JPH0630759B2 - Cyan waste liquid treatment device - Google Patents

Cyan waste liquid treatment device

Info

Publication number
JPH0630759B2
JPH0630759B2 JP28363887A JP28363887A JPH0630759B2 JP H0630759 B2 JPH0630759 B2 JP H0630759B2 JP 28363887 A JP28363887 A JP 28363887A JP 28363887 A JP28363887 A JP 28363887A JP H0630759 B2 JPH0630759 B2 JP H0630759B2
Authority
JP
Japan
Prior art keywords
temperature
time
waste liquid
guaranteed
injection valve
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 - Lifetime
Application number
JP28363887A
Other languages
Japanese (ja)
Other versions
JPH01123687A (en
Inventor
允 吉川
雅三 戸ノ本
節夫 樋口
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.)
Mitsubishi Cable Industries Ltd
Original Assignee
Mitsubishi Cable Industries Ltd
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 Mitsubishi Cable Industries Ltd filed Critical Mitsubishi Cable Industries Ltd
Priority to JP28363887A priority Critical patent/JPH0630759B2/en
Publication of JPH01123687A publication Critical patent/JPH01123687A/en
Publication of JPH0630759B2 publication Critical patent/JPH0630759B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Removal Of Specific Substances (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は圧力容器内で加熱用蒸気によりシアン廃液を加
熱保持し、熱加水分解するシアン廃液処理装置に関す
る。
Description: TECHNICAL FIELD The present invention relates to a cyan waste liquid treatment apparatus that heats and holds a cyan waste liquid by heating steam in a pressure vessel and thermally hydrolyzes it.

(従来技術) この種処理装置では、分解処理工程中における処理温度
及び所定時間の管理が処理能力に大きく左右する。
(Prior Art) In this type of processing apparatus, management of the processing temperature and a predetermined time during the decomposition processing step largely depends on the processing capacity.

即ち処理温度に関しては、所定の処理温度まで加熱した
シアン廃液を、単に保温機能を有する圧力容器内で保っ
ておくだけでは、分解処理工程中に必然的に温度が低下
するため、従来より処理工程中に間欠的に加熱用蒸気を
投入することにより、所定の処理温度を保つようにして
いる。
That is, regarding the treatment temperature, if the cyan waste liquid heated to a predetermined treatment temperature is kept in a pressure vessel having a heat retaining function, the temperature will inevitably decrease during the decomposition treatment process. A predetermined processing temperature is maintained by intermittently introducing heating steam into the inside.

また所定時間に関しては、タイマー等により例えば3時
間の分解処理を行えるようにしている。
As for the predetermined time, a timer or the like can perform the decomposition process for, for example, 3 hours.

ところが分解処理中の温度変化においては、一時的に保
証温度以下になることもあり、この保証温度以下の時間
範囲では分解処理性能が極端に落ちる。一方分解処理時
間は上記のように一律に設定されるので、保証温度以下
の時間も処理時間に含まれることになり、シアン廃液を
十分に分解できないことがある。
However, when the temperature changes during the decomposition process, the temperature may temporarily fall below the guaranteed temperature, and the decomposition process performance is extremely deteriorated in the time range below the guaranteed temperature. On the other hand, since the decomposition processing time is uniformly set as described above, the processing time also includes the time equal to or lower than the guaranteed temperature, and the cyan waste liquid may not be decomposed sufficiently.

また、処理温度を高く設定することによりシアン廃液の
処理能力の安定化を図ることができるが、加熱用エネル
ギーの増加分の割りには処理能力は増加せず、エネルギ
ー効率が極端に下がり、燃料経費が大幅に増加する。
Also, by setting the processing temperature high, it is possible to stabilize the processing capacity of the cyan waste liquid, but the processing capacity does not increase in proportion to the increase in heating energy, and the energy efficiency drops extremely, resulting in Expense will increase significantly.

(発明の目的) 本発明の目的は、シアン廃液を分解処理能力の安定化と
燃料経費の節約を達成することである。
(Object of the invention) The object of the present invention is to achieve stabilization of the decomposition treatment capacity of cyan waste liquid and saving of fuel cost.

