JPS628208A - Rate controller - Google Patents

Rate controller

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Publication number
JPS628208A
JPS628208A JP14572585A JP14572585A JPS628208A JP S628208 A JPS628208 A JP S628208A JP 14572585 A JP14572585 A JP 14572585A JP 14572585 A JP14572585 A JP 14572585A JP S628208 A JPS628208 A JP S628208A
Authority
JP
Japan
Prior art keywords
water quality
flow rate
target
rate
injection
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
JP14572585A
Other languages
Japanese (ja)
Inventor
Akira Kamoto
明 加本
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 JP14572585A priority Critical patent/JPS628208A/en
Publication of JPS628208A publication Critical patent/JPS628208A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To correct the mixing rate of a mixer to a target rate speedily even when the supply amount of a primary-side raw material is small by supplying a secondary-side raw material regardless of the size of the primary-side raw material if the mixing rate of the mixer deviates from the target ratio. CONSTITUTION:If water quality detected by a water quality gauge 38 deviates from target water quality for some reason, the 2nd water quality controller 44 performs P operation on the basis of the deviation between the detected water quality and target water quality to calculate the correction quantity of a chemical injection flow rate corresponding to the deviation. The adder 52 of a chemical injection flow rate adjusting part 46 adds the correction quantity of the chemical injection flow rate to the injection flow rate of chemicals proportional to the flow rate of raw water and outputs a target chemical injection flow rate to a flow rate controller 47, thereby controlling the flow rate of chemicals. The 1st water quality controller 42, on the other hand, performs P operation on the basis of the deviation between the detected water quality and target water quality and vary the correction quantity of an injection rate which is constant so far.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は、浄水場などで行なわれる薬品の比例注入制御
や燃料ガスのカロリーコントロールを行なうためのガス
比例混合制i[1等に適用され、ある変数Xに比例して
他の変数Yを制御して加え、目標のvIZを得るように
した比率i!llIn装置に131Yづ゛る。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention is applied to a gas proportional mixing system i [1, etc.] for controlling the proportional injection of chemicals and controlling the calorie content of fuel gas in water purification plants, etc. A ratio i that controls and adds another variable Y in proportion to a certain variable X to obtain the target vIZ! 131Y is attached to the llIn device.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

従来の薬品注入制御システムは、薬品注入流量=注入率
X原水滝壷の関係式に基づき、例えば、第2図に示す如
く、原水流fdH110から得る原水流量を薬注制御装
置11内の掛輝器12により注入率と乗じ、これにより
目標薬品注入流量を求めておき、流量コントローラ14
で薬品流量計16から得る薬品注入流間が前記目標薬品
注入流量と等しくなるように調部弁18を操作して増減
し混合槽20に加えるようにしている。
The conventional chemical injection control system is based on the relational expression: chemical injection flow rate = injection rate x raw water basin, and for example, as shown in FIG. The injection rate is multiplied by 12 to determine the target chemical injection flow rate, and the flow rate controller 14
Then, the control valve 18 is operated to increase or decrease the flow rate of the chemical injected from the chemical flow meter 16 so that the flow rate of the chemical is added to the mixing tank 20 so that it becomes equal to the target chemical injection flow rate.

ところで、混合槽20の水質と予め設定された目標水質
のずれを修正するため、従来から薬注制御装置?!11
内に水質コントローラ22を設置し、水質it 24で
得た薬品注入後の水質と目標水質の偏差から注入率補正
間を求め、これを予め設定された基本注入率に加算器2
6で加算するなどして、目標水質と薬品注入後の水質の
偏差がなくなるまで前記注入率を増減補正する方法が採
られている。
By the way, in order to correct the discrepancy between the water quality of the mixing tank 20 and the preset target water quality, a chemical injection control device has conventionally been used. ! 11
A water quality controller 22 is installed in the water quality controller 22, and the injection rate correction interval is determined from the deviation between the water quality after chemical injection obtained in the water quality IT 24 and the target water quality, and this is added to the preset basic injection rate using the adder 2.
A method is adopted in which the injection rate is increased/decreased until there is no difference between the target water quality and the water quality after chemical injection, such as by adding 6 times.

