JPH0934557A - Water distribution terminal pressure controller - Google Patents

Water distribution terminal pressure controller

Info

Publication number
JPH0934557A
JPH0934557A JP20027395A JP20027395A JPH0934557A JP H0934557 A JPH0934557 A JP H0934557A JP 20027395 A JP20027395 A JP 20027395A JP 20027395 A JP20027395 A JP 20027395A JP H0934557 A JPH0934557 A JP H0934557A
Authority
JP
Japan
Prior art keywords
water distribution
pressure
target value
discharge pressure
discharge
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
JP20027395A
Other languages
Japanese (ja)
Inventor
Kenji Takeuchi
賢治 竹内
Futoshi Kurokawa
太 黒川
Shuichiro Kobayashi
主一郎 小林
Masanaga Niiyama
雅永 新山
Tatsuo Ashiki
達雄 芦木
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP20027395A priority Critical patent/JPH0934557A/en
Publication of JPH0934557A publication Critical patent/JPH0934557A/en
Pending legal-status Critical Current

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  • Control Of Positive-Displacement Pumps (AREA)
  • Feedback Control In General (AREA)
  • Control Of Non-Electrical Variables (AREA)
  • Control Of Fluid Pressure (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a water distribution terminal pressure controller which can secure the desired water distribution terminal pressure in response to its demand factor and with the desired response when the terminal pressure is controlled at a fixed level. SOLUTION: A target discharge pressure value calculation means 9 calculates the correction value of the target discharge pressure value by the fuzzy inference based on the deviation between the water distribution terminal pressure and its set value and also the discharge flow rate of a water distribution pump, so that the terminal pressure is kept at its set value. The target discharge pressure value is corrected based on the calculated correction value. A water distribution pump rotational frequency control means 10 controls the rotational frequency of the distribution pump, so that the discharge pressure of the pump is set at the target discharge pressure value corrected by the means 9. Thus it is possible to apply the proper control even to a nonlinear change characteristic that is defined between the water distribution terminal pressure and the discharge flow rate of the pump.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、配水管網の配水末
端圧力の一定制御を行なうにあたり、需要量に従って応
答を変えられる制御を行なうための配水末端圧力制御装
置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water distribution end pressure control device for controlling the water distribution end pressure of a water distribution pipe network so that the response can be changed according to the demand.

【0002】[0002]

【従来の技術】一般に、各家庭に供給される水道水は、
各家庭付近の道路下に埋没された配水管からの配水され
るようになっている。この所定地域内の配水管全体を配
水管網と呼んでいる。そして、河川から送られてくる水
は、浄化場を経由して配水池に溜められ、この溜められ
た水を配水ポンプにより配水管網に送り出している。
2. Description of the Related Art Generally, tap water supplied to each home is
Water is distributed from a distribution pipe buried under the road near each home. The entire distribution pipe in this prescribed area is called the distribution network. Then, the water sent from the river is stored in a distribution reservoir via a purification plant, and the stored water is sent to a distribution pipe network by a distribution pump.

【0003】ところで、各家庭で水道水を快適に使用す
るためには、水道水の圧力はできるだけ一定であること
が要求される。したがって、配水管網における圧力、即
ち配水末端圧力を一定にするための制御を行なう必要が
あるが、その制御応答は需要量の大きさによって所定の
応答が得られることが望まれている。この配水末端圧力
制御には、従来から、主として、いわゆる推定末端圧力
制御又はPI制御が行なわれている。
By the way, in order to comfortably use tap water in each home, the pressure of tap water is required to be as constant as possible. Therefore, it is necessary to control the pressure in the water distribution network, that is, the pressure at the water distribution end to be constant, and it is desired that the control response be a predetermined response depending on the amount of demand. Conventionally, so-called estimated end pressure control or PI control has been mainly performed for the water distribution end pressure control.

【0004】推定末端圧力制御とは、配水ポンプの吐出
圧力及び吐出流量をそれぞれPO、Qとした場合に、配水
管網内の圧力損失分Rfを推定し、P1=PO-Rf・Q で表され
る配水末端圧力P1が一定となるように吐出圧力POを調整
する制御である。また、PI制御とは、配水管網内の所
定箇所に設置された圧力計により検出された配水末端圧
力とその配水末端圧力設定値との偏差に基づいて、比例
積分演算により配水ポンプの吐出圧力目標値を求め、こ
れにより吐出圧力がその吐出圧力目標値に追従するよう
に制御するものである。
Estimated terminal pressure control is to estimate the pressure loss Rf in the water distribution network when the discharge pressure and the discharge flow rate of the water distribution pump are PO and Q, respectively, and express it as P1 = PO-Rf · Q. This is a control for adjusting the discharge pressure PO so that the distribution end pressure P1 is constant. The PI control is a discharge pressure of a water distribution pump calculated by proportional-plus-integral calculation based on a deviation between a water distribution end pressure detected by a pressure gauge installed at a predetermined position in the water distribution network and a set value of the water distribution end pressure. A target value is obtained, and thereby the discharge pressure is controlled so as to follow the discharge pressure target value.

【0005】[0005]

【発明が解決しようとする課題】しかし、推定末端圧力
制御では、圧力損失分Rfの推定値と実際値とに誤差を持
つため、その場合には所望の配水末端圧力を得ることが
できなくなる。また、PI制御では、設計したパラメー
タに従って、需要量が多い場合にも少ない場合にも同じ
制御応答でしか制御することができない。つまり、制御
応答は需要量となる配水ポンプの吐出流量によって変え
ることができない。
However, in the estimated terminal pressure control, there is an error between the estimated value and the actual value of the pressure loss Rf, and in that case, the desired water distribution terminal pressure cannot be obtained. Further, according to the designed parameter, the PI control can be controlled only with the same control response when the demand amount is large or small. That is, the control response cannot be changed depending on the discharge flow rate of the water distribution pump, which is the demand amount.