(目的を達成するための技術的手段) 上記目的を達成するために本発明は、シアン廃液の温度
を検出する温度センサーと、温度センサーによる検出温
度が、保証温度より低い温度範囲か保証温度以上の範囲
かを判別すると共に所定処理温度以上になる時点と最適
処理下限温度以下になる時点を判別する判別手段と、最
適処理下限温度以下になる時点を検出した時に蒸気投入
弁のアクチュエータに開信号を発信し、所定処理温度以
上になる時点を検出した時に閉信号を発信する開閉信号
発信手段と、分解処理開始後保証温度以上の温度の時間
のみを積算する積算手段と、該積算手段による積算時間
が所定時間に達したときに蒸気投入弁のアクチュエータ
に閉状態ロック信号を発信する信号発信手段とを備えて
いる。
(Technical means for achieving the object) In order to achieve the above object, the present invention provides a temperature sensor for detecting the temperature of a cyan waste liquid, and a temperature detected by the temperature sensor is in a temperature range lower than the guaranteed temperature or higher than the guaranteed temperature. And a determination means for determining when the temperature becomes equal to or higher than a predetermined processing temperature and when the temperature becomes equal to or lower than the optimum processing lower limit temperature. And a closing signal transmitting means for transmitting a closing signal when a time point at which the temperature exceeds a predetermined processing temperature is detected, an integrating means for integrating only the time of the temperature equal to or higher than the guaranteed temperature after the start of the decomposition processing, and the integrating means And a signal transmitting means for transmitting a closed state lock signal to the actuator of the steam injection valve when the time reaches a predetermined time.

(作用) 圧力容器内の高温の加熱蒸気により、シアン廃液はアン
モニアガス、蟻酸塩及び金属酸化物に熱加水分解され
る。この分解処理工程中、温度センサーの温度検出及び
これによる蒸気投入弁の開閉により、できるだけ所定の
処理温度を維持するように制御される。しかも処理中に
たとえ保証温度より低い温度に下がったとしても、その
時間範囲は処理時間に積算されず、保証温度以上の高い
温度の時間のみ処理時間と積算して処理時間が制御され
る。
(Operation) The cyan waste liquid is thermally hydrolyzed into ammonia gas, formate salt and metal oxide by the high-temperature heating steam in the pressure vessel. During the decomposition process, the temperature is detected by a temperature sensor and the steam injection valve is opened / closed by the temperature detection so that the temperature is controlled to be as high as possible. Moreover, even if the temperature falls below the guaranteed temperature during processing, the time range is not integrated into the processing time, and the processing time is controlled by integrating only the time at a temperature higher than the guaranteed temperature with the processing time.

(実施例) 第1図は本発明を適用したシアン廃液処理装置は配管略
図であり、この第1図において、圧力容器1には給液弁
2を介して予熱槽3が接続されると共に、排液弁5を介
して次工程槽、例えば冷却槽6が接続されている。予熱
槽3は送液ポンプ8を介してシアン廃液貯槽10に接続
されている。圧力容器1内にはノズル式の蒸気供給部4
が配置され、該蒸気供給部4は蒸気投入弁11を介して
蒸気供給源12に接続されている。蒸気供給源12は所
定処理温度170℃より少し高い温度の加熱用蒸気を圧
力容器1に供給するようになっている。
(Example) FIG. 1 is a schematic piping diagram of a cyan waste liquid treatment apparatus to which the present invention is applied. In FIG. 1, a pressure vessel 1 is connected with a preheating tank 3 via a liquid supply valve 2, and A next process tank, for example, a cooling tank 6 is connected via the drain valve 5. The preheating tank 3 is connected to a cyan waste liquid storage tank 10 via a liquid feeding pump 8. Nozzle type steam supply unit 4 is provided in the pressure vessel 1.
And the steam supply unit 4 is connected to a steam supply source 12 via a steam injection valve 11. The steam supply source 12 supplies heating steam having a temperature slightly higher than a predetermined processing temperature of 170 ° C. to the pressure vessel 1.

また圧力容器1にはガス抜き弁13を介してアンモニア
ガス吸収槽14が接続されている。この実施例ではガス
抜き弁13を、ガス投入弁15を介して予熱槽3に接続
することにより、排ガスを予熱槽3の熱源として利用で
きるようになっている。ガス抜き弁13にはこれを自動
開閉するためのアクチュエータ23、例えば油圧シリン
ダーあるいは空圧シリンダーが連結されている。
An ammonia gas absorption tank 14 is connected to the pressure vessel 1 via a gas vent valve 13. In this embodiment, the gas vent valve 13 is connected to the preheating tank 3 via the gas charging valve 15 so that the exhaust gas can be used as a heat source for the preheating tank 3. An actuator 23 for automatically opening and closing the gas vent valve 13, such as a hydraulic cylinder or a pneumatic cylinder, is connected to the gas vent valve 13.

