JPH0150441B2 - - Google Patents
Info
- Publication number
- JPH0150441B2 JPH0150441B2 JP62076237A JP7623787A JPH0150441B2 JP H0150441 B2 JPH0150441 B2 JP H0150441B2 JP 62076237 A JP62076237 A JP 62076237A JP 7623787 A JP7623787 A JP 7623787A JP H0150441 B2 JPH0150441 B2 JP H0150441B2
- Authority
- JP
- Japan
- Prior art keywords
- concentration
- solution
- level
- flow rate
- evaporator
- 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
- 239000000243 solution Substances 0.000 claims description 22
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000011550 stock solution Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 230000001364 causal effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000004043 responsiveness Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は加熱源として蒸気を使用する濃縮装置
の制御装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a control device for a concentrator that uses steam as a heating source.
(従来技術)
第3図は従来型の制御装置を示す。1は蒸発缶
で、内部に熱交換器2がある。蒸発缶1の底部か
ら原液が原液入口管3から送られ、上部の蒸気入
口管4から加熱用蒸気が送られる。蒸発缶1の底
部の液は、ポンプ5によつて循環管路6を介し循
環され、熱交換器2の上部にてフラツシユされて
熱交換器2内で加熱される。発生した蒸気は蒸気
缶の頂部の排出管7から排出される。蒸発によつ
て濃縮された液は蒸発缶1の底部から取出管8に
より取出される。(Prior Art) FIG. 3 shows a conventional control device. 1 is an evaporator with a heat exchanger 2 inside. A stock solution is sent from the bottom of the evaporator 1 through a stock solution inlet pipe 3, and heating steam is sent from a steam inlet pipe 4 at the top. The liquid at the bottom of the evaporator 1 is circulated by a pump 5 through a circulation line 6, flushed at the top of the heat exchanger 2, and heated within the heat exchanger 2. The generated steam is discharged through a discharge pipe 7 at the top of the steam can. The liquid concentrated by evaporation is taken out from the bottom of the evaporator 1 through a take-out pipe 8.
9はレベルコントローラで、蒸発缶底部の溶液
レベルをレベル計10にて検出し、原液入口管3
に配設された入口側の流量調節弁11をこれによ
り制御する。 9 is a level controller that detects the solution level at the bottom of the evaporator with a level meter 10 and connects the raw solution inlet pipe 3.
This controls the flow control valve 11 on the inlet side, which is disposed at the inlet side.
一方12は濃度コントローラで、取出管8内に
設けた濃度計14で濃縮された液の濃度を検出
し、出口側流量調節弁13をコントロールする。 On the other hand, 12 is a concentration controller which detects the concentration of the concentrated liquid with a concentration meter 14 provided in the take-out pipe 8 and controls the outlet side flow rate control valve 13.
このように出口側流量を操作量とした濃度制御
系と、入口側流量を操作量としたレベル制御系を
備えた濃縮装置が一般的である。しかしながら濃
度など諸量の因果関係は第4図のようになつてお
り、濃度制御はレベル制御を介在して動作してい
る。このため濃度制御の性能は、レベル制御の性
能にも左右され、結局濃度制御の性能向上が困難
となつている。 As described above, a concentrating device is generally provided with a concentration control system using the outlet side flow rate as the manipulated variable and a level control system using the inlet side flow rate as the manipulated variable. However, the causal relationship between various quantities such as concentration is as shown in FIG. 4, and concentration control operates through level control. For this reason, the performance of concentration control also depends on the performance of level control, making it difficult to improve the performance of concentration control.
(発明の解決しようとする問題点)
従来型装置の問題点に鑑み、加熱源として蒸気
を使う溶液濃縮装置において、濃縮液の濃度制御
のハンチングの抑制及び濃縮液の濃度制御の応答
性向上を図ろうとするものである。(Problems to be Solved by the Invention) In view of the problems of conventional devices, it is desirable to suppress hunting in concentrated liquid concentration control and improve responsiveness of concentrated liquid concentration control in a solution concentrator that uses steam as a heating source. This is what we are trying to achieve.
(発明による解決手段)
熱交換器を内部に備えた蒸発缶の底部に供給さ
れた原液を循環管路を介し熱交換器上にフラツシ
ユして蒸発させる濃縮装置において、出口側溶液
濃度を検出し、濃度コントローラによつて入口側
の溶液流量を操作する濃度制御系と、蒸発缶内の
溶液レベルを検出し、レベルコントローラによつ
て出口側溶液流量を操作するレベル制御系とを備
え、濃度制御系がレベル制御系を介さないで制御
できるようにした。(Solving Means by the Invention) In a concentrating device that flashes a stock solution supplied to the bottom of an evaporator equipped with a heat exchanger on the heat exchanger via a circulation pipe and evaporates, the concentration of the solution on the outlet side is detected. , a concentration control system that controls the solution flow rate on the inlet side using a concentration controller, and a level control system that detects the solution level in the evaporator and controls the solution flow rate on the outlet side using a level controller. The system can now be controlled without going through the level control system.
