JPS60687B2 - How to adjust the water level in a tunnel - Google Patents
How to adjust the water level in a tunnelInfo
- Publication number
- JPS60687B2 JPS60687B2 JP13998575A JP13998575A JPS60687B2 JP S60687 B2 JPS60687 B2 JP S60687B2 JP 13998575 A JP13998575 A JP 13998575A JP 13998575 A JP13998575 A JP 13998575A JP S60687 B2 JPS60687 B2 JP S60687B2
- Authority
- JP
- Japan
- Prior art keywords
- water level
- amount
- flow rate
- tunnel
- water
- 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
Links
Landscapes
- Barrages (AREA)
- Feedback Control In General (AREA)
- Control Of Non-Electrical Variables (AREA)
Description
【発明の詳細な説明】
本発明は上下水道設備におけるずし、道吐出槽の水位を
制御するずし、道の水位調整方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water level adjustment method for controlling the water level of a water discharge tank in water supply and sewage facilities.
従来上下水道設備におけるずし、道の水位制御は吐出槽
の水位をアナログ調節計に入力し、予め設定された目標
水位との偏差よりPm演算(D動作は無い場合もある。
)を行ないずし、道への流入量を制御する流入弁の開度
を制御するようにしている。ところが、かかる水位制御
では吐出槽水位による貯水表面積の変化につまり貯水量
と水位の間の非線形要素および流入弁開度と流入量の間
の非線形要素等が考慮されず、したがってその制御定数
はこれらの非線形要素が最悪の場合でも系が安定である
よう制御されていた。Conventional water level control in water and sewage facilities involves inputting the water level of the discharge tank into an analog controller, and calculating Pm based on the deviation from a preset target water level (in some cases, there is no D operation).
), and the opening degree of the inflow valve that controls the amount of inflow into the road is controlled. However, such water level control does not take into account nonlinear elements between the water storage amount and water level, nonlinear elements between the inflow valve opening degree and the inflow amount, etc. in changes in the storage surface area due to the discharge tank water level, and therefore, the control constants are The system was controlled to be stable even in the worst case of nonlinear elements.
このため系の反応はかなり遅くなりすし、道の吐出槽の
容積が小さい場合又はずし、道がかなり長く導水時間遅
れが長い場合には制御不可能になることがあった。従っ
て、このように制御不可能の場合には人間が吐出塁の変
化を予想して流入弁の関度を調整するなどしており安定
した制御ができなかった。また電子計算機を使用した場
合にも前記PID調整計内部で行なっている演算を計算
機内部で行なうだけであり上述と同様の欠点は依然とし
てあった。As a result, the reaction of the system becomes quite slow, and control may become uncontrollable when the volume of the discharge tank in the road is small, or when the road is quite long and the water introduction time delay is long. Therefore, in such a case where control is impossible, stable control cannot be achieved because a person has to predict changes in the discharge base and adjust the inlet valve. Further, even when an electronic computer is used, the calculations performed inside the PID adjuster are simply performed inside the computer, and the same drawbacks as described above still exist.
本発明は上記事情に鑑みてなされたもので、すし、道吐
出槽の水位制御を応答よく且つ安定して行なうことがで
きるずい道の水位調整方法を提供することを目的とする
。The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a method for adjusting the water level of a sushi canal that can control the water level of a sushi tank with good response and stability.
以下、本発明の一実施例を第1図a,b乃至第4図に従
い説明する。An embodiment of the present invention will be described below with reference to FIGS. 1a, b to 4.
即ち、第1図aにおいて、1はずし・道で、このずい道
1はその断面を同図bに示すよう馬蹄形にしている。ま
たずし、道1には吐出槽2が設けられている。3は前記
ずし、道1への流入量を制御する流量調整弁で、この流
量調整弁3は後述の演算制御装置6により制御される駆
動モータ4によってその弁開度が制御される。That is, in FIG. 1a, the channel 1 has a horseshoe-shaped cross section as shown in FIG. 1b. In addition, a discharge tank 2 is provided in the sushi road 1. Reference numeral 3 denotes a flow rate regulating valve for controlling the amount of flow into the stream 1, and the opening degree of this flow rate regulating valve 3 is controlled by a drive motor 4 controlled by an arithmetic and control device 6, which will be described later.