しかしながら、斬かる従来技術では、原水流量の変動に
伴なって次のような問題が生じていた。
However, with the innovative conventional technology, the following problems have arisen due to fluctuations in the flow rate of raw water.

即ち、混合槽に既に流入流の混合水の水質と目標水質の
偏差を無くすためには、不足率×混合槽の容積に相当す
る量の薬品を余分に注入しなければならないが、同じ量
の薬品を注入するのに原水流量が小さいとこれに比例す
る薬品注入流量も小さくなってしまい長時間要する。
In other words, in order to eliminate the deviation between the water quality of the mixed water already flowing into the mixing tank and the target water quality, it is necessary to inject an extra amount of chemicals equivalent to the shortage rate x the volume of the mixing tank, but if the same amount If the raw water flow rate is small for injecting chemicals, the chemical injection flow rate proportional to this will also be small and it will take a long time.

換言すると、薬品注入−の水質を目標水質に保つための
制御応答速度が原水流量の大きさに左右され、原水流量
が小さいと応答が非常に遅くなり、偏差が長く続くこと
を表わす。
In other words, the control response speed for maintaining the water quality for chemical injection at the target water quality depends on the magnitude of the raw water flow rate, and if the raw water flow rate is small, the response becomes extremely slow and the deviation continues for a long time.

特に、原水流量が零になると永久に偏差が残ってしまう
In particular, when the raw water flow rate becomes zero, the deviation remains forever.

また、混合槽20に既流入分を目標水質にすることとは
別に、その後の原水流入弁に対して薬品注入後の水質が
目標水質となるように注入率の最適化を図る補正動作も
必要であるが、原水流量が小さいと制御応答が遅いため
、本来的に注入率を最適値に収束させるのに時間が掛か
ること、及び、薬品注入後の混合槽の水質と目標水質と
に偏差がある問は、その時点の流入原水に対する最適注
入率(その時の原水流入弁に対し目標水質とすることが
できる注入率)に対し、混合槽に流入部分を補正する分
だけ注入率を更に増加又は減少していなければならない
という不合理があることから、最適注入率を迅速に得る
ことが困難であった。従って原水の新たな流入部分に対
しての注入率が長時間最適注入率からずれるため、注入
後の水質と目標水質との新たな偏差要因となってしまう
不都合があり制御特性が悪いという問題があった。
In addition to adjusting the water that has already flowed into the mixing tank 20 to the target water quality, it is also necessary to perform a correction operation to optimize the injection rate so that the water quality after chemical injection at the subsequent raw water inflow valve will reach the target water quality. However, since the control response is slow when the raw water flow rate is small, it inherently takes time to converge the injection rate to the optimal value, and there is a deviation between the water quality of the mixing tank after chemical injection and the target water quality. One question is whether to further increase the injection rate by the amount that corrects the inflow portion to the mixing tank, or It has been difficult to quickly obtain the optimum injection rate due to the unreasonable requirement that the injection rate should be reduced. Therefore, the injection rate for the new inflow portion of raw water deviates from the optimum injection rate for a long time, which causes a new deviation between the water quality after injection and the target water quality, which causes the problem of poor control characteristics. there were.

〔発明の目的〕[Purpose of the invention]

本発明は上記従来技術の欠点に鑑みなされたものであり
、一次側原料と二次側原料の混合後の比率と目標比率と
の間に偏差があるとき一次側、原料の大きさに関係なく
二次側原料の供給を行なう要素を追加して、一次側原料
の供給量が零であっても混合後の比率品質の制御が可能
で制御応答性の改善を図ることができる比率制御装置を
得ることを目的とする。
The present invention was made in view of the drawbacks of the prior art described above, and when there is a deviation between the ratio of the primary raw material and the secondary raw material after mixing and the target ratio, regardless of the size of the primary raw material and the secondary raw material, By adding an element to supply secondary raw materials, we have created a ratio control device that can control the ratio quality after mixing and improve control response even when the supply amount of primary raw materials is zero. The purpose is to obtain.