【0006】本発明の目的は、配水末端圧力の一定制御
を行なうにあたり、所望の値の配水末端圧力を需要量の
大きさに応じて所望の応答で得ることができる配水末端
圧力制御装置を提供することである。
An object of the present invention is to provide a water distribution end pressure control device capable of obtaining a desired value of the water distribution end pressure with a desired response in accordance with the magnitude of demand when performing constant control of the water distribution end pressure. It is to be.

【0007】[0007]

【課題を解決するための手段】請求項1の発明は、配水
末端圧力とその配水末端圧力設定値との偏差及び配水ポ
ンプの吐出流量に基づいてファジィ推論により配水ポン
プの吐出圧力目標値の修正量を算出しこの修正量に基づ
いて吐出圧力目標値を修正する吐出圧力目標値演算手段
と、配水ポンプの吐出圧力が吐出圧力目標値演算手段で
修正された吐出圧力目標値になるように配水ポンプの回
転数を制御する配水ポンプ回転数制御手段とを備えたも
のである。
According to a first aspect of the present invention, the discharge pressure target value of the water distribution pump is corrected by fuzzy inference based on the deviation between the water distribution end pressure and the set value of the water distribution end pressure and the discharge flow rate of the water distribution pump. A discharge pressure target value calculating means for calculating the amount and correcting the discharge pressure target value based on this correction amount, and a water distribution so that the discharge pressure of the water distribution pump becomes the discharge pressure target value corrected by the discharge pressure target value calculating means. The water distribution pump rotation speed control means for controlling the rotation speed of the pump is provided.

【0008】請求項2の発明は、請求項1の発明におい
て、吐出圧力目標値演算手段は、配水末端圧力とその配
水末端圧力設定値との偏差及び配水ポンプの吐出流量に
基づいてファジィ推論により得た第1の修正量と、配水
末端圧力とその配水末端圧力設定値との偏差の変化率及
び配水ポンプの吐出流量に基づいてファジィ推論により
得た第2の修正量との双方に基づいて、吐出圧力目標値
を修正するようにしたものである。
According to a second aspect of the present invention, in the first aspect of the present invention, the discharge pressure target value calculating means uses fuzzy inference based on the deviation between the distribution end pressure and the distribution end pressure set value and the discharge flow rate of the distribution pump. Based on both the first correction amount obtained and the second correction amount obtained by fuzzy inference based on the change rate of the deviation between the distribution end pressure and the set value of the distribution end pressure and the discharge flow rate of the distribution pump. The discharge pressure target value is corrected.

【0009】請求項3の発明は、請求項2の発明におい
て、吐出圧力目標値演算手段は、第1の修正量及び第2
の修正量に、それぞれ所定のゲインを乗じるようにした
ものである。
According to a third aspect of the present invention, in the second aspect of the invention, the discharge pressure target value calculating means includes a first correction amount and a second correction amount.
The correction amount of is multiplied by a predetermined gain.

【0010】請求項1の発明においては、吐出圧力目標
値演算手段は、配水末端圧力とその配水末端圧力設定値
との偏差及び配水ポンプの吐出流量に基づいてファジィ
推論により、配水末端圧力が配水末端圧力設定値に維持
されるように、吐出圧力目標値の修正量を算出し、この
修正量に基づいて吐出圧力目標値を修正する。配水ポン
プ回転数制御手段は、配水ポンプの吐出圧力が吐出圧力
目標値演算手段で修正された吐出圧力目標値になるよう
に配水ポンプの回転数を制御する。これにより、配水末
端圧力と吐出流量との非線形な変化特性に対しても適切
な制御が可能となる。
According to the first aspect of the present invention, the discharge pressure target value calculating means uses the fuzzy inference based on the deviation between the distribution end pressure and the set value of the distribution end pressure and the discharge flow rate of the distribution pump to determine the distribution end pressure. The correction amount of the discharge pressure target value is calculated so as to be maintained at the terminal pressure setting value, and the discharge pressure target value is corrected based on this correction amount. The water distribution pump rotation speed control means controls the rotation speed of the water distribution pump so that the discharge pressure of the water distribution pump becomes the discharge pressure target value corrected by the discharge pressure target value calculation means. As a result, it is possible to appropriately control the non-linear change characteristic of the water distribution end pressure and the discharge flow rate.

【0011】請求項2の発明においては、請求項1の発
明の作用に加え、吐出圧力目標値演算手段では、配水末
端圧力とその配水末端圧力設定値との偏差及び配水ポン
プの吐出流量に基づいてファジィ推論を行い、それによ
り得た第1の修正量と、配水末端圧力とその配水末端圧
力設定値との偏差の変化率及び配水ポンプの吐出流量に
基づいてファジィ推論を行い、それにより得た第2の修
正量との双方に基づいて吐出圧力目標値を修正する。こ
の場合、第1の修正量がPI制御におけるI要素(積分
要素)の制御動作信号に相当し、第2の修正量がPI制
御におけるP要素(比例要素)の制御動作信号に相当す
る非線形PI制御とみなして設計することができる。こ
れにより、従来のPI制御では不可能な吐出流量に対す
る非線形的な変化を行なわせながら、PI制御と同等の
制御を行なうことができる。
According to the invention of claim 2, in addition to the operation of the invention of claim 1, the discharge pressure target value calculating means is based on the deviation between the distribution end pressure and the set value of the distribution end pressure and the discharge flow rate of the distribution pump. Fuzzy inference based on the first correction amount, the change rate of the deviation between the distribution end pressure and the set value of the distribution end pressure, and the discharge flow rate of the distribution pump. The discharge pressure target value is corrected based on both the second correction amount and the second correction amount. In this case, the first correction amount corresponds to the control operation signal of the I element (integral element) in PI control, and the second correction amount corresponds to the control operation signal of the P element (proportional element) in PI control. It can be regarded as control and designed. As a result, it is possible to perform the same control as the PI control while making a non-linear change in the discharge flow rate, which is impossible with the conventional PI control.

