JPS58139704A - Device for controlling detection of boundary of waste resin liquid - Google Patents
Device for controlling detection of boundary of waste resin liquidInfo
- Publication number
- JPS58139704A JPS58139704A JP2300382A JP2300382A JPS58139704A JP S58139704 A JPS58139704 A JP S58139704A JP 2300382 A JP2300382 A JP 2300382A JP 2300382 A JP2300382 A JP 2300382A JP S58139704 A JPS58139704 A JP S58139704A
- Authority
- JP
- Japan
- Prior art keywords
- way valve
- conductivity
- waste liquid
- resin
- liquid
- 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
Links
Abstract
Description
【発明の詳細な説明】
零発#4Vi樹脂廃液からフェノール樹脂を回収すると
ともに不要廃液を排出する樹脂廃液界面検出制御装置に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a resin waste liquid interface detection and control device that recovers phenol resin from #4Vi resin waste liquid and discharges unnecessary waste liquid.
従来、有機樹脂たるフェノール液と不要廃液とを分離し
て回収するのに、比重変化検出法があったOこれはフェ
ノール液と不要廃液の比電差が小さすぎて検出ができな
いという問題があった。また他の方法としては光セシリ
ーを用い九本のがあった。この場合には液の色が一定せ
ず使用できなかった。更に他の方法としては、静電容量
式というものがあるが、液の導電率が高すぎ、静電容量
変化が検出しにくいという問題があつ几。Conventionally, a specific gravity change detection method has been used to separate and recover phenol liquid, which is an organic resin, and unnecessary waste liquid. Ta. There were also nine other methods using optical cecily. In this case, the color of the liquid was inconsistent and could not be used. Another method is the capacitance method, but the problem is that the conductivity of the liquid is too high, making it difficult to detect changes in capacitance.
本発明は上述の点に鑑みて提供したものであって、有機
樹脂と不要廃液間の、境界面検出において、境界面検出
セルの汚れ、液温度変化、液の流れ状態において確実に
境界面検出を行って、有機樹脂と不要廃液とを分離回収
できる樹脂廃液界面検出制御装置を提供することを目的
とするものである。The present invention has been provided in view of the above points, and is capable of reliably detecting an interface between an organic resin and an unnecessary waste liquid even when the interface detection cell is contaminated, the liquid temperature changes, and the liquid flow condition is detected. It is an object of the present invention to provide a resin waste liquid interface detection and control device that can separate and recover organic resin and unnecessary waste liquid.
中(2)はフェノール樹脂反応釜よりフェノール樹脂△
発液を沈降せしめるタンクで、このタンク(2)内で不
要廃液たる水(9)と、回収樹脂友るフェノール(lO
)とを分離沈降せしめる。(3)はタンク(2)下方に
設けられた三方弁で、フェノール(l(2)を回収する
ためのものである。(4)は三方弁(3)の一方に接続
され九二方弁で、不要廃液を排出せしめるものである。Inside (2) is a tank in which the phenol resin △ liquid is allowed to settle from the phenol resin reaction vessel.In this tank (2), water (9) which is an unnecessary waste liquid and phenol (1O
) and are allowed to separate and settle. (3) is a three-way valve installed below the tank (2) for recovering phenol (l(2)). (4) is a nine-way valve connected to one side of the three-way valve (3). This allows unnecessary waste liquid to be discharged.
(5)はタンク(2)と三方弁(3)との間に配置した
導電率計で、フェノール樹脂廃液の導電率を測定するも
のである。(6)はフェノール樹脂の導電率の上下限を
設定しておいて回収するフェノール(101を判定する
+lJ定器で、導電率の上下限は夫々、上限設定デジタ
ルスイッチ(ll)と下限設定デジタルスイッチθ匂と
で設定するようにしである。即ち、この導電率のE下限
の設定は、液温や0ツトのばらつきを加味し念値として
、上限値20μυ/備、下限値111υ/1Mとしてい
る。(7)は不要廃液の最小導電率とフェノール(10
)の最大導電率の差に安全率を加味した値を予め設定し
ておく変化量演算器で、例えば不要廃液次ろ水(9)の
最小導電率を9.65 、回収するフェノール(io)
の最大導電率を250、安全率を1゜3とし、(250
−9,65)÷1.3中185μTJ/6Rを設定する
。但し安全率H1,0〜1.5とする。そしてこの設定
値は質化坂設定デジタルスイッチ0埠にて設定する。!