〔発明の概要〕[Summary of the invention]

本発明に係る比率制御装置では、一次側原料と二次側原
料の混合後の混合比率を検出する手段と、この混合比率
と目標比率の偏差から比率補正僅を求める手段と、前記
混合比率と目標比率の偏差から二次側原料供給量補正量
を求める手段と、予め設定された基本比率を前記比率補
正層によって補正し補正比率を求め、この補正比率に一
次側原料の供給量を乗じ、更に前記二次側原料供給量補
正量を加算して二次側原料の目標供給量を求める手段と
、この目標供給量を受けて二次側原料の供給制御を行な
う手段とを備えている。
In the ratio control device according to the present invention, there is provided a means for detecting a mixing ratio of a primary raw material and a secondary raw material after mixing, a means for determining a ratio correction amount from a deviation between this mixing ratio and a target ratio, and means for determining a secondary side raw material supply amount correction amount from a deviation of the target ratio; a preset basic ratio is corrected by the ratio correction layer to obtain a correction ratio; the correction ratio is multiplied by the primary side raw material supply amount; The apparatus further includes means for adding the secondary side raw material supply amount correction amount to obtain a target supply amount of the secondary side raw material, and means for controlling the supply of the secondary side raw material in response to the target supply amount.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例を第一実施例に基づいて説明す
る。
Hereinafter, one embodiment of the present invention will be described based on the first embodiment.

第1図は本発明の係る薬品注入システムを示すブロック
図である。図において、原水が原水流量計30を介して
、薬品が薬品流l計32、調節弁34を介して混合)P
J36に供給されるようになっている。
FIG. 1 is a block diagram showing a drug injection system according to the present invention. In the figure, raw water is mixed via a raw water flow meter 30, and chemicals are mixed via a chemical flow meter 32 and a control valve 34)
It is designed to be supplied to J36.

混合槽36の出口側には薬品注入後の水質を測定する水
質計38が備えられている。
A water quality meter 38 is provided on the outlet side of the mixing tank 36 to measure the water quality after the chemical is injected.

原水流伶計30.薬品流色計32、水質計38は薬注制
till装[40の入力側に接続され、調節弁34は薬
注制御装M40の出力側に接続されている。
Raw water flow rate 30. The chemical flow meter 32 and the water quality meter 38 are connected to the input side of the chemical injection control device M40, and the control valve 34 is connected to the output side of the chemical injection control device M40.

薬注制御装置40は、基本的には原水流量に比例して薬
品の供給制御を行なうものであるが、薬品注入後の混合
槽36の水質が目標水質を維持するようにするため注入
率を可変する他、原水流Rとは無関係に薬品供給m<流
口)を可変制御できるようになっている。
The chemical injection control device 40 basically controls the supply of chemicals in proportion to the raw water flow rate, but the injection rate is adjusted so that the water quality in the mixing tank 36 after chemical injection maintains the target water quality. In addition to being variable, the chemical supply m<flow port) can be variably controlled independently of the raw water flow R.

この薬注制御装置40は、水質計38から検出データと
して得る薬品注入後の水質と予め設定された目標水質の
偏差をとりサンプルPI動作などで注入率補正量を求め
る第1水質コントローラ42と、同じく水質計38から
得る薬品注入後の水質と目標水質の偏差をとりサンプル
P動作などで薬品注入流量補正量を求める第2水質コン
トローラ44と、予め設定された基本注入率、前記注入
率補正量及び薬品注入流量補正量、原水流量計30から
検出データとして得る原水流量から目標薬品注入流量を
求める目標注入流量調整部46と、薬品流伍計32よら
検出データとして得る薬品流量が前記目標薬品流量と一
致するように調整弁34を制御する流量コントローラ4
7とから構成されている。
This chemical injection control device 40 includes a first water quality controller 42 that calculates the deviation between the water quality after chemical injection obtained as detection data from the water quality meter 38 and a preset target water quality and calculates an injection rate correction amount by sample PI operation or the like; A second water quality controller 44 calculates the deviation between the water quality after chemical injection and the target water quality obtained from the water quality meter 38 and calculates the chemical injection flow rate correction amount by sample P operation, etc., and a preset basic injection rate and the injection rate correction amount. and a drug injection flow rate correction amount, a target injection flow rate adjustment unit 46 that calculates a target drug injection flow rate from the raw water flow rate obtained as detection data from the raw water flow meter 30, and a drug flow rate obtained as detection data from the drug flow meter 32 as the target drug flow rate. A flow rate controller 4 that controls the regulating valve 34 to match the
It consists of 7.