圧力容器1内をできるだけ所定の処理温度に保持するた
めに、圧力容器1には温度センサー20が設けられ、蒸
気投入弁11にはこれを自動開閉するためのアクチュエ
ータ21、例えば油圧シリンダーあるいは空圧シリンダ
ーが連結されている。上記各アクチュエータ21、23
は制御装置22の出力部に、温度センサー20は制御装
置22の入力部に接続されている。
In order to keep the inside of the pressure vessel 1 at a predetermined processing temperature as much as possible, the pressure vessel 1 is provided with a temperature sensor 20, and the steam injection valve 11 is provided with an actuator 21 for automatically opening and closing the temperature sensor 20, such as a hydraulic cylinder or pneumatic pressure. The cylinders are connected. Each actuator 21, 23
Is connected to the output of the controller 22, and the temperature sensor 20 is connected to the input of the controller 22.

第3図は制御装置22のブロック図を示しており、制御
装置22には温度センサー20からの検出温度の各種範
囲及び時点を判別する判別手段31と、投入弁開閉信号
発信手段32と、積算手段33と、ロック信号発信手段
35等が備えられている。
FIG. 3 shows a block diagram of the control device 22. The control device 22 includes a discrimination means 31 for discriminating various ranges and time points of the temperature detected by the temperature sensor 20, a closing valve opening / closing signal transmission means 32, and an integration. Means 33, lock signal transmitting means 35 and the like are provided.

判別手段31は、保証温度(例えば165℃)より低い
温度範囲か保証温度以上の範囲かを判別すると共に所定
処理温度(170℃)以上になる時点と上記所定処理温
度より△t℃(約1〜2℃)低い最適処理下限温度(1
69℃或は168℃)以下になる時点を判別する機能を
有している。
The discriminating means 31 discriminates whether the temperature range is lower than the guaranteed temperature (for example, 165 ° C.) or is the guaranteed temperature or more, and when the temperature reaches a predetermined processing temperature (170 ° C.) or more and Δt ° C. (about 1 ° C.) from the predetermined processing temperature. 〜2 ℃) Low optimum lower limit temperature (1
It has a function to determine the time when the temperature falls below 69 ° C or 168 ° C.

蒸気投入弁開閉信号発信手段32は、最適処理下限温度
以下になる時点を判別手段32が検出した時に蒸気投入
弁11のアクチュエータ21に開信号を送り、所定処理
温度以上になる時点を判別手段31が検出した時に蒸気
投入弁11をアクチュエータ21に閉信号を送る機能を
有している。
The steam injection valve opening / closing signal transmitting means 32 sends an open signal to the actuator 21 of the steam injection valve 11 when the determination means 32 detects a time point at which the temperature becomes equal to or lower than the optimum processing lower limit temperature, and determines the time point at which the processing temperature becomes equal to or higher than the predetermined processing temperature. Has a function of sending a closing signal to the actuator 21 when the steam injection valve 11 is detected.

積算手段33は分解処理工程中、保証温度以上の温度範
囲の時間のみを積算する機能を有している。
The integrating means 33 has a function of integrating only the time in the temperature range equal to or higher than the guaranteed temperature during the decomposition process.

ロック信号発信手段35は、積算手段33による積算時
間が所定時間(3時間)に達した時に蒸気供給弁11の
アクチュエータ21に閉状態ロック信号を発信しかつガ
ス抜き弁13のアクチュエータ23に開信号を発信する
機能を有している。
The lock signal transmission means 35 transmits a closed state lock signal to the actuator 21 of the steam supply valve 11 and an open signal to the actuator 23 of the gas vent valve 13 when the integration time by the integration means 33 reaches a predetermined time (3 hours). It has the function of transmitting.

また判別手段31には異常警報装置50が接続され、保
証温度以下になる時点を検出するとランプあるいはブザ
ー等で異常警報を発するようになっている。
Further, an abnormality warning device 50 is connected to the discrimination means 31, and an abnormality warning is issued by a lamp, a buzzer or the like when detecting a time point at which the temperature falls below the guaranteed temperature.

さらに判別手段31には異常温度時間積算手段51が接
続され、該積算手段51は保証温度より低い温度が設定
時間、例えば30分以上積算された時に、再度異常警報
装置50に作動信号を送る機能を有している。
Further, an abnormal temperature time integration means 51 is connected to the determination means 31, and the integration means 51 sends a working signal to the abnormality alarm device 50 again when a temperature lower than the guaranteed temperature is integrated for a set time, for example, 30 minutes or more. have.