8) tI′i判定器(6)や変化量演算器(7)から
の値によって、二方弁(4)の開閉信号と三方弁(3)
の切替信号を出すシーケシスコシトO−うで、とのシー
ケシスコシトローラ(8)にて三方弁(3)と二方弁(
4)を制御してフェノール(lO)を回収し、水(9)
を排出するのである。(5) is a conductivity meter placed between the tank (2) and the three-way valve (3), which measures the conductivity of the phenol resin waste liquid. (6) is a +lJ meter that determines the phenol (101) to be recovered after setting the upper and lower limits of the electrical conductivity of the phenolic resin. In other words, the lower limit of the electrical conductivity is set with an upper limit of 20μυ/1M and a lower limit of 111υ/1M, taking into account liquid temperature and zero-point variations. (7) is the minimum conductivity of unnecessary waste liquid and phenol (10
) is a change amount calculator that presets a value that takes into account a safety factor to the difference in the maximum conductivity of
The maximum conductivity of is 250, the safety factor is 1°3, and (250
Set 185μTJ/6R in -9,65)÷1.3. However, the safety factor H1 is set to 0 to 1.5. This set value is set using the grading slope setting digital switch 0. !
8) The open/close signal for the two-way valve (4) and the three-way valve (3) are determined based on the values from the tI′i determiner (6) and the change amount calculator (7).
The three-way valve (3) and the two-way valve (
4) to recover phenol (lO) and water (9).
It discharges.
しかして、フェノール樹脂反応釜よりフェノール樹脂廃
液をタンク(2)へ受は入れ、沈降に必要な時間だけ廃
液を静置する。そして沈降完了時(静置時間経過)、!
I’ll定器(6)の判定で廃液の導電率が上下限の中
間値であれば、導電率計(6)正常で沈降完了と判断し
、三方弁(3)を回収フェノールタシク゛側へ切替える
。判定器(6)の判定が上限設定値より大であれば、沈
降未完又は導1iIi″4計(5)異常と判断し、オペ
レーターへ点検指示を通報する。また判定器(6)の判
定が下限値より小であれば、導電率計(6)の汚れ、又
は故障と判断しオペレーターへ点検指示を通報する。回
収フェノールtIO) JIX出し開始後、変化量演算
器(7)の判定出力が変化量設定値より大であれば、三
方弁(3)を不要廃液排出側へ切替える。この時二方弁
(4)は閉状態である。この状態で、変化量演算器(7
)の判定出力が変化量設定値より大であり、判定器(6
)の判定出力が上限値より大が数分間出力されておれば
、二方弁(4)を開とし、不稗廃液を排出する。上記数
分間は、水(9)とフェノール(10)の分離時間で、
簡単な撹拌混合であれば1分稈1!liでほぼ分離する
。もし、判定器(6)と変化量演算器(7)の出力が数
分以内に変化すれば、導電率計(6)異常と#4]断し
、オペレーターへ通報する。次に変化量演算器(7)の
出力が設定値より大、判定器(6)の出力が上限値よシ
大の#4j定を数゛十秒間(排出時の気泡通過及びパル
プ内等の残留防止のためにタイムラグをとる)出力して
おればフェノール回収1gイクル終Tとする。尚、上記
判定器(6)及び変化量演算器(7)の出力はシーケシ
スフシト0−ラ(8)に入力されて、三方弁(3)及び
二方弁(4)を制御している。このようにして、フェノ
ール+101の沈降分離操作のシーケシスに従い導電率
計(5)の出力値をリアルタイムに判断し、導電率計(
5)異常を可能にしたものである。また境界面検出器と
して導電率計(6)を採用したことにより、液の流れ状
態の影響をなくしたものである。導電率測定値信号から
境界面検出を行う方法として、導電率の値の大小だけで
なく、変化値の演算も行い、境界面検出を行うことによ
り沈降分離したフェノール液温、フェノール濃度検出セ
ルの汚れにょる検出三スを未然に防ぐものである。Then, the phenol resin waste liquid is received from the phenol resin reaction vessel into the tank (2), and the waste liquid is allowed to stand still for a time required for sedimentation. And when settling is complete (standing time has elapsed),!