(実施例)
第1図に基いて説明する。蒸発缶そのものは第
3図と同様の構成である。即ち1は蒸発缶で、内
部に熱交換器2がある。蒸発缶1の底部から原液
が原液入口管3より送られ、上部の蒸気入口管4
から加熱用蒸気が送られる。蒸発缶1の底部の液
はポンプ5によつて循環管路6を介し循環され、
熱交換器2の上部にてフラツシユされ熱交換器2
内で加熱される。発生した蒸気は、蒸気缶の頂部
の排出管7から排出される。蒸発によつて濃縮さ
れた液は蒸発缶1の底部から取出管8より取出さ
れる。(Example) An explanation will be given based on FIG. 1. The evaporator itself has the same structure as shown in FIG. That is, 1 is an evaporator, and a heat exchanger 2 is located inside. The undiluted solution is sent from the bottom of the evaporator 1 through the undiluted solution inlet pipe 3, and then into the vapor inlet pipe 4 at the top.
Heating steam is sent from The liquid at the bottom of the evaporator 1 is circulated through a circulation line 6 by a pump 5.
The heat exchanger 2 is flashed at the upper part of the heat exchanger 2.
heated inside. The generated steam is discharged through a discharge pipe 7 at the top of the steam can. The liquid concentrated by evaporation is taken out from the bottom of the evaporator 1 through a take-out pipe 8.
さて、本発明においては取出管8内の出口濃度
Dを濃度計14で検出し、操作量が入口側溶液流
量Fiとなるように濃度コントローラ12によつて
入口側流量調節弁11を操作する濃度制御系を構
成する。又缶内溶液重量Wを溶液レベルとしてレ
ベル計10で検出し、操作量が出口側流量Foと
なるようにレベルコントローラ9によつて出口側
流量調節弁13を操作するレベル制御系を構成す
る。 Now, in the present invention, the outlet concentration D in the take-out pipe 8 is detected by the concentration meter 14, and the concentration controller 12 operates the inlet side flow rate control valve 11 so that the manipulated variable becomes the inlet side solution flow rate Fi. Configure the control system. In addition, a level control system is constructed in which the weight W of the solution in the can is detected as the solution level by a level meter 10, and the outlet side flow rate control valve 13 is operated by the level controller 9 so that the manipulated variable becomes the outlet side flow rate Fo.
以上2つの制御系による諸量の因果関係は第2
図のようになる。このとき前記コントローラは、
PID制御器を使用する。 The causal relationship between various quantities due to the above two control systems is the second
It will look like the figure. At this time, the controller
Use a PID controller.
なお取出管8を運転中に洗浄する場合など、蒸
発缶1内の溶液を抜けないことがある。そのとき
には第3図のような構成となるように信号を切換
えて濃度コントローラ12は動作させず、入口側
でレベルコントローラ9を動作させてレベルコン
トロールを行うこともある。 Note that when cleaning the take-out pipe 8 during operation, the solution in the evaporator 1 may not be able to escape. At that time, the signal may be switched so that the configuration as shown in FIG. 3 is obtained, and the concentration controller 12 is not operated, and the level controller 9 is operated on the entrance side to perform level control.
(作用)
第2図に示すように濃度設定値Drefと、検出
した濃度Dとの偏差を入力として濃度制御用のコ
ントローラ12を動作させ、その出力により入口
側流量調節弁11が操作される。その結果とし
て、入口側流量Fiが操作量となる。入口側流量Fi
は濃度に直接影響を与え、また出口流量Foの影
響を受けない。(Function) As shown in FIG. 2, the concentration control controller 12 is operated using the deviation between the concentration setting value Dref and the detected concentration D as input, and the inlet side flow rate control valve 11 is operated by the output thereof. As a result, the inlet side flow rate Fi becomes the manipulated variable. Inlet side flow rate Fi
directly affects the concentration and is not affected by the outlet flow rate Fo.
溶液レベル設定値Lrefと検出した溶液レベルL
との偏差を入力としてレベル制御用のコントロー
ラ9を動作させ、その出力により出口側流量調節
弁13が操作され、結果として出口側流量Foが
操作量となる。入口側流量Fiと出口側流量Foの
差を積分する効果で缶内の溶液量が動かされ、そ
れは溶液レベルとして検出される。このレベル制
御系においては、入口側流量Fiは見かけ上外乱の
ように動く。 Solution level set value Lref and detected solution level L
The controller 9 for level control is operated using the deviation from the output as input, and the outlet side flow rate control valve 13 is operated based on the output thereof, and as a result, the outlet side flow rate Fo becomes the manipulated variable. The amount of solution in the can is moved by the effect of integrating the difference between the inlet flow rate Fi and the outlet flow rate Fo, which is detected as the solution level. In this level control system, the inlet flow rate Fi appears to move like a disturbance.