5は前記吐出槽2内の現在水位を測定するための水位計
でこの水位計5の出力は後述の演算制御装置6に入力さ
れる。ここで前記吐出槽2内の水位は上限水位をHWL
、下限水位をLWLおよび目標水位をLspで示してい
る。一方、6は前記水位計5の出力が与えられる演算制
御装置で、この演算制御装置6は予め第2図の如き吐出
槽水位Lと吐出槽内貯蔵水量Vの関係を表わす曲線、第
3図の如き流量調節弁関度0と流入量Fの関係を表わす
特性曲線および第4図の如きずし・道流入量Fとずし、
道導水遅れ時間tの関係を表わす曲線を夫々高次関数又
は折線近似として記憶しておき、これらの曲線と後述の
演算により流量調節弁3の開度修正量を求め、前後駆動
モータ4にその修正量を出力するようにしている。Reference numeral 5 denotes a water level gauge for measuring the current water level in the discharge tank 2, and the output of this water level gauge 5 is input to an arithmetic and control unit 6, which will be described later. Here, the water level in the discharge tank 2 is set to the upper limit water level HWL.
, the lower limit water level is indicated by LWL, and the target water level is indicated by Lsp. On the other hand, numeral 6 denotes an arithmetic and control device to which the output of the water level gauge 5 is given, and this arithmetic and control device 6 has a curve representing the relationship between the water level L of the discharge tank and the amount of water stored in the discharge tank V as shown in FIG. 2, as shown in FIG. A characteristic curve representing the relationship between the flow rate regulating valve function 0 and the inflow amount F as shown in FIG.
The curves representing the relationship between the road water conveyance delay time t are stored as high-order functions or polygonal line approximations, and the amount of opening correction of the flow rate control valve 3 is determined by using these curves and calculations described later. I am trying to output the amount of correction.
つまり、この場合の演算制御装置6は吐出槽2の現在水
位をLpvとしたとき第2図の曲線より現在貯水量Vp
vを求め、一方予め記憶されている吐出槽2の目標水位
Lspより同機に第2図の曲線から目標貯水量Vspを
求める。そして、これらVpv、Vspによる貯水量偏
差より下式からずし、道流入量の修正量△Fを求める。
△F=K{(en−en‐・)+T台n+字〈en−肌
,十en‐2)},..,.en:貯水量偏差(=Vs
p−Vpv)en‐,:同上の前回制御周期時の値
en‐2:同上の前々回制御周期時の値
7:制御周期
K:比例定数
TI:積分時間
TD:微分時間
ここで、一般にすし、道内の流速はマニングの公式およ
びバザーンの公式等から求められるが、上述した第1図
bに示すような馬蹄形のずし、道ではずし・道内流量F
とずし、道内導水遅れ時間tの関係が第4図の如き曲線
になることから流入量Fが変化した場合導水遅れ時間t
が変化することになり水位制御系の無駄時間が変化する
ため{1’式における比例定数Kを下式により修正する
。In other words, in this case, the arithmetic and control device 6 calculates the current water storage amount Vp from the curve of FIG. 2 when the current water level of the discharge tank 2 is Lpv.
On the other hand, from the pre-stored target water level Lsp of the discharge tank 2, the target water storage amount Vsp is determined from the curve shown in FIG. Then, from the water storage amount deviation due to these Vpv and Vsp, the correction amount ΔF of the road inflow amount is obtained by subtracting from the following equation.