【0012】請求項3の発明においては、請求項2の発
明の作用に加え、吐出圧力目標値演算手段では、第1の
修正量及び第2の修正量にそれぞれ所定のゲインを乗じ
る。これにより、I要素とP要素との比率を変更するこ
とができる。
According to the invention of claim 3, in addition to the operation of the invention of claim 2, the discharge pressure target value calculating means multiplies the first correction amount and the second correction amount by predetermined gains. Thereby, the ratio of the I element and the P element can be changed.

【0013】[0013]

【発明の実施の形態】以下、本発明の実施例を図面を参
照して説明する。図1は、本発明の実施例を示すブロッ
ク構成図である。図1において、配水池1の浄水はn台
の配水ポンプP1〜Pnにより配水管網2に配水される
ようになっている。そして、配水ポンプP1〜Pn と配
水管網2との間には吐出圧力計3及び吐出流量計4が設
けられ、配水管網2の所定箇所には配水末端圧力計5が
設けられている。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram showing an embodiment of the present invention. In FIG. 1, the purified water in the distribution reservoir 1 is distributed to the distribution pipe network 2 by n distribution pumps P1 to Pn. A discharge pressure gauge 3 and a discharge flow meter 4 are provided between the water distribution pumps P1 to Pn and the water distribution network 2, and a water distribution terminal pressure gauge 5 is provided at a predetermined position of the water distribution network 2.

【0014】中央管理制御室には、キーボード等の操作
機器であるヒューマンインタフェイス6が設けられてお
り、操作員はCRT表示装置7の表示を見ながらこのヒ
ューマンインタフェイス6を操作できるようになってい
る。ヒューマンインタフェイス6からの指令信号は演算
装置8に出力されるようになっている。演算装置8は、
吐出圧力目標値演算手段9、配水ポンプ回転数制御手段
10、第1のファジィルールテーブル11及び第2のフ
ァジィルールテーブル12を有している。
The central management control room is provided with a human interface 6 which is an operating device such as a keyboard, and an operator can operate the human interface 6 while watching the display on the CRT display device 7. ing. The command signal from the human interface 6 is output to the arithmetic unit 8. The arithmetic unit 8 is
It has a discharge pressure target value calculation means 9, a water distribution pump rotation speed control means 10, a first fuzzy rule table 11 and a second fuzzy rule table 12.

【0015】吐出圧力目標値演算手段9では、配水末端
圧力とその配水末端圧力設定値との偏差及び配水ポンプ
の吐出流量に基づいて、第1のファジィルールテーブル
11によりファジィ推論を行い、それにより第1の修正
量を算出する。一方、配水末端圧力とその配水末端圧力
設定値との偏差の変化率及び配水ポンプの吐出流量に基
づいて、第2のファジィルールテーブル12によりファ
ジィ推論を行い、それにより第2の修正量を算出する。
そして、吐出圧力目標値にこれら双方の修正量を加算し
て、吐出圧力目標値を修正しその修正した吐出圧力目標
値を出力する。また、配水ポンプ回転数制御手段10
は、配水ポンプの吐出圧力が吐出圧力目標値演算手段9
で修正された吐出圧力目標値になるように配水ポンプの
回転数を制御する。
In the discharge pressure target value calculation means 9, fuzzy inference is performed by the first fuzzy rule table 11 based on the deviation between the distribution end pressure and the set value of the distribution end pressure and the discharge flow rate of the distribution pump. A first correction amount is calculated. On the other hand, based on the change rate of the deviation between the distribution end pressure and the set value of the distribution end pressure and the discharge flow rate of the distribution pump, fuzzy inference is performed by the second fuzzy rule table 12, and thereby the second correction amount is calculated. To do.
Then, both of these correction amounts are added to the discharge pressure target value, the discharge pressure target value is corrected, and the corrected discharge pressure target value is output. Further, the water distribution pump rotation speed control means 10
The discharge pressure of the water distribution pump is the discharge pressure target value calculation means 9
The rotation speed of the water distribution pump is controlled so that the discharge pressure target value corrected in step 1 is reached.

【0016】即ち、操作員が設定した配水末端圧力設定
値と計測した配水末端圧力とから配水ポンプPの吐出圧
力目標値をファジィ推論により演算する。このとき、フ
ァジィ推論では、吐出流量及び配水末端圧力の情報を基
に吐出圧力目標値の修正量を演算する。この演算結果に
前回の操作量を加算して新たな修正された吐出圧力目標
値とし、PI演算により配水ポンプの圧力制御を行な
う。
That is, the discharge pressure target value of the water distribution pump P is calculated by fuzzy inference from the water distribution end pressure set value set by the operator and the measured water distribution end pressure. At this time, in the fuzzy inference, the correction amount of the discharge pressure target value is calculated based on the information of the discharge flow rate and the water distribution end pressure. The previous manipulated variable is added to this calculation result to obtain a new corrected discharge pressure target value, and the pressure of the water distribution pump is controlled by PI calculation.