(効果)
濃度制御系の中にレベル制御系が介在していな
いので、濃度制御の性能をレベル制御系の性能に
依らずに改善することが可能となつた。それによ
り濃度制御のハンチングを抑制しながら応答性を
向上させることが容易となつた。(Effects) Since the level control system is not interposed in the concentration control system, it has become possible to improve the performance of concentration control without depending on the performance of the level control system. This makes it easy to improve responsiveness while suppressing hunting in concentration control.
因みに第5図は本発明による制御系を備えたも
のにおける時間−重量(wt)%線図を示し、濃
縮液の濃度が極めて安定していることがわかる。
又第6図は従来型の制御系を備えたものの時間―
重量(wt)%線図である。濃縮液の濃度がハン
チングしている状態が良く理解できる。 Incidentally, FIG. 5 shows a time-weight (wt) % diagram for an apparatus equipped with the control system according to the present invention, and it can be seen that the concentration of the concentrated liquid is extremely stable.
Figure 6 shows the time for a device equipped with a conventional control system.
It is a weight (wt)% diagram. It is easy to understand that the concentration of the concentrate is hunting.
第1図は本発明装置の配管制御回路図。第2図
は同じく制御系の説明図。第3図は従来型装置の
配管制御回路図。第4図は同じく制御系の説明
図。第5図は本発明装置に於ける時間―重量
(wt)%図。第6図は従来型装置に於ける時間−
重量(wt)%図。
図において、1…蒸発缶、2…熱交換器、3…
原液入口管、4…蒸気入口管、5…ポンプ、6…
循環管路、7…排出管、8…取出管、9…レベル
コントローラ、10…レベル計、11…流量調節
弁、12…濃度コントローラ、13…流量調節
弁、14…濃度計。
FIG. 1 is a piping control circuit diagram of the device of the present invention. FIG. 2 is also an explanatory diagram of the control system. Figure 3 is a piping control circuit diagram of a conventional device. FIG. 4 is also an explanatory diagram of the control system. FIG. 5 is a time-weight (wt) % diagram in the device of the present invention. Figure 6 shows time in conventional equipment.
Weight (wt)% figure. In the figure, 1... evaporator, 2... heat exchanger, 3...
Stock solution inlet pipe, 4... Steam inlet pipe, 5... Pump, 6...
Circulation pipe, 7...Discharge pipe, 8...Takeout pipe, 9...Level controller, 10...Level meter, 11...Flow rate control valve, 12...Concentration controller, 13...Flow rate control valve, 14...Concentration meter.
Claims (1)
された原液を循環管路を介し熱交換器上にフラツ
シユして蒸発させた濃縮装置において、出口側溶
液濃度を検出し、濃度コントローラによつて入口
側の溶液流量を操作する濃度制御系と、蒸発缶内
の溶液レベルを検出し、レベルコントローラによ
つて出口側溶液流量を操作するレベル制御系とを
備えたことを特徴とする加熱源として蒸気を使用
する溶液の濃縮装置における制御装置。1 In a concentrating device where the stock solution supplied to the bottom of an evaporator equipped with an internal heat exchanger is flashed onto the heat exchanger via a circulation pipe and evaporated, the concentration of the solution on the outlet side is detected and the concentration controller A heating device characterized by comprising a concentration control system for controlling the solution flow rate on the inlet side, and a level control system for detecting the solution level in the evaporator and controlling the outlet side solution flow rate using a level controller. Control device in a solution concentrator using steam as a source.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7623787A JPS63242302A (en) | 1987-03-31 | 1987-03-31 | Control device for solution concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7623787A JPS63242302A (en) | 1987-03-31 | 1987-03-31 | Control device for solution concentration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63242302A JPS63242302A (en) | 1988-10-07 |
| JPH0150441B2 true JPH0150441B2 (en) | 1989-10-30 |
Family
ID=13599565
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7623787A Granted JPS63242302A (en) | 1987-03-31 | 1987-03-31 | Control device for solution concentration device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63242302A (en) |
-
1987
- 1987-03-31 JP JP7623787A patent/JPS63242302A/en active Granted
Non-Patent Citations (1)
| Title |
|---|
| STARCH STARKE=1985 * |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63242302A (en) | 1988-10-07 |
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