting the water supply flow rate control valve to the minimum differential pressure necessary for control, but in that case, the problems mentioned above occur. be.

そこで、本発明では、給水流量制御弁の差圧を可変とす
ることにより、ポンプ吐出圧力を第2図の破線L3で示
すようにして、過流量とならないようにしている。
Therefore, in the present invention, by making the differential pressure of the water supply flow rate control valve variable, the pump discharge pressure is set as indicated by the broken line L3 in FIG. 2, and an excessive flow rate is prevented.

第3図は本発明によるポンプ制御装置の一実施例を示す
亀ので、1けポンプ、2け可変速装置、3け原#機、4
は給水流量制御弁、5および6は圧力検出器、7は減算
器、&け偏差演算器、9は比例積分演算器、9は比例積
分演算器、10は差圧信号発生器、11け高値選択器、
12および13#i差圧発生器、14Ifiバイアス器
、15け減算器である。
Figure 3 shows an embodiment of the pump control device according to the present invention, including a 1-piece pump, a 2-piece variable speed device, a 3-piece pump, and a 4-piece pump.
is a water supply flow rate control valve, 5 and 6 are pressure detectors, 7 is a subtractor, & is a deviation calculator, 9 is a proportional integral calculator, 9 is a proportional integral calculator, 10 is a differential pressure signal generator, and 11 is a high value. selector,
12 and 13 #i differential pressure generators, 14 Ifi bias device, and 15 digit subtractor.

このような構成において、ポンプ1は可変速装置2を介
して原動機3に接続され、可変速装置2を加減すること
により、ポンプ1の回転数を制御する。
In such a configuration, the pump 1 is connected to the prime mover 3 via the variable speed device 2, and the rotation speed of the pump 1 is controlled by adjusting the variable speed device 2.

従来は、差圧−量制御として給水流量制御弁4の繭後の
圧力を圧力検出器5.6で検出し、減算器7で給水流量
制御弁の差圧を求め、この差圧を偏差演算器8と比例積
分演算器9を通して可変連装#2に入力し、予じめ設定
し走差圧信号発生器10の出力との偏差が常になくなる
ように可変速装置lt2を操作している。
Conventionally, as differential pressure-volume control, the pressure after cocooning of the water supply flow rate control valve 4 is detected by a pressure detector 5.6, the differential pressure of the water supply flow rate control valve is obtained by a subtractor 7, and this differential pressure is calculated by a deviation calculation. The signal is input to the variable speed unit #2 through the unit 8 and the proportional integral calculator 9, and the variable speed unit lt2 is operated so that there is always no deviation from the preset output of the running differential pressure signal generator 10.

本発明の実施例では、ポンプ1の入口に設置fした流量
検出用差圧発生器12、差圧検出器13、バイアス器1
4、減算器15、高値選値器11を新たに付加している
In the embodiment of the present invention, a flow rate detection differential pressure generator 12, a differential pressure detector 13, and a bias device 1 are installed at the inlet of the pump 1.
4. A subtracter 15 and a high value selector 11 are newly added.

ポンプlの吐出圧力PAとその圧力時の最大流量Q1と
は、次の(1)式の関係がある。
The relationship between the discharge pressure PA of the pump l and the maximum flow rate Q1 at that pressure is expressed by the following equation (1).

Q、中k[・・・・・・(1) 但し、kけ定数である。Q, middle k [・・・・・・(1) However, it is a k constant.

ここで、逆に、あるポンプ入口流量Q!におけるポンプ
吐出圧力の最低値P、け次の(2)式のようにすること
ができる。
Here, conversely, a certain pump inlet flow rate Q! The lowest value P of the pump discharge pressure at can be expressed by the following equation (2).

p 、 *に/ Q I*     ・・・・・・(2
)但し、k′は定数である。
p , * to / Q I * ・・・・・・(2
) However, k' is a constant.

そこで、本発明では、ポンプ吐出圧力P、がポンプ入口
流量Q!から得られる最低圧力以上となるように制御し
ている。そのため、差圧発生器12でポンプ入口流量Q
1を検出するが、差圧式流量検出の場合に取り出される
信号は流−の2乗こに比例するので得られた信号は最底
圧力P、の信号となる。この信号にバイアス器14で若
干のバイアス分を乗せているが、これは、制御装置の遅
れ等によりポンプが過流量となるのを防止するためKi
tlJa上の余裕を取るためである。このようにして得
られた信号は第2図の破線L3のポンプ吐出圧力設定値
となる。
Therefore, in the present invention, the pump discharge pressure P is changed to the pump inlet flow rate Q! The pressure is controlled so that it is at least the lowest pressure that can be obtained. Therefore, the pump inlet flow rate Q at the differential pressure generator 12
1, but since the signal extracted in the case of differential pressure type flow rate detection is proportional to the square of the flow, the obtained signal is a signal of the bottom pressure P. A slight bias is added to this signal by the bias device 14, but this is done to prevent the pump from overflowing due to delays in the control device, etc.
This is to ensure a margin on tlJa. The signal obtained in this manner becomes the pump discharge pressure setting value indicated by the broken line L3 in FIG.