△F=K{(en-en-・)+T unit n+character〈en-skin, ten en-2)},. .. 、. en: Water storage amount deviation (=Vs
p-Vpv)en-,: Value at the previous control cycle as above en-2: Value at the time before the previous control cycle as above 7: Control cycle K: Proportionality constant TI: Integral time TD: Derivative time Here, generally, The flow velocity in Hokkaido can be found from Manning's formula, Bazahn's formula, etc., but the flow velocity in Hokkaido is determined by the horseshoe-shaped drop, the drop in the road, and the flow rate F in Hokkaido as shown in Figure 1b above.
Since the relationship between the prefecture water introduction delay time t becomes a curve as shown in Figure 4, when the inflow amount F changes, the water introduction delay time t
As a result, the dead time of the water level control system changes, so the proportionality constant K in equation {1' is corrected by the following equation.
K=f(t) ……■
t:ずし、道内導水遅れ時間
f(t):一般に単調減少関数
次いで‘1’式で求めたずし、道流入量の修正量△Fよ
り第3図の特性曲線から流量調節弁開度修正量△めを求
めるが、まず現在流量調節関度でpvより第3図の曲線
から現在流入量Fpvを求め、上記修正量△Fを用いて
Fpv+△Fを演算し、この流入量Fpv十△Fのとき
流量調節弁関度◇を同様に第3図の曲線から求め、最後
に下式から流量調節弁開度修正量△0を求める。K=f(t) ……■ t: Water introduction delay time f(t): Generally a monotonically decreasing function, then calculated using the '1' formula. The flow rate control valve opening correction amount △ is determined from the characteristic curve of . First, the current inflow amount Fpv is determined from the curve in Figure 3 using the current flow rate control function pv, and using the above correction amount △F, Fpv + △F When the inflow amount Fpv is 10ΔF, the flow rate regulating valve function ◇ is similarly determined from the curve in FIG. 3, and finally the flow rate regulating valve opening correction amount Δ0 is determined from the following equation.
△少=○PV−中 ……{3}そして
{3’式より求められた流量調節弁開度修正量△めを前
記駆動モー夕4に出力し、流量調節弁3の弁開度を制御
するようにしている。△Low = ○PV-Medium...{3} Then, the flow rate control valve opening correction amount △ obtained from the formula {3' is outputted to the drive motor 4 to control the valve opening of the flow rate control valve 3. I try to do that.
次に以上のように構成した本発明の作用を述べると、い
まずし、道1の吐出槽2の現在水位をLpvとすると、
この水位Lpvが水位計5の出力として演算制御装置6
に与えられる。Next, to describe the operation of the present invention configured as above, let us say that the current water level of the discharge tank 2 of the road 1 is Lpv.
This water level Lpv is used as the output of the water level gauge 5 by the arithmetic and control unit 6.
given to.
すると演算制御装置6にて現在水位Lpvから第2図の
曲線より現在貯水量Vpvが求められ、次いで予め記憶
されている目標水位Lspから第2図の曲線より目標貯
水量Vspが求められ、これらVpv、Vspによる貯
水量偏差から(1}式よりずし、道流入量の修正量△F
が求められる。この場合前記ずし、道1はその断面を第
1図bに示すよう馬蹄形にしており、ずし、道1内の流
量Fとずし、道1内導水遅れ時間tの関係が第4図のよ
うになることから{1ー式における比例定数Kが(2}
式により修正される。Then, the arithmetic and control unit 6 calculates the current water storage amount Vpv from the curve shown in FIG. 2 from the current water level Lpv, and then calculates the target water storage amount Vsp from the curve shown in FIG. 2 from the previously stored target water level Lsp. From the water storage amount deviation due to Vpv and Vsp, the correction amount of road inflow △F is removed from equation (1).
is required. In this case, the cross section of the road 1 has a horseshoe shape as shown in Fig. 1b, and the relationship between the flow rate F in the road 1 and the water introduction delay time t in the road 1 is shown in Fig. 4. Since it becomes as follows, the proportionality constant K in the equation {1- is (2}
Modified by Eq.