【0017】次に、吐出圧力目標値演算手段9における
ファジィ推論による吐出圧力目標値の修正量の演算につ
いて説明する。ファジィ推論の入力となるのは、配水末
端圧力と配水末端圧力設定値との偏差(配水末端圧力偏
差)、配水末端圧力と配水末端圧力設定値との偏差の変
化率(配水末端圧力偏差の変化率)、及び配水ポンプ吐
出流量である。これらの情報を基に、ファジィ推論で
は、図2に示すように第1のファジィルールテーブル1
1及び第2のファジィルールテーブル12により吐出圧
力目標値の修正量を演算する。
Next, the calculation of the correction amount of the discharge pressure target value by the fuzzy inference in the discharge pressure target value calculation means 9 will be described. The input of fuzzy inference is the deviation between the distribution end pressure and the distribution end pressure set value (distribution end pressure deviation), the change rate of the deviation between the distribution end pressure and the distribution end pressure set value (change in distribution end pressure deviation). Rate), and the discharge flow rate of the water distribution pump. Based on these pieces of information, in the fuzzy inference, as shown in FIG.
The correction amount of the discharge pressure target value is calculated by the first and second fuzzy rule tables 12.

【0018】図2に示すように、第1のファジィルール
テーブル11では、配水末端圧力偏差と吐出流量とによ
り、吐出圧力目標値の第1の修正量を演算する。第2の
ファジィルールテーブル12では、配水末端圧力偏差の
変化率と吐出流量とにより、吐出圧力目標値の第2の修
正量を演算する。そして、加算手段14で、第1のファ
ジィルールテーブル11からの第1の修正量と第2のフ
ァジィルールテーブル12からの第2の修正量とを加算
して、最終の吐出圧力目標値の修正量を算出する。この
形は、第1のルールテーブル11がPI制御におけるI
制御(積分制御)に相当する形、また、第2のルールテ
ーブル12がP制御(比例制御)に相当する形となって
おり、非線形PI制御とみなして設計することができ
る。
As shown in FIG. 2, in the first fuzzy rule table 11, the first correction amount of the discharge pressure target value is calculated from the distribution end pressure deviation and the discharge flow rate. In the second fuzzy rule table 12, a second correction amount of the discharge pressure target value is calculated based on the change rate of the distribution end pressure deviation and the discharge flow rate. Then, the adding means 14 adds the first correction amount from the first fuzzy rule table 11 and the second correction amount from the second fuzzy rule table 12 to correct the final discharge pressure target value. Calculate the amount. In this form, the first rule table 11 is I in PI control.
The second rule table 12 corresponds to the control (integral control) and the second rule table 12 corresponds to the P control (proportional control), and can be designed by considering it as the non-linear PI control.

【0019】次に、吐出流量目標値の修正量をファジィ
推論する方法を説明する。図3(a)は、配水末端圧力
の時間的推移を示すものであり、図3(b)は、吐出流
量の時間的推移を示すものである。いま、図3(a)に
示すように、時刻t-dtでの配水末端圧力設定値Hsv と配
水末端圧力Hpv(t-dt) との偏差をe(t-dt) 、時刻t での
配水末端圧力設定値Hsv と配水末端圧力Hpv(t)との偏差
をe(t)とする。また、図3(b)に示すように、時刻t
での吐出流量をQpv(t)とする。
Next, a method of fuzzy inferring the correction amount of the discharge flow rate target value will be described. FIG. 3 (a) shows a temporal transition of the water distribution end pressure, and FIG. 3 (b) shows a temporal transition of the discharge flow rate. Now, as shown in Fig. 3 (a), the deviation between the distribution end pressure set value Hsv and the distribution end pressure Hpv (t-dt) at time t-dt is e (t-dt), and the distribution at time t The deviation between the terminal pressure setting value Hsv and the water distribution terminal pressure Hpv (t) is e (t). In addition, as shown in FIG.
Let Qpv (t) be the discharge flow rate at.

【0020】このとき、制御周期dtでの配水末端圧力設
定値Hsv と配水末端圧力Hpv(t)との偏差e(t)、偏差の変
化率de(t) は、次式で求められる。
At this time, the deviation e (t) between the water distribution end pressure set value Hsv and the water distribution end pressure Hpv (t) at the control cycle dt and the change rate de (t) of the deviation are obtained by the following equations.

【0021】 e(t)=Hsv-Hpv(t) …(1) de(t)=e(t)-e(t-dt) ={Hsv-Hpv(t)}-{Hsv-Hpv(t-dt)} =Hpv(t-dt)-Hpv(t) …(2) ファジィ推論の入力となる配水末端圧力偏差e(t)、偏差
の変化率de(t) 及び吐出流量Qpv(t)は、実際の推論の際
には下記に示すように正規化する。
E (t) = Hsv-Hpv (t) (1) de (t) = e (t) -e (t-dt) = {Hsv-Hpv (t)}-{Hsv-Hpv (t -dt)} = Hpv (t-dt) -Hpv (t) (2) Distribution end pressure deviation e (t), deviation change rate de (t) and discharge flow rate Qpv (t), which are the inputs of fuzzy inference. Is normalized as shown below during actual inference.