混合槽36の水質と目標水質にずれが生じてくる場合、
原水に対する薬品注入率が不適当であると考えられる。
If a discrepancy occurs between the water quality in the mixing tank 36 and the target water quality,
It is thought that the chemical injection rate to raw water is inappropriate.

前記第1水質コントローラ42は、薬品注入率を補正さ
せて今後流入する原水に対して最適の注入率で薬品注入
を行なわしめる機能を有している。
The first water quality controller 42 has a function of correcting the chemical injection rate and injecting the chemical into the raw water that will flow in from now on at the optimum injection rate.

一方、前記第2水質コントローラ44は、混合槽36に
既に流入した原水と薬品との混合水を目標水質にするた
め原水比例分とは別に薬品注入流量の追加を行なわしめ
る機能を有している。
On the other hand, the second water quality controller 44 has a function of adding a chemical injection flow rate in addition to the raw water proportional amount in order to bring the mixed water of raw water and chemicals that has already entered the mixing tank 36 to the target water quality. .

目標注入流は調整部46は、予め設定された基本注入率
に第1水質コントローラ42から送られる注入率補正間
を加算し補正注入率を計算する加鈴3/I8と、この補
正注入率に原水流量計30から検出データとして得る原
水流口を掛けて薬品注入流量=補正比率×原水流ωの計
算式より薬品注入流量の原水比例分を計算するli)算
器50と、この原水比例薬品注入流量に第2水質コント
ローラ44から送られる薬品注入流量補正量を加え目標
薬品注入流かを計詐する加算器52とから成る。
The adjustment unit 46 calculates the corrected injection rate by adding the injection rate correction period sent from the first water quality controller 42 to the preset basic injection rate, and the adjustment unit 46 calculates the corrected injection rate. li) Calculator 50 that calculates the raw water proportional portion of the chemical injection flow rate by multiplying the raw water flow port obtained as detection data from the raw water flow meter 30 and using the calculation formula: chemical injection flow rate = correction ratio × raw water flow ω; It consists of an adder 52 that adds the chemical injection flow rate correction amount sent from the second water quality controller 44 to the injection flow rate to determine whether it is the target chemical injection flow.

流量コントローラ47は目標薬品注入流量に従い、薬品
流品計32から得る薬品流量との偏差を求め、偏差をな
くす方向に調節弁34の開度を操作し、薬品流量の制御
を行なうII能を有している。
The flow rate controller 47 has a II function that determines the deviation from the chemical flow rate obtained from the chemical flow meter 32 in accordance with the target chemical injection flow rate, and controls the chemical flow rate by controlling the opening degree of the control valve 34 in a direction to eliminate the deviation. are doing.

次に上記実施例の作用につき説明する。Next, the operation of the above embodiment will be explained.

ここでは、第1水質コントローラ42、第2水質コント
ローラ44は各々PI動作とP動作を行なうものとする
Here, it is assumed that the first water quality controller 42 and the second water quality controller 44 perform a PI operation and a P operation, respectively.

まず、原水に対しある注入率で薬品が注入されており、
混合槽20が目標水質を保持している定常状態の場合、
水質計38の検出値と目標水質の間に偏差がないため第
2水質コントローラ44はP動作上出力が零となってい
る。このため混合槽20に既流入分の原水と薬品との混
合水に薬品が追加されることはない。
First, chemicals are injected into raw water at a certain injection rate.
In a steady state where the mixing tank 20 maintains the target water quality,
Since there is no deviation between the detected value of the water quality meter 38 and the target water quality, the output of the second water quality controller 44 is zero due to P operation. Therefore, no chemicals are added to the mixed water of raw water and chemicals that has already entered the mixing tank 20.