そして、{1)式より求められた修正量△Fから第3図
の特性曲線より流量調節弁3の開度修正量△◇が求めら
れるが、まず現在流量調節弁開度◇pvより第3図の曲
線から現在流入量Fpvが求められ、上記修正量△Fを
用いてFpv+△Fが演算され、次いでこの流入量Fp
v+△Fより第3図の曲線から流量調節弁開度0が求め
られ最後に制式から流量調節弁閥度修正量△中が求めら
れる。Then, the opening correction amount △◇ of the flow rate control valve 3 is determined from the correction amount △F obtained from equation {1) and the characteristic curve in FIG. The current inflow amount Fpv is obtained from the curve in the figure, Fpv+△F is calculated using the above correction amount △F, and then this inflow amount Fp
From v+ΔF, the flow rate regulating valve opening degree 0 is determined from the curve in FIG. 3, and finally, the flow rate regulating valve opening degree correction amount Δmedium is determined from the control formula.
従ってこの修正量△0‘こ応じた出力が演算制御装置6
により駆動モータ4に与えられ流量調整弁3の弁開度が
制御され、これにより吐出槽2の水位は予め設定される
目標水位Lspに向け制御されることになる。しかして
、かような構成によると、制御の基本計算は【1)式に
より貯水量偏差のみを使って計算しており任意の目標水
位に対し制御定数の調整をすることがないので応答のよ
い制御を行なうことができる。Therefore, the output corresponding to this correction amount △0' is the output from the arithmetic and control unit 6.
This is applied to the drive motor 4 to control the valve opening of the flow rate regulating valve 3, thereby controlling the water level in the discharge tank 2 toward a preset target water level Lsp. According to such a configuration, the basic control calculation is performed using only the water storage amount deviation according to equation [1], and there is no need to adjust the control constants for any target water level, resulting in a good response. can be controlled.
またずし、道内流量による導水遅れ時間の変化を予め考
慮して制御式のゲインを自動調整していることにより任
意の流入量に対し制御定数の調整を行なうことなく応答
のよい制御を行なうことができる。更に流入量修正量を
流量調節弁関度修正量に変換する際弁の特性曲線を利用
しているので任意の弁関度において応答のよい制御を行
なうことができる。従って全ての条件のもとで同一特性
の最も応答のよい所謂適応制御をもってずし、道吐出槽
の水位制御を安定して行なうことができる。尚、上述の
実施例における【1}式は一般のDDC用制御計算を基
本としているが、本発明は貯水量偏差を使用して制御計
算を行なっていることが特徴であり、他の種々の制御計
算式を【1)式の代わりに使用する場合でも水位偏差の
代わりに貯水量偏差を使用することにより同様の効果を
あげることができる。In addition, the gain of the control formula is automatically adjusted by taking into consideration changes in the water introduction delay time due to the flow rate in Hokkaido, so responsive control can be performed without having to adjust control constants for any inflow amount. Can be done. Furthermore, since the characteristic curve of the valve is utilized when converting the inflow amount correction amount into the flow rate regulating valve function correction amount, responsive control can be performed at any valve function. Therefore, the water level in the road discharge tank can be stably controlled without using so-called adaptive control which has the same characteristics and provides the best response under all conditions. Note that formula [1} in the above embodiment is based on general DDC control calculation, but the present invention is characterized in that control calculation is performed using the water storage amount deviation, and various other methods can be used. Even when the control calculation formula is used in place of formula (1), the same effect can be achieved by using the water storage amount deviation instead of the water level deviation.