【0022】 e(t)=Hsv-Hpv(t) …(3) de(t)=e(t)-e(t-1) …(4) E(t)=e(t)/Hemax …(5) dE(t)=de(t)/Hdemax …(6) Qm=(Qmax+Qmin)/2 …(7) Qg=(Qmax-Qmin)/2 …(8) Q(t)=(Qpv(t)-Qm)/Qg ここで、 e(t): 配水末端圧力設定値と配水末端圧力との偏差[mA
q] de(t):偏差の変化率[mAq] Hsv:配水末端圧力設定値[mAq] Hpv(t): 配水末端圧力[mAq] Hemax:配水末端圧力偏差幅[mAq] Hdmax:配水末端圧力偏差の変化率幅[mAq] Qmax: 最大吐出流量[m3/h] Qmin: 最小吐出流量[m3/h] Qm:Qmax とQminとの平均[m3/h] Qg:Qmax とQminとの差の絶対値[m3/h] Qpv(t): 実績吐出流量[m3/h] Q(t): 吐出流量を正規化した値 E(t): 配水末端圧力設定値と配水末端圧力との偏差を正
規化した値 dE(t):偏差の変化率を正規化した値 t:時刻 以上の式により正規化された配水末端圧力設定値と配水
末端圧力との偏差E(t)、偏差の変化率dE(t) 及び吐出流
量Q(t)により、吐出圧力目標値の修正量を演算する。
E (t) = Hsv-Hpv (t) (3) de (t) = e (t) -e (t-1) (4) E (t) = e (t) / Hemax ... (5) dE (t) = de (t) / Hdemax… (6) Qm = (Qmax + Qmin) / 2… (7) Qg = (Qmax-Qmin) / 2… (8) Q (t) = ( Qpv (t) -Qm) / Qg where e (t): Deviation between the distribution end pressure setting value and the distribution end pressure [mA
q] de (t): Deviation rate [mAq] Hsv: Distribution end pressure set value [mAq] Hpv (t): Distribution end pressure [mAq] Hemax: Distribution end pressure deviation range [mAq] Hdmax: Distribution end pressure Rate of deviation change [mAq] Qmax: Maximum discharge flow rate [m3 / h] Qmin: Minimum discharge flow rate [m3 / h] Qm: Average of Qmax and Qmin [m3 / h] Qg: Difference between Qmax and Qmin Absolute value [m3 / h] Qpv (t): Actual discharge flow rate [m3 / h] Q (t): Normalized discharge flow rate E (t): Deviation between distribution end pressure setting value and distribution end pressure Normalized value dE (t): Normalized value of deviation change rate t: Deviation E (t), deviation rate of deviation between distribution end pressure set value and distribution end pressure normalized by the formula above The correction amount of the discharge pressure target value is calculated from dE (t) and the discharge flow rate Q (t).

【0023】入力変数である配水末端圧力設定値と配水
末端圧力との偏差、偏差の変化率、吐出流量をそれぞれ
規定するメンバーシップ関数を図4(a) に示す。また、
出力変数である吐出圧力目標値の第1の修正量及び吐出
圧力目標値の第2の修正量をそれぞれ規定するメンバー
シップ関数を図4(b) に示す。
FIG. 4 (a) shows the membership functions that define the deviation between the water distribution end pressure set value and the water distribution end pressure, which are input variables, the deviation change rate, and the discharge flow rate. Also,
FIG. 4 (b) shows the membership functions that define the first correction amount of the discharge pressure target value and the second correction amount of the discharge pressure target value, which are output variables.

【0024】各メンバーシップ関数のPB、PM、P
S、Z、NS、NM、NBの記号の意味を図5に示す。
また、第1のファジィルールテーブル11の詳細を図6
に示し、第2のファジィルールテーブル12の詳細を図
7に示す。
PB, PM, P of each membership function
The meanings of the symbols S, Z, NS, NM and NB are shown in FIG.
The details of the first fuzzy rule table 11 are shown in FIG.
The details of the second fuzzy rule table 12 are shown in FIG.

【0025】図6の第1のファジィルールテーブル11
及び図7の第2のファジィルールテーブル12は、配水
の需要量、即ち吐出流量の多い昼間の場合には、速い制
御応答がえられ、配水の需要量の少ない夜間の場合に
は、ゆっくりとした制御応答が得られるように設計して
いる。例えば、図3に示したように配水端末圧力が変動
した例では、時刻t で配水末端圧力が設定値より小さく
なっており、吐出流量Qpv(t)が多い(配水需要が多い)
ので、図5から分かるように、配水末端圧力偏差の状態
はPBであり、配水ポンプの吐出流量の状態はPBであ
る。従って、図6に示す第1のファジィルールテーブル
11から分かるように、吐出圧力目標値の第1の修正量
はPBの状態でなければならないにことになり、吐出圧
力目標値の第1の修正量を正で大きくするとのファジィ
推論結果が出る。つまり、図6の第1のファジィルール
テーブル11のルールR1が発火する。
The first fuzzy rule table 11 shown in FIG.
The second fuzzy rule table 12 of FIG. 7 shows that a fast control response can be obtained in the daytime when the demand of water distribution is large, that is, in the daytime when the discharge flow rate is large, and it can be slowly controlled in the nighttime when the demand of water distribution is small. It is designed to obtain the controlled response. For example, in the example where the water distribution terminal pressure fluctuates as shown in FIG. 3, the water distribution end pressure becomes smaller than the set value at time t, and the discharge flow rate Qpv (t) is large (the water distribution demand is large).
Therefore, as can be seen from FIG. 5, the state of the water distribution end pressure deviation is PB, and the state of the discharge flow rate of the water distribution pump is PB. Therefore, as can be seen from the first fuzzy rule table 11 shown in FIG. 6, the first correction amount of the discharge pressure target value must be in the PB state, and the first correction of the discharge pressure target value is performed. A fuzzy inference result that the amount is positive and large is obtained. That is, the rule R1 of the first fuzzy rule table 11 in FIG. 6 is fired.