また検出値と目標水質の間に偏差がないので、第1水質
コントローラ42はPI動作上ある一定の注入率補正量
を出力しており、これが目標薬品注入流量調節部46の
加算器48で基本注入率と加算されて最適注入率として
の補正注入率が求められている。但し、原水に基本注入
率で薬品を注入している状態で目標水質が得られている
場合は注入率補正量は零である。そして、掛算器50で
この最適注入率に原水流口が乗じられてその時の原水流
入流量に対する薬品注入流口が求められ、薬品注入流量
補正量が零なのでそのまま目標薬品注入流量として流量
コントローラ47に出力される。
Furthermore, since there is no deviation between the detected value and the target water quality, the first water quality controller 42 outputs a certain injection rate correction amount for PI operation, and this is the basic value that is determined by the adder 48 of the target chemical injection flow rate adjustment section 46. A corrected injection rate is calculated as the optimum injection rate by adding it to the injection rate. However, if the target water quality is obtained while injecting chemicals into raw water at the basic injection rate, the injection rate correction amount is zero. Then, the optimum injection rate is multiplied by the raw water flow rate in the multiplier 50 to obtain the chemical injection flow rate for the raw water inflow flow rate at that time, and since the chemical injection flow rate correction amount is zero, it is directly sent to the flow rate controller 47 as the target chemical injection flow rate. Output.

流層コントローラ47は薬品流量が前記目標薬品注入流
量となるように調節弁18を制御する。
The flow layer controller 47 controls the control valve 18 so that the chemical flow rate becomes the target chemical injection flow rate.

これにより、その後流入する原水に対し最適注入率で薬
品が注入される。原水流量が変化してもそれに比例して
薬品流量が変化するので混合槽36内の混合水質は目標
水質を維持する。
As a result, chemicals are injected into the raw water that subsequently flows in at an optimal injection rate. Even if the raw water flow rate changes, since the chemical flow rate changes in proportion to the raw water flow rate, the mixed water quality in the mixing tank 36 maintains the target water quality.

この状態から何らかの原因で水質計38の検出水質が目
標水質からずれた場合、第2水質コントローラ44は検
出水質と目標水質の偏差に基づきP動作を行ない6;i
差に対応した薬品注入流量補正量を求めて薬品注入流1
調整部46へ出力する。
If the water quality detected by the water quality meter 38 deviates from the target water quality for some reason in this state, the second water quality controller 44 performs the P operation based on the deviation between the detected water quality and the target water quality.
Find the chemical injection flow rate correction amount corresponding to the difference and adjust the chemical injection flow 1
It is output to the adjustment section 46.

薬品注入流m補正量は加算器52で原水流量、比例薬品
注入渡場に加算されて目標薬品注入流量として流量コン
トローラ47に出力され薬品流量が制御される。但し、
目標薬品注入流量が負のときは零として扱われる。
The chemical injection flow rate m correction amount is added to the raw water flow rate and the proportional chemical injection flow rate by an adder 52, and is outputted to the flow rate controller 47 as a target chemical injection flow rate to control the chemical flow rate. however,
When the target chemical injection flow rate is negative, it is treated as zero.

このように第2水質コントローラ44により、原水流用
の大きさとは関係なく水質偏差に対応して薬品流量の補
正が行なわれ混合槽36に既流入分の混合水の水質補正
がなされるので、水質制御の応答性が原水流口に影響さ
れず原水流量が小さい場合でも速やかに補正が行なわれ
る。原水流口が零になっても薬品注入流8補正最が正の
場合は既流入分の混合水は成る時間内に確実に目標水質
とされる。
In this way, the second water quality controller 44 corrects the chemical flow rate in response to the water quality deviation, regardless of the size of the raw water being diverted, and corrects the water quality of the mixed water that has already flown into the mixing tank 36. Control responsiveness is not affected by the raw water flow rate, and correction is quickly performed even when the raw water flow rate is small. Even if the raw water flow becomes zero, if the chemical injection flow 8 correction maximum is positive, the mixed water of the already inflow will surely reach the target water quality within the specified time.