If the conductivity of the waste liquid is determined by the I'll meter (6) to be between the upper and lower limits, it is determined that the conductivity meter (6) is normal and sedimentation is complete, and the three-way valve (3) is turned to the collecting phenol tube side. Switch to If the judgment of the judgment device (6) is larger than the upper limit set value, it is judged that the sedimentation is not completed or that there is an abnormality (5), and an inspection instruction is notified to the operator. Also, if the judgment of the judgment device (6) is If it is smaller than the lower limit, it is determined that the conductivity meter (6) is dirty or malfunctioning, and an inspection instruction is sent to the operator. If the amount of change is greater than the set value, the three-way valve (3) is switched to the unnecessary waste liquid discharge side.At this time, the two-way valve (4) is in the closed state.In this state, the amount of change calculator (7
) is larger than the change amount setting value, and the judgment output of the judge (6
) is greater than the upper limit for several minutes, the two-way valve (4) is opened and the sterile waste liquid is discharged. The above several minutes are the separation time of water (9) and phenol (10),
One culm per minute for simple stirring and mixing! almost separated by li. If the outputs of the determiner (6) and the change amount calculator (7) change within a few minutes, it is determined that the conductivity meter (6) is abnormal and the operator is notified. Next, the output of the change amount calculator (7) is greater than the set value, and the output of the determiner (6) is greater than the upper limit value. (take a time lag to prevent residue)) If it is output, the end time is T for 1 g of phenol recovery. The outputs of the determination device (6) and the change amount calculation device (7) are input to the sequence controller (8) to control the three-way valve (3) and the two-way valve (4). In this way, the output value of the conductivity meter (5) is judged in real time according to the sequence of sedimentation separation operation of phenol+101, and the output value of the conductivity meter (5) is determined in real time.
5) It is what made the abnormality possible. Furthermore, by employing a conductivity meter (6) as the boundary surface detector, the influence of the flow state of the liquid is eliminated. As a method for detecting the boundary surface from the conductivity measurement signal, we not only calculate the magnitude of the conductivity value, but also calculate the change value, and by detecting the boundary surface, we can calculate the temperature of the precipitated phenol liquid and the phenol concentration detection cell. This prevents detection problems due to dirt.
以下実験結果ケ示す。The experimental results are shown below.
0 回収フェノール導電率(液温:26℃)0 液温度
−導電率(リンづルAの場合)L記のごとく廃液発生0
ツト、液温により導電率か変化する。0 Recovered phenol electrical conductivity (liquid temperature: 26°C) 0 Liquid temperature - electrical conductivity (in the case of Linzuru A) Waste liquid generation as shown in L 0
However, the conductivity changes depending on the liquid temperature.
0 不要廃液の導電率(液温:26℃)尚、フェノール
だけでなく、メタノール、ホルマリン等の有機物の界面
検出もできるのももちろんである。0 Electrical conductivity of unnecessary waste liquid (liquid temperature: 26°C) Of course, it is also possible to detect not only phenol but also organic substances such as methanol and formalin at the interface.
本発#4は、タシクと、三方弁と、二方弁と、導電率計
と、判定器と、変化量演算器と、シーケシスコシトD−
ラとを上述のように構5成し友ので、検出器を導電率計
とすることにより、液が流動状態と静止状態の差がない
ものであり、また導電率の大小と変化量から界面検出を
行うことにより、出セル汚れによるゆるやかな変化は無
視し、確実に界面検出ができ、有機樹脂分回収できて不
要廃液を排出できる’II果を奏する。This engine #4 consists of the following: a three-way valve, a two-way valve, a conductivity meter, a judge, a change amount calculator, and a search system D-
Since the conductivity meter is configured as described above, and the detector is a conductivity meter, there is no difference between the fluid state and the static state, and the interface By performing detection, gradual changes due to discharge cell contamination can be ignored, interfaces can be reliably detected, organic resin components can be recovered, and unnecessary waste liquid can be discharged.