【0026】同様に、配水末端圧力偏差の変化率は負で
大きくなる。つまり、配水末端圧力が急激に下がってい
る状態であるので、このとき、第2のファジィルールテ
ーブル12で吐出圧力目標値の修正量を正で大きくする
とのファジィ推論結果が出る。つまり、図7の第2のル
ールテーブル12のルールR1が発火する。従って、ファ
ジィ推論では、吐出圧力目標値の第2の修正量が正で大
きくなるよう推論する。
Similarly, the rate of change of pressure deviation at the water distribution end is negative and large. That is, since the water distribution end pressure is rapidly decreasing, a fuzzy inference result that the correction amount of the discharge pressure target value in the second fuzzy rule table 12 is increased by a positive value is obtained at this time. That is, the rule R1 of the second rule table 12 of FIG. 7 is fired. Therefore, in the fuzzy inference, it is inferred that the second correction amount of the discharge pressure target value is positive and large.

【0027】以上のファジィ推論により求められたファ
ジィ推論値を基に、修正された吐出圧力目標値hsv(t)、
その際の第1の修正量dh1(t)及び第2の修正量dh2(t)
は、次式で示される。
Based on the fuzzy inference value obtained by the above fuzzy inference, the corrected discharge pressure target value hsv (t),
The first correction amount dh1 (t) and the second correction amount dh2 (t) at that time
Is expressed by the following equation.

【0028】 hsv(t)=hsv(t-dt)+K1*dh1(t)+K2*dh2(t) …(10) dh1(t)=[Hinf1]*dhmax1 …(11) dh2(t)=[Hinf2]*dhmax2 …(12) ここで、 hsv(t): 吐出圧力目標値[mAq] dh1(t): 吐出圧力目標値の第1の修正量[mAq] dh2(t): 吐出圧力目標値の第2の修正量[mAq] dhmax1: 吐出圧力目標値の修正量幅1[mAq] dhmax2: 吐出圧力目標値の修正量幅2[mAq] K1: 吐出圧力目標値の第1の修正量のゲイン K2: 吐出圧力目標値の第2の修正量のゲイン dt: 制御周期 [Hinf1]:ファジィ推論値(吐出圧力目標値の第1の修正
量の正規化値) [Hinf2]:ファジィ推論値(吐出圧力目標値の第2の修正
量の正規化値) (10)式において、吐出圧力目標値の第1の修正量のゲイ
ンK1、及び吐出圧力目標値の第2の修正量のゲインK2
を、適宜必要に応じて設定することができるので、第1
の修正量及び第2の修正量に重み付けをすることができ
る。
Hsv (t) = hsv (t-dt) + K1 * dh1 (t) + K2 * dh2 (t) (10) dh1 (t) = [Hinf1] * dhmax1 (11) dh2 (t) = [Hinf2] * dhmax2… (12) where hsv (t): Target discharge pressure value [mAq] dh1 (t): 1st correction amount of target discharge pressure value [mAq] dh2 (t): Discharge pressure Second correction amount of target value [mAq] dhmax1: Range of correction amount of discharge pressure target value 1 [mAq] dhmax2: Range of correction amount of discharge pressure target value 2 [mAq] K1: First correction of discharge pressure target value Volume gain K2: Gain of second correction amount of discharge pressure target value dt: Control cycle [Hinf1]: Fuzzy inference value (Normalized value of first correction amount of discharge pressure target value) [Hinf2]: Fuzzy inference Value (normalized value of the second correction amount of the discharge pressure target value) In the equation (10), the gain K1 of the first correction amount of the discharge pressure target value and the gain of the second correction amount of the discharge pressure target value K2
Can be set as needed according to the necessity.
Can be weighted.

【0029】このように、この実施例では、吐出圧力目
標値演算手段9は、ヒューマンインタフェイス6からの
配水末端圧力設定値と配水末端圧力計5からの検出値で
ある配水末端圧力との配水末端圧力偏差を求め、この配
水末端圧力偏差と吐出流量計4からの吐出流量との組合
せから、第1のファジィルールテーブル11を用いてフ
ァジィ推論値を求める。さらに、吐出圧力目標値演算手
段9は、配水末端圧力偏差の変化率を求め、この配水末
端圧力偏差の変化率と吐出流量計4からの吐出流量との
組合せから、第2のファジィルールテーブル12を用い
てファジィ推論値を求める。
As described above, in this embodiment, the discharge pressure target value computing means 9 distributes the distribution end pressure set value from the human interface 6 and the distribution end pressure which is the detection value from the distribution end pressure gauge 5. The end pressure deviation is obtained, and the fuzzy inference value is obtained using the first fuzzy rule table 11 from the combination of the distribution end pressure deviation and the discharge flow rate from the discharge flow meter 4. Further, the discharge pressure target value calculation means 9 obtains the change rate of the water distribution end pressure deviation, and from the combination of the change rate of the water distribution end pressure deviation and the discharge flow rate from the discharge flow meter 4, the second fuzzy rule table 12 is obtained. Is used to find the fuzzy inference value.

【0030】そして、第1のファジィルールテーブル1
1から得られたファジィルール推論値に基づいて得られ
た吐出圧力目標値の第1の修正量と、第2のファジィル
ールテーブル12から得られたファジィ推論値に基づい
て得られた吐出圧力目標値の第2の修正量との和によっ
て吐出圧力目標値の修正量を演算し、推論周期ごとに吐
出圧力目標値を修正する。配水ポンプ回転数制御手段1
0は、このように修正された吐出圧力目標値と吐出圧力
計3からの吐出圧力検出値との偏差がゼロになるように
配水ポンプP1〜Pn の回転数をフィードバック制御す
る。
Then, the first fuzzy rule table 1
The first correction amount of the discharge pressure target value obtained based on the fuzzy rule inference value obtained from 1 and the discharge pressure target obtained based on the fuzzy inference value obtained from the second fuzzy rule table 12 The correction amount of the discharge pressure target value is calculated by the sum of the value and the second correction amount, and the discharge pressure target value is corrected every inference cycle. Distribution pump rotation speed control means 1
0 controls the number of rotations of the water distribution pumps P1 to Pn in a feedback manner so that the deviation between the discharge pressure target value corrected in this way and the discharge pressure detection value from the discharge pressure gauge 3 becomes zero.