一方、水質計38で検出した混合槽36の水質が目標水
質からずれを生じた場合、第1水質コントローラ42は
検出水質と目標水質の&i差に基づきPI動作を行ない
それまで一定していた注入率補正量を変更する。
On the other hand, if the water quality of the mixing tank 36 detected by the water quality meter 38 deviates from the target water quality, the first water quality controller 42 performs the PI operation based on the &i difference between the detected water quality and the target water quality, and the injection that was constant until then Change the rate correction amount.

第1.水質コントローラ42の調部動作の内、■動作部
分は検出水質と目標水質の偏差を時間的に積分していき
何らかの原因で最適値からずれた注入率を最適化の方向
へ修正する役割をなす。原水流量が小さくても第2水質
コントローラ44の薬品注入流8補正母出力などで混合
槽36に既流入分の混合水の水質と目標水質の偏差が迅
速に修正されていくので注入率の最適化も速やかになさ
れる。
1st. Among the control operations of the water quality controller 42, the operating section (1) integrates the deviation between the detected water quality and the target water quality over time, and plays the role of correcting an injection rate that deviates from the optimum value for some reason in the direction of optimization. . Even if the raw water flow rate is small, the deviation between the water quality of the mixed water already flowing into the mixing tank 36 and the target water quality is quickly corrected by the chemical injection flow 8 correction base output of the second water quality controller 44, so that the injection rate can be optimized. The changes will be made promptly.

一方、第1水質コントローラ42の調節動作の内、P動
作部分は検出水質と目標水質の偏差に対応して注入率を
前記■動作に上乗せして補正することにより、混合槽3
6に既流入分の混合水の水質と目標水質の偏差を、その
後の原水流入に従い修正せしめる役割をなす。
On the other hand, in the P operation part of the adjustment operation of the first water quality controller 42, the mixing tank 3
6 has the role of correcting the deviation between the water quality of the already inflow mixed water and the target water quality according to the subsequent inflow of raw water.

第1水質コントローラ42の出力値は注入率補正量とし
て目標注入流ω調整部46の加算器48にj工られ基本
注入率と加算され補正注入率が求められる。そして、掛
算器50で補正注入率に原水流量が掛は合わされて原水
流量に比例弁の薬品注入流量が求められる。
The output value of the first water quality controller 42 is sent as an injection rate correction amount to an adder 48 of the target injection flow ω adjustment section 46 and added to the basic injection rate to obtain a corrected injection rate. Then, the corrected injection rate is multiplied by the raw water flow rate in a multiplier 50 to obtain the raw water flow rate and the chemical injection flow rate of the proportional valve.

この原水流量比例薬品注入′?Jl量は加算器52で前
記第2水質コントローラ44の出力する薬品注入流8補
正最に足し合わされて流量コントローラ47に目標値と
して出力され薬品流量が制御される。
Is this raw water flow rate proportional chemical injection? The Jl amount is added to the chemical injection flow 8 correction output from the second water quality controller 44 in an adder 52, and is output as a target value to the flow rate controller 47 to control the chemical flow rate.

これによって薬品注入流8補正最によるのとは別個に混
合槽36に既流入分の水質の修正が行なわれ原水流量が
大きいときは一層修正が甲められるとともに、この結果
迅速に最適化されていく注入率でその後の流入原水に対
し薬品を注入することができ、新たな流入部分について
も速やかに、目標水質となっていく。従って混合槽36
に該流入弁の水質に対する偏差修正動作をほとんど防げ
ることがなく、制御応答が早くなる。
As a result, the water quality of the water that has already flowed into the mixing tank 36 is corrected separately from the chemical injection flow 8 correction, and when the raw water flow rate is large, the correction is made even more intense, and as a result, optimization is quickly achieved. Chemicals can be injected into subsequent inflow raw water at a certain injection rate, and the new inflow portion will quickly reach the target water quality. Therefore, the mixing tank 36
This hardly prevents the inflow valve from correcting deviations in water quality, and the control response becomes faster.