図は本発明の実施例の構成図である。
(2)けタシク、(3)は三方弁、(4)は二方弁、(
5)は導電率計、(6)は判定器、(7)は変化量演算
器、(8)はシーケシスコシトD−ラを示す。
代理人 弁理士 石 1)長 七The figure is a configuration diagram of an embodiment of the present invention. (2) Ketashiku, (3) is a three-way valve, (4) is a two-way valve, (
5) is a conductivity meter, (6) is a determiner, (7) is a variation calculator, and (8) is a sequence controller. Agent Patent Attorney Ishi 1) Choshichi
Claims (1)
脂とに分離沈降せしめるタシクさ、このタシクから有機
樹脂を回収する三方弁と、三方弁の一方に接続されて不
要廃液を排出する二方弁と、タシクと三方弁との間に設
けられて樹脂廃液の導電率を測定する導電率計ど、導電
率からの測定値信号にて予め導電率の上下限を設定して
回収樹脂をヤ」定する判定器と、不要廃液の最小導電率
と回収樹脂の最大導電率の差に安全率を加味し友値を予
め設定しておざく変化量演算器と、回収樹脂取出し開始
後変化量演算器の値によって三方弁を不要廃液排出側に
制御するとと亀に、この制御状態において判定器の値に
より二方弁を不要廃液゛を排出せしめるべく制御するシ
ーケシスコシトD−ラとを具備して成る樹脂廃液界面検
出制御装置。(1) A tank that separates and settles resin waste liquid containing organic resin into unnecessary waste liquid and recovered resin, a three-way valve that recovers the organic resin from this tank, and a two-way valve that is connected to one side of the three-way valve to discharge the unnecessary waste liquid. A conductivity meter is installed between the valve, the tank, and the three-way valve to measure the conductivity of the resin waste, and the upper and lower limits of the conductivity are set in advance based on the measured value signal from the conductivity, and the recovered resin is measured. ”, a change amount calculator that presets a value by adding a safety factor to the difference between the minimum conductivity of unnecessary waste liquid and the maximum conductivity of recovered resin, and a change amount calculator that determines the amount of change after starting to take out the recovered resin. In addition to controlling the three-way valve to the unnecessary waste liquid discharge side according to the value of the computing unit, the system also includes a sequence controller that controls the two-way valve to discharge unnecessary waste liquid according to the value of the determiner in this control state. Resin waste liquid interface detection control device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2300382A JPS58139704A (en) | 1982-02-15 | 1982-02-15 | Device for controlling detection of boundary of waste resin liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2300382A JPS58139704A (en) | 1982-02-15 | 1982-02-15 | Device for controlling detection of boundary of waste resin liquid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58139704A true JPS58139704A (en) | 1983-08-19 |
Family
ID=12098320
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2300382A Pending JPS58139704A (en) | 1982-02-15 | 1982-02-15 | Device for controlling detection of boundary of waste resin liquid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58139704A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018141434A1 (en) * | 2017-01-31 | 2018-08-09 | Siemens Aktiengesellschaft | System and method for operating reactor units in a process plant |
-
1982
- 1982-02-15 JP JP2300382A patent/JPS58139704A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018141434A1 (en) * | 2017-01-31 | 2018-08-09 | Siemens Aktiengesellschaft | System and method for operating reactor units in a process plant |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3457787A (en) | Method of and apparatus for the automatic observation and regeneration of devices for the sampling of waste gases | |
US3088592A (en) | Control system | |
US4057721A (en) | Oil pollution monitoring and monitoring unit | |
CN103649712A (en) | Solid phase extraction device and viscosity measurement device | |
JPS58139704A (en) | Device for controlling detection of boundary of waste resin liquid | |
JPS6247071Y2 (en) | ||
JPH06136366A (en) | Method and apparatus for separating tar from ammonia liquor contained in waste coke-oven-gas cleaning liquid | |
JPH0129202B2 (en) | ||
ZA200105515B (en) | Sludge density measurement for controlling a sludge treatment stage. | |
JPH06265555A (en) | Automatic chemical analyzer | |
JP2804638B2 (en) | Cross-flow type solid-liquid separator | |
JPS6133371B2 (en) | ||
CN204740169U (en) | Quality of water on line analyzer water sample preprocessing device in earlier stage | |
JPS60161558A (en) | Detecting method of abnormality of reaction chamber | |
US4558714A (en) | Resin interface detection system | |
CN219201492U (en) | Online detection device for catalyst concentration in brominated SBS synthesis process | |
JPS6339607A (en) | Operating method for filtering and concentrating device for sludge | |
CN212410504U (en) | Liquid medicine PH sampling, detection device | |
JP7028939B1 (en) | Fuel purifier | |
CN107281779A (en) | A kind of solvent separation unit | |
JPS58156815A (en) | Measuring device for flow rate | |
JPS5987008A (en) | Liquid separation apparatus | |
CA1072770A (en) | Monitoring of contaminated fluid streams | |
CN104730178B (en) | The online chromatography of ions in situ detection of full-automatic high-pressure water supply line takes, sampling device | |
JPH0310057B2 (en) |