また、ずし、道内導水遅れ時間により制御計算式のゲイ
ンを自動修正していること、および流入量修正量と流量
調節弁の特性を考慮して弁開度修正量を得る等の特徴を
備えているが、これらのうちのいくつかのみを利用する
場合でも従来技術に比してかなりの効果を期待すること
もできる。更に上述した実施例では演算制御装置を使用
しているが、一般の関数発生器およびアナログ調整計等
を組合せて本装贋を構成することも可能である。更に又
、上述した実施例では簡単のためテレメータ/テレコン
トロール装置を設けていないが、ずし、道流量調節弁と
吐出槽の場所が離れている場合には当然テレメータノテ
レコントロール装置を使用して構成されることになる。In addition, the gain of the control calculation formula is automatically corrected based on the prefecture water introduction delay time, and the valve opening correction amount is obtained by taking into account the inflow amount correction amount and the characteristics of the flow rate control valve. However, even if only some of these are used, considerable effects can be expected compared to the conventional techniques. Furthermore, although an arithmetic and control unit is used in the above-described embodiment, it is also possible to construct the present system by combining a general function generator, an analog regulator, etc. Furthermore, in the above embodiment, a telemeter/telecontrol device is not provided for simplicity, but if the flow rate control valve and discharge tank are located far apart, a telemeter/telecontrol device can of course be used. It will be configured.
その他本発明は上記し且つ図面に示す実施例にのみ限定
されず要旨を変更しない範囲で適宜変形して実施し得る
ことは勿論である。In addition, it goes without saying that the present invention is not limited to the embodiments described above and shown in the drawings, but can be implemented with appropriate modifications without changing the gist.
第1図a,bは本発明によろずい道の水位調整方法の一
実施例を示し第1図aは本方法を実施する装置の構成図
、第1図bは第1図aのX−X′面におけるずし、道の
断面図、第2図乃至第4図は同実施例に適用される演算
制御装置の記憶曲線を示し、第2図は吐出槽水位Lと吐
出槽内貯水量Vの関係を表す曲線図、第3図は流量調節
弁開度0と流入量Fの関係を表す曲線図、第4図は流入
量Fとずし、道導水遅れ時間tの関係を表す曲線図であ
る。
1・・・・・・ずし、道、2・・・・・・吐出槽、3・
・・・・‘流量調節弁、4・・・・・・モータ、5・・
…・水位計、6・・・・・・演算制御装置。
メナM
メク@
メゾ■
メク蛾1a and 1b show an embodiment of the method for adjusting the water level in a waterway according to the present invention, FIG. 1a is a block diagram of an apparatus for implementing the method, and FIG. 1b is a 2 to 4 show the memory curves of the arithmetic and control unit applied to the same embodiment, and FIG. 2 shows the discharge tank water level L and the amount of water stored in the discharge tank. Figure 3 is a curve diagram representing the relationship between the flow rate control valve opening degree 0 and the inflow amount F, and Figure 4 is a curve diagram representing the relationship between the inflow amount F and the water transfer delay time t. It is a diagram. 1... Sushi, road, 2... Discharge tank, 3.
...'Flow control valve, 4...Motor, 5...
...・Water level gauge, 6.... Arithmetic control device. Mena M Meku @ Mezo ■ Meku moth
Claims (1)
槽の水位を調整する方法において、あらかじめ吐出槽水
位と吐出槽内貯水量の関係を表わす第1の曲線、ずい道
流入量調節弁開度とずい道流入量の関係を表わす第2の
曲線、ずい道流入量とずい道導水遅れ時間の関係を表わ
す第3の曲線およびずい道流入量の修正量ΔFを求める
演算式ΔF=K{(en−en_−_1)+τ/(Τ_
I)en+(ΤD)/τ(en−2en_−_1+en
_−_2)}但しen:貯水量偏差 en_−_1:同上の前回制御周期時の値en_−_2
:同上の前々回制御周期時の値τ:制御周期K:比例定
数 Τ_I:積分時間 T_D:微分時間 を知り、前記吐出槽の現在水位と目標水位から第1の曲
線を用い貯水量偏差を求め、これを上式に用いるととも
にずい道内流量による導水遅れ時間の変化を第3の曲線
より考慮して上式の比例定数を調整しつつずい道流入量
の修正量ΔFを演算し、この修正量ΔFと前記流量調節
弁の現在開度から前記第2の曲線を用い前記流量調節弁
の弁開度を制御するようにしたずい道の水位調整方法。[Claims] 1. In a method of adjusting the water level of a channel discharge tank by operating a channel flow rate regulating valve, a first curve representing the relationship between the discharge tank water level and the amount of water stored in the discharge tank is defined in advance. A second curve representing the relationship between the opening degree of the inflow control valve and the tunnel inflow amount, a third curve representing the relationship between the tunnel inflow amount and the tunnel water introduction delay time, and calculation for calculating the correction amount ΔF of the tunnel inflow amount. Formula ΔF=K{(en-en_-_1)+τ/(Τ_