このようにして混合槽36の水質が目標水質に近づくと
加算器48が出力する補正注入率も最適値に近づいて行
き、目標水質が得られたところで最適注入率となる。
In this way, as the water quality in the mixing tank 36 approaches the target water quality, the corrected injection rate output by the adder 48 also approaches the optimum value, and when the target water quality is obtained, the optimum injection rate is reached.

その後は、目標水質となっている混合槽36に、ある量
の原水が流入するとそれに比例して最適注入率により薬
品も注入されるので混合槽36の水質は目標水質を維持
する。
Thereafter, when a certain amount of raw water flows into the mixing tank 36, which has the target water quality, chemicals are also injected at the optimum injection rate in proportion to the amount of raw water, so that the water quality in the mixing tank 36 maintains the target water quality.

なお、第1水質コントローラ42は目標水質と検出水質
の偏差から1動作だけを行なって注入率補正量を待るよ
うにしてもよい。また、原水流量計30から原水流量を
、薬品流量計32から薬品流口を入力しておき、各々あ
る時間積算し原水流量積算値と薬品流量積算値の比と検
出水質との関係から目標水質を達成するための最適な注
入率補正量を得るようにしてもよい。
Note that the first water quality controller 42 may perform only one operation based on the deviation between the target water quality and the detected water quality and wait for the injection rate correction amount. In addition, input the raw water flow rate from the raw water flow meter 30 and the chemical flow rate from the chemical flow meter 32, integrate each for a certain time, and determine the target water quality from the relationship between the ratio of the raw water flow rate integrated value and the chemical flow rate integrated value and the detected water quality. An optimum injection rate correction amount may be obtained to achieve this.

一方、第2水質コントローラ44は、目標水質と検出水
質の偏差があるとき一定値の薬品注入流8補正最を出力
したり、或いは偏差に二乗比例する薬品注入流口補正量
を出力するようにしてもよい。
On the other hand, the second water quality controller 44 outputs a constant value of the chemical injection flow 8 correction amount when there is a deviation between the target water quality and the detected water quality, or outputs a chemical injection flow port correction amount that is proportional to the square of the deviation. It's okay.

また、これとは別に目標水質を変更する場合、基本注入
率も一緒に変更し注入率補正量のレベルを小さくして制
御性を高める必要があるが、第3図に示すように、薬注
制御装置60に目標水質を入力するとこれを予め実験な
どで定められた一次式等の関係に基づき基本注入率に変
換し加算器48へ出力する変換器54を設けることによ
り操作性の向上を図ることができる。
Separately, when changing the target water quality, it is necessary to change the basic injection rate as well and reduce the injection rate correction level to improve controllability. Improved operability is achieved by providing a converter 54 that inputs a target water quality into the control device 60 and converts it into a basic injection rate based on a relationship such as a linear equation determined in advance through experiments, etc. and outputs it to the adder 48. be able to.

また、目標水質を変更したとき、第1又は第2水質コン
トローラ42又は44のPI動作、P動作などの係数を
目標水質の大小に応じて大小補正ずればより制御応答性
を高めることができる。
Further, when the target water quality is changed, the control responsiveness can be further improved by adjusting the coefficients of the PI operation, P operation, etc. of the first or second water quality controller 42 or 44 according to the magnitude of the target water quality.

更に、第1図における基本注入率と注入率補正量を加算
するための加算器をS算器に置き替えて補正注入率を求
めるようにしてもよい。この、場合、第1水質コントロ
ーラは注入率を補正り゛る必要がないとき1を出ツノす
るよう作動せしめればよい。
Furthermore, the adder for adding the basic injection rate and the injection rate correction amount in FIG. 1 may be replaced with an S calculator to obtain the corrected injection rate. In this case, the first water quality controller may be operated to output 1 when there is no need to correct the injection rate.