【0031】ここで、第1の修正量のゲインK1をK1=1、
第2の修正量2のゲインK2をK2=0とすると、第1のファ
ジィルールテーブル11による第1の修正量が吐出圧力
目標値の修正量となり、請求項1に記載の発明と等価と
なる。即ち、第2のファジィルールテーブル12を削除
したものとなる。また、第1の修正量のゲインK1をK1=
0.5、第2の修正量2のゲインK2をK2=0.5とすると、第
1のファジィルールテーブル11による第1の修正量
と、第2のファジィルールテーブル12による第2の修
正量との重みが均等な吐出圧力目標値の修正量となり、
請求項2に記載の発明と等価となる。そして、第1の修
正量のゲインK1、第2の修正量2のゲインK2を必要に応
じて、任意に重みを付けて設定すると、請求項3の発明
となる。
Here, the gain K1 of the first correction amount is K1 = 1,
When the gain K2 of the second correction amount 2 is set to K2 = 0, the first correction amount by the first fuzzy rule table 11 becomes the correction amount of the discharge pressure target value, which is equivalent to the invention according to claim 1. . That is, the second fuzzy rule table 12 is deleted. Also, the gain K1 of the first correction amount is set to K1 =
If the gain K2 of 0.5 and the second correction amount 2 is K2 = 0.5, the weight of the first correction amount by the first fuzzy rule table 11 and the second correction amount by the second fuzzy rule table 12 becomes It is an even correction amount of the discharge pressure target value,
It is equivalent to the invention described in claim 2. Then, the gain K1 of the first correction amount and the gain K2 of the second correction amount 2 are arbitrarily weighted and set as needed, whereby the invention of claim 3 is obtained.

【0032】[0032]

【発明の効果】以上のように、本発明によれば、吐出流
量及び配水末端圧力を検出し、吐出流量と配水末端圧力
偏差とを入力とするファジィルールテーブルによって吐
出圧力目標値の修正量を演算し、推論周期ごとに吐出圧
力目標値を修正し得るようにしたので、配水末端圧力の
一定制御を行なうにあたり、所望の値の配水末端圧力を
需要量に応じて所望の応答で制御することができる。
As described above, according to the present invention, the discharge flow rate and the water distribution end pressure are detected, and the amount of correction of the discharge pressure target value is determined by the fuzzy rule table which inputs the discharge flow rate and the water distribution end pressure deviation. Since the target value of discharge pressure can be corrected for each inference cycle by calculation, in order to perform constant control of the water distribution end pressure, it is necessary to control the water distribution end pressure of a desired value with a desired response according to the demand amount. You can

【0033】さらに、吐出流量と配水末端圧力偏差とを
入力とする第1のファジィルールテーブルと、吐出流量
と配水末端圧力偏差の変化率とを入力とする第2のファ
ジィルールテーブルとからのそれぞれのファジィ演算出
力の和によって吐出圧力目標値の修正量を演算すること
で、より精度の高い制御を行なうことができる。
Further, the first fuzzy rule table having the discharge flow rate and the water distribution end pressure deviation as input and the second fuzzy rule table having the discharge flow rate and the change rate of the water distribution end pressure deviation as the input respectively. By calculating the correction amount of the target value of the discharge pressure based on the sum of the fuzzy calculation outputs of, the control with higher accuracy can be performed.

【0034】また、これらの修正量にそれぞれ所定のゲ
インを乗じることができるので、重み付けをすることが
できるので、幅広い制御が可能となる。
Further, since these correction amounts can be respectively multiplied by a predetermined gain, weighting can be performed, so that a wide range of control is possible.

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

【図1】発明の実施例を示すブロック構成図。FIG. 1 is a block diagram showing an embodiment of the invention.

【図2】図1における第1のファジィルールテーブルと
第2のファジィルールテーブルの間の関係を示す説明
図。
FIG. 2 is an explanatory diagram showing a relationship between a first fuzzy rule table and a second fuzzy rule table in FIG.

【図3】配水末端圧力及び吐出流量の特性例を示す特性
図。
FIG. 3 is a characteristic diagram showing a characteristic example of a water distribution end pressure and a discharge flow rate.

【図4】本発明の吐出圧力目標値演算手段でのファジィ
演算の際に用いるメンバーシップ関数を示す説明図。
FIG. 4 is an explanatory diagram showing a membership function used in fuzzy calculation by the discharge pressure target value calculation means of the present invention.

【図5】本発明のメンバーシップ関数における記号の意
味を表した説明図。
FIG. 5 is an explanatory diagram showing the meaning of symbols in the membership function of the present invention.

【図6】本発明における第1のファジィルールテーブル
の説明図。
FIG. 6 is an explanatory diagram of a first fuzzy rule table according to the present invention.

【図7】本発明における第2のファジィルールテーブル
の説明図
FIG. 7 is an explanatory diagram of a second fuzzy rule table according to the present invention.