I) en+(TD)/τ(en-2en_-_1+en
____2)} However, en: Water storage amount deviation en_-_1: Value at the previous control cycle same as above en_-_2
: Value τ at the time of the control cycle before the previous same as above: Control cycle K: Proportionality constant T_I: Integral time T_D: Derivative time, find the water storage amount deviation from the current water level and target water level of the discharge tank using the first curve, Using this in the above formula and taking into account the change in water introduction delay time due to the flow rate in the tunnel from the third curve, calculating the correction amount ΔF of the tunnel inflow amount while adjusting the proportionality constant in the above formula, and calculating the correction amount ΔF and a method for adjusting the water level of a channel, wherein the opening degree of the flow rate regulating valve is controlled using the second curve based on the current opening degree of the flow rate regulating valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13998575A JPS60687B2 (en) | 1975-11-21 | 1975-11-21 | How to adjust the water level in a tunnel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13998575A JPS60687B2 (en) | 1975-11-21 | 1975-11-21 | How to adjust the water level in a tunnel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5264145A JPS5264145A (en) | 1977-05-27 |
| JPS60687B2 true JPS60687B2 (en) | 1985-01-09 |
Family
ID=15258246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13998575A Expired JPS60687B2 (en) | 1975-11-21 | 1975-11-21 | How to adjust the water level in a tunnel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60687B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57134045A (en) * | 1981-02-13 | 1982-08-19 | Toyota Motor Corp | Lubricating structure for differential-locking device |
-
1975
- 1975-11-21 JP JP13998575A patent/JPS60687B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5264145A (en) | 1977-05-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6688532B2 (en) | Controller, temperature controller and heat processor using same | |
| CN100422882C (en) | Model-Free Adaptation of Process Controllers | |
| JPS60687B2 (en) | How to adjust the water level in a tunnel | |
| JPS6219641A (en) | Method of controlling combustion for hot water supplier | |
| JPS63148050A (en) | Combustion control method for water heater | |
| CN116105375B (en) | Water heater and water temperature control method, system and storage medium thereof | |
| JPS6069451A (en) | Temperature control device of gas water heater | |
| JP2600777B2 (en) | Hot water temperature control device | |
| JPH07111268B2 (en) | Water heater controller | |
| JPH0633880B2 (en) | Steam tracing equipment | |
| JPH0694210A (en) | Vapor temperature controller for boiler | |
| JPH049604Y2 (en) | ||
| JPS5830499B2 (en) | Combustion amount control method with two types of control modes | |
| JPH01263402A (en) | Drain water level control device for water supplying and heating device | |
| JP3223339B2 (en) | controller | |
| JPH1163481A (en) | Method and apparatus for controlling fuel gas pressure of gas-fired boiler | |
| JPH0934555A (en) | Received water flow controller | |
| JPS6186814A (en) | Control system of dam discharge amount | |
| JPS6044561B2 (en) | Load distribution control method between two boilers | |
| JPH0996415A (en) | Water heater and its control method | |
| JP2512519B2 (en) | Extruder cylinder temperature control method | |
| JPS5484102A (en) | Evaporator outlet steam tempeature controller | |
| JPS60144804A (en) | Flow rate controller | |
| JPS59157707A (en) | on-off control device | |
| JPH02183815A (en) | Controller for feedwater flow rate |