(発明の効果〕 以上説明したように本発明によれば混合後の混合比率と
目標比率との間に偏差が生じた場合、一次側原料の大ぎ
さに関係なく二次側原料を供給するようにしたので、一
次側原料の供給量が少ないときでも迅速に目標比率への
修正を行なうことができ、檎だ、これから混合する一次
側原料と二次側原料の比率補正と、混合済原料に対する
比率補正を平行して行なえるので制御応答性が良好とな
る。
(Effects of the Invention) As explained above, according to the present invention, if a deviation occurs between the mixing ratio after mixing and the target ratio, the secondary raw material is supplied regardless of the size of the primary raw material. As a result, even when the supply amount of primary raw materials is small, it is possible to quickly adjust the target ratio. Since ratio correction can be performed in parallel, control responsiveness is improved.

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

第1図は本発明の一実施例に係る薬品比例注入装置を示
す概略構成図、第2図は従来の薬品比例注入装置を示す
概略構成図、第3図は本発明の他の実施例に係る薬品比
例注入装置を示す概略構成図である。 30・・・原水流聞計    32・・・薬品流母計3
6・・・混合槽      38・・・水質計  ・4
0・・・薬注制御装置 42・・・第1水質コントローラ 44・・・第2水質コントローラ 46・・・流ω調整部 47・・・流量コントローラ 60・・・薬注制御装置 第1図 第2図
FIG. 1 is a schematic configuration diagram showing a chemical proportional injection device according to an embodiment of the present invention, FIG. 2 is a schematic configuration diagram showing a conventional chemical proportional injection device, and FIG. 3 is a schematic configuration diagram showing a conventional chemical proportional injection device. FIG. 1 is a schematic configuration diagram showing such a chemical proportional injection device. 30... Raw water flow meter 32... Chemical flow meter 3
6...Mixing tank 38...Water quality meter ・4
0... Chemical injection control device 42... First water quality controller 44... Second water quality controller 46... Flow ω adjustment section 47... Flow rate controller 60... Chemical injection control device Fig. 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 一次側原料の供給量を検出し、この一次側原料の供給量
に比例して二次側原料の供給量を制御する比率制御装置
において、一次側原料と二次側原料の混合後の混合比率
を検出する手段と、この混合比率と目標比率の偏差から
比率補正量を求める手段と、前記混合比率と目標比率の
偏差から二次側原料供給量補正量を求める手段と、予め
設定された基本比率を前記比率補正量によつて補正し補
正比率を求め、この補正比率に一次側原料供給量を乗じ
、更に前記二次側原料供給量補正量を加算して二次側原
料の目標供給量を求める手段と、この目標供給量を受け
て二次側原料の供給制御を行なう手段とを備えたことを
特徴とする比率制御装置。
In a ratio control device that detects the supply amount of the primary side raw material and controls the supply rate of the secondary side raw material in proportion to the supply rate of the primary side raw material, the mixing ratio after mixing the primary side raw material and the secondary side raw material is means for detecting the ratio correction amount from the deviation between the mixing ratio and the target ratio, means for obtaining the secondary side raw material supply amount correction amount from the deviation between the mixing ratio and the target ratio, The ratio is corrected by the ratio correction amount to obtain a correction ratio, this correction ratio is multiplied by the primary side raw material supply amount, and the secondary side raw material supply amount correction amount is added to obtain the target supply amount of the secondary side raw material. 1. A ratio control device comprising: means for determining the target supply amount; and means for controlling the supply of secondary side raw materials in response to the target supply amount.
JP14572585A 1985-07-04 1985-07-04 Rate controller Pending JPS628208A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14572585A JPS628208A (en) 1985-07-04 1985-07-04 Rate controller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14572585A JPS628208A (en) 1985-07-04 1985-07-04 Rate controller

Publications (1)

Publication Number Publication Date
JPS628208A true JPS628208A (en) 1987-01-16

Family

ID=15391688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14572585A Pending JPS628208A (en) 1985-07-04 1985-07-04 Rate controller

Country Status (1)

Country Link
JP (1) JPS628208A (en)

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