バイアス器14からの信号と、給水流!制御弁当ロ圧力
検出器6の信号との差を減算器15でとり、給水流量制
御弁4の差圧設定値を演算する。
Signal from bias device 14 and water supply flow! A subtracter 15 takes the difference between the signal from the control lunchbox pressure detector 6 and calculates the differential pressure setting value of the water supply flow rate control valve 4.

この差圧設定値と、差圧−量制御用の設定信号発生器1
0の出力とを高値選択器11に入力し、それらの人力信
号の内、大きい方の信号を差圧設定値として制御する。
This differential pressure setting value and a setting signal generator 1 for differential pressure/volume control
The output of 0 is input to the high value selector 11, and the larger signal among these human input signals is controlled as the differential pressure setting value.

このようにすれば、過流量域に入る前にポンプ吐出圧力
が上るので過流庸とはならない。
If this is done, the pump discharge pressure will rise before entering the overflow region, so no overflow will occur.

以上述べたように、本発明によれば、変圧運転のために
圧力を下げた状態において、ポンプの吐出圧力をポンプ
特性に応じて高く制御することができるので、従来、ポ
ンプの運転ができなかった領域例えば、第1図の例では
、点P1から定格流IQI近傍の点までの領域まで運転
できるようになった。
As described above, according to the present invention, when the pressure is lowered for variable pressure operation, the discharge pressure of the pump can be controlled to be high according to the pump characteristics. For example, in the example shown in FIG. 1, operation is now possible from point P1 to a point near the rated flow IQI.

このように、ポンプの運転状態を過流Wktaからポン
プの運転可能な領域になるように制御することにより、
ポンプ1台での運転範囲を著るしく拡大することができ
る。
In this way, by controlling the operating state of the pump from the excess flow Wkta to the region where the pump can be operated,
The operating range of a single pump can be significantly expanded.

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

第1図は従来のポンプの運転特性を示す図、第2図は本
発明によるポンプの運転特性を説明する図、第3図は本
発明によるポンプ制御装置の一実施例の構成を示す図で
ある。
FIG. 1 is a diagram showing the operating characteristics of a conventional pump, FIG. 2 is a diagram explaining the operating characteristics of a pump according to the present invention, and FIG. 3 is a diagram showing the configuration of an embodiment of a pump control device according to the present invention. be.

Claims (1)

【特許請求の範囲】 1、ボイラ給水ポンプと、該ポンプの回転数を制御する
制御手段と、上記ポンプの給水流量を制御するために上
記ポンプの出口に設置した給水流量制御弁とからなるボ
イラ給水ポンプの制御装置において、上記ポンプの定格
流量以下で、上記ポンプが過流量となる領域において、
上記ポンプの特性に応じて該ポンプの吐出圧力を高くし
て運転可能にする手段を備えたことを特徴とするボイラ
給水ポンプ制御装置。 2、前記ポンプの特性に応じたポンプ吐出圧力を上記ポ
ンプの入口流量より決定するようにしたことを特徴とす
る特許請求の範囲第1項記載のボイラ給水ポンプ制御装
置。
[Claims] 1. A boiler comprising a boiler feed water pump, a control means for controlling the rotation speed of the pump, and a water feed flow rate control valve installed at the outlet of the pump to control the water feed flow rate of the pump. In a control device for a water supply pump, in a region where the pump has an excessive flow rate below the rated flow rate of the pump,
A boiler feed water pump control device characterized by comprising means for increasing the discharge pressure of the pump in accordance with the characteristics of the pump to enable operation. 2. The boiler feed water pump control device according to claim 1, wherein the pump discharge pressure according to the characteristics of the pump is determined from the inlet flow rate of the pump.
JP7984482A 1982-05-14 1982-05-14 Controller for feed pump of boiler Pending JPS58198602A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7984482A JPS58198602A (en) 1982-05-14 1982-05-14 Controller for feed pump of boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7984482A JPS58198602A (en) 1982-05-14 1982-05-14 Controller for feed pump of boiler

Publications (1)

Publication Number Publication Date
JPS58198602A true JPS58198602A (en) 1983-11-18

Family

ID=13701507

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7984482A Pending JPS58198602A (en) 1982-05-14 1982-05-14 Controller for feed pump of boiler

Country Status (1)

Country Link
JP (1) JPS58198602A (en)

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