シアン廃液処理作業について説明する。第1図のシアン
廃液貯槽10のシアン廃液は所定量がポンプ8により予
熱槽3に送られ、そこで100℃位まで加熱される。
The cyan waste liquid treatment work will be described. A predetermined amount of the cyan waste liquid in the cyan waste liquid storage tank 10 shown in FIG. 1 is sent to the preheating tank 3 by the pump 8 and heated there to about 100 ° C.

加熱されたシアン廃液は予熱槽3から例えば予熱槽3と
圧力容器1とのレベル差により圧力容器1内に送られ、
蒸気投入弁11が開かれ、蒸気供給源12からの加熱用
蒸気により所定の処理温度170℃まで加熱される。
The heated cyan waste liquid is sent from the preheating tank 3 into the pressure vessel 1 due to the level difference between the preheating tank 3 and the pressure vessel 1, for example.
The steam injection valve 11 is opened and heated to a predetermined processing temperature of 170 ° C. by the heating steam from the steam supply source 12.

シアン廃液温度が170℃まで達すると、蒸気投入弁1
1が一旦閉じると共に第3図の積算手段33が作動し始
め、熱加水分解によるシアン排液の分解処理工程が始ま
る。上記積算手段33による積算終了時間は例えば3時
間にセットされている。分解処理工程中の熱加水分解に
よりシアン廃液はアンモニアガスと、蟻酸塩並びに金属
酸化物等に分解される。
When the temperature of the cyan waste liquid reaches 170 ° C, the steam injection valve 1
When 1 is once closed, the integrating means 33 in FIG. 3 starts to operate, and the decomposition process of the cyan effluent by thermal hydrolysis starts. The integration end time by the integration means 33 is set to 3 hours, for example. The cyan waste liquid is decomposed into ammonia gas, formate salts, metal oxides and the like by thermal hydrolysis during the decomposition treatment step.

分解処理工程においては、例えば第2図のように自然に
温度が下がるが、点P1 のように最適処理下限温度以下
に下がる時点で、判別手段31により判別され、信号発
信手段32から蒸気投入弁11のアクチュエータ21に
開信号を発し、その信号によりアクチュエータ21が作
動して蒸気投入弁11を開き、加熱用蒸気を圧力容器内
に投入する。それにより圧容器1内の温度は上昇する。
In the decomposition treatment step, for example, as shown in FIG. 2, the temperature naturally decreases, but when it falls below the optimum lower limit temperature of treatment like point P1, it is judged by the judging means 31, and the signal injection means 32 causes the steam injection valve. An open signal is issued to the actuator 21 of No. 11, and the actuator 21 is actuated by the signal to open the steam injection valve 11, and the heating steam is injected into the pressure vessel. As a result, the temperature inside the pressure vessel 1 rises.

そして点P2 のように所定処理温度170℃まで達する
と、今度は信号発信手段32より閉信号が発信され、蒸
気投入弁11を閉じ、圧力容器1内の温度が過上昇を防
ぐ。
Then, when the temperature reaches a predetermined processing temperature of 170 ° C. like point P2, a closing signal is sent from the signal sending means 32 this time, the steam injection valve 11 is closed, and the temperature inside the pressure vessel 1 is prevented from rising excessively.

上記のような温度自動調節は点P3 にも示すように容器
内の温度が最適処理下限以下に下がる毎に繰り返され
る。
The automatic temperature adjustment as described above is repeated every time the temperature inside the container falls below the optimum processing lower limit, as indicated by point P3.

正常運転中は、例えば第2図のP3 以降に仮想線で示す
ように、蒸気投入弁11の開閉調整により概ね所定処理
温度と最適処理下限温度の範囲内に保たれる。そしてそ
の処理時間が積算されて所定時間の3時間に達すると、
第3図の信号発信手段35により蒸気投入弁11のアク
チュエータ21に対して閉状態にロックする信号を送る
と同時に、ガス抜き弁13のアクチュエータ23に対し
て開信号を送り、それにより上記蒸気投入弁11を閉状
態にロックすると共にガス抜き弁13を開く。
During normal operation, for example, as shown by the phantom line after P3 in FIG. 2, the opening / closing adjustment of the steam injection valve 11 keeps the temperature substantially within the range of the predetermined processing temperature and the optimum processing lower limit temperature. Then, when the processing time is added up and reaches a predetermined time of 3 hours,
A signal for locking the actuator 21 of the steam injection valve 11 in a closed state is sent by the signal transmitting means 35 shown in FIG. 3 and at the same time, an open signal is sent to the actuator 23 of the gas vent valve 13 so that the steam injection is performed. The valve 11 is locked in the closed state and the degassing valve 13 is opened.