【符号の説明】[Explanation of symbols]

1 配水池 2 配水管網 3 吐出圧力計 4 吐出流量計 5 配水末端圧力計 6 ヒューマンインタフェイス 7 CRT表示装置 8 演算装置 9 吐出圧力目標値演算手段 10 配水ポンプ回転数制御手段 11 第1のファジィルールテーブル 12 第2のファジィルールテーブル P1 〜Pn 配水ポンプ 1 Reservoir 2 Water distribution network 3 Discharge pressure gauge 4 Discharge flowmeter 5 Water distribution end pressure gauge 6 Human interface 7 CRT display device 8 Calculation device 9 Discharge pressure target value calculation means 10 Water distribution pump rotation speed control means 11 First fuzzy Rule table 12 Second fuzzy rule table P1 to Pn Water distribution pump

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 G05D 27/02 G05D 27/02 29/00 29/00 (72)発明者 新山 雅永 東京都府中市東芝町1番地 株式会社東芝 府中工場内 (72)発明者 芦木 達雄 東京都港区芝浦一丁目1番1号 株式会社 東芝本社事務所内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Reference number within the agency FI Technical display location G05D 27/02 G05D 27/02 29/00 29/00 (72) Inventor Masanaga Niiyama Tokyo Fuchu Toshiba Town Fuchu Factory, Toshiba Corporation (72) Inventor Tatsuo Ashiki 1-1-1 Shibaura, Minato-ku, Tokyo Inside Toshiba Head Office

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 配水池の浄水が配水ポンプにより配水管
網に供給され、前記浄水の需要量の変動に対して前記配
水ポンプの吐出圧力がその吐出圧力目標値になるように
制御することにより、前記配水管網の配水末端圧力を一
定に制御するようにした配水末端圧力制御装置におい
て、前記配水末端圧力とその配水末端圧力設定値との偏
差及び前記配水ポンプの吐出流量に基づいてファジィ推
論により前記配水ポンプの吐出圧力目標値の修正量を算
出しこの修正量に基づいて前記吐出圧力目標値を修正す
る吐出圧力目標値演算手段と、前記配水ポンプの吐出圧
力が前記吐出圧力目標値演算手段で修正された吐出圧力
目標値になるように前記配水ポンプの回転数を制御する
配水ポンプ回転数制御手段とを備えたことを特徴とする
配水末端圧力制御装置。
1. The purified water in a distribution reservoir is supplied to a distribution pipe network by a distribution pump, and the discharge pressure of the distribution pump is controlled to reach its discharge pressure target value in response to fluctuations in the demand for the purified water. In a water distribution terminal pressure control device for controlling the water distribution terminal pressure of the water distribution network at a constant level, fuzzy inference based on a deviation between the water distribution terminal pressure and a set value of the water distribution terminal pressure and a discharge flow rate of the water distribution pump. And a discharge pressure target value calculating means for calculating a correction amount of the discharge pressure target value of the water distribution pump and correcting the discharge pressure target value based on the correction amount, and calculating the discharge pressure target value of the discharge pressure of the water distribution pump. Water distribution pump rotation speed control means for controlling the rotation speed of the water distribution pump so that the discharge pressure target value corrected by the means is provided. .
【請求項2】 前記吐出圧力目標値演算手段は、前記配
水末端圧力とその配水末端圧力設定値との偏差及び前記
配水ポンプの吐出流量に基づいてファジィ推論により得
た第1の修正量と、前記配水末端圧力とその配水末端圧
力設定値との偏差の変化率及び前記配水ポンプの吐出流
量に基づいてファジィ推論により得た第2の修正量との
双方に基づいて、前記吐出圧力目標値を修正するように
したことを特徴とする請求項1に記載の配水末端圧力制
御装置。
2. A first correction amount obtained by fuzzy inference based on a deviation between the water distribution end pressure and a set value of the water distribution end pressure and the discharge flow rate of the water distribution pump, the discharge pressure target value calculating means; Based on both the rate of change of the deviation between the water distribution end pressure and the set value of the water distribution end pressure and the second correction amount obtained by fuzzy inference based on the discharge flow rate of the water distribution pump, the discharge pressure target value is calculated. The water distribution end pressure control device according to claim 1, wherein the water distribution end pressure control device is modified.
【請求項3】 前記吐出圧力目標値演算手段は、前記第
1の修正量及び前記第2の修正量に、それぞれ所定のゲ
インを乗じるようにしたことを特徴とする請求項2に記
載の配水末端圧力制御装置。
3. The water distribution according to claim 2, wherein the discharge pressure target value calculation means is configured to multiply the first correction amount and the second correction amount by predetermined gains, respectively. Terminal pressure control device.
JP20027395A 1995-07-14 1995-07-14 Water distribution terminal pressure controller Pending JPH0934557A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20027395A JPH0934557A (en) 1995-07-14 1995-07-14 Water distribution terminal pressure controller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20027395A JPH0934557A (en) 1995-07-14 1995-07-14 Water distribution terminal pressure controller

Publications (1)

Publication Number Publication Date
JPH0934557A true JPH0934557A (en) 1997-02-07

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP20027395A Pending JPH0934557A (en) 1995-07-14 1995-07-14 Water distribution terminal pressure controller

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JP (1) JPH0934557A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103529695A (en) * 2013-10-08 2014-01-22 郭景礼 Variable-frequency speed regulation water supply system based on day parting intelligent PID (proportion integration differentiation) regulator
CN114442710A (en) * 2022-01-24 2022-05-06 中冶长天国际工程有限责任公司 Water supply control system and method for material mixing and pelletizing process and storage medium

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103529695A (en) * 2013-10-08 2014-01-22 郭景礼 Variable-frequency speed regulation water supply system based on day parting intelligent PID (proportion integration differentiation) regulator
CN114442710A (en) * 2022-01-24 2022-05-06 中冶长天国际工程有限责任公司 Water supply control system and method for material mixing and pelletizing process and storage medium
CN114442710B (en) * 2022-01-24 2023-02-28 中冶长天国际工程有限责任公司 Water supply control system and method for material mixing and pelletizing process and storage medium

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