ところが運転中に、例えば蒸気源(ボイラ)あるいは配
管部損傷等の異常により、第2図のP3 以降の実線で示
すように蒸気投入弁の開放にもかかわらず処理温度が上
昇せず、保証温度より下がる場合(点P4 )がある。こ
の場合はなんらかの異常が発生したと判断し、警報装置
50により異常警報を発し、不具合部分の調整等の目安
とする。このように処理中に、保証温度より下がる状態
が発生した場合には、積算手段33には第2図の保証温
度より低い時間範囲t1 は処理時間に積算されず、保証
温度より高い温度の範囲T1 、T2 のみが積算される。
即ちT1 、T2 の合計が所定時間の3時間に達すると、
第3図の信号発信手段35により蒸気投入弁11のアク
チュエータ21に対して閉状態にロックする信号を送る
と同時に、ガス抜き弁13のアクチュエータ23に対し
て開信号を送り、それにより上記蒸気投入弁11を閉状
態にロックすると共にガス抜き弁13を開く。
However, during operation, due to abnormalities such as damage to the steam source (boiler) or piping, the processing temperature did not rise despite the opening of the steam injection valve, as shown by the solid line after P3 in Fig. 2. There is a case (point P4) when it falls further. In this case, it is determined that some abnormality has occurred, and the alarm device 50 issues an abnormality alarm, which is used as a guide for adjusting the defective portion. In this way, when a temperature lower than the guaranteed temperature occurs during the processing, the time range t1 lower than the guaranteed temperature shown in FIG. Only T1 and T2 are added up.
That is, when the total of T1 and T2 reaches the predetermined time of 3 hours
A signal for locking the actuator 21 of the steam injection valve 11 in a closed state is sent by the signal transmission means 35 of FIG. 3, and at the same time, an open signal is sent to the actuator 23 of the gas vent valve 13, whereby the steam injection is performed. The valve 11 is locked in the closed state and the degassing valve 13 is opened.

また第2図の保証温度より低い状態(t1)が設定時間
(例えば約30分)以上積算手段51により積算された
場合には、シアン廃液処理全サイクルの遅れの原因とも
なりうるため、再度異常警報装置50により警報が発せ
される。この警報は異常原因の確認の目安とすることが
できる。
Further, when the state (t1) lower than the guaranteed temperature shown in FIG. 2 is accumulated by the accumulating means 51 for a set time (for example, about 30 minutes) or more, it may cause a delay in the entire cyan waste liquid treatment cycle. An alarm is issued by the alarm device 50. This alarm can be used as a guide for confirming the cause of the abnormality.

分解処理が終わると、分解処理後の処理済液を圧力容器
1内である程度温度低下した後、排液弁5を開いて処理
済液を冷却槽6に送る。アンモニアガスはガス吸収槽1
4に送られるか、あるいは予熱槽3に送られて予熱に利
用される。
When the decomposition process is completed, the temperature of the decomposed processed liquid is lowered in the pressure vessel 1 to some extent, and then the drain valve 5 is opened to send the processed liquid to the cooling tank 6. Ammonia gas is a gas absorption tank 1
4 or the preheating tank 3 for preheating.

(発明の効果) 以上説明したように本発明によると: (1) 圧力容器1内での加熱保持による分解処理工程にお
いて、保証温度より高い温度の時間のみを積算し、それ
を所定の処理時間とするようにしているので、処理装置
の自動化による処理能力が安定する。
(Effects of the Invention) According to the present invention as described above: (1) In the decomposition treatment step by heating and holding in the pressure vessel 1, only the time of a temperature higher than the guaranteed temperature is integrated, and it is calculated as a predetermined treatment time. As a result, the processing capacity by the automation of the processing device becomes stable.

即ちシアン廃液の分解が十分に行われている時間のみを
所定処理時間として積算するようにしているので、圧力
容器1内での保証温度以下の温度低下の頻度あるいは大
小にかかわらず、常に所定のシアン廃液量を十分に分解
処理できる。
That is, since only the time during which the cyan waste liquid is sufficiently decomposed is integrated as the predetermined processing time, the predetermined time is always maintained regardless of the frequency or the size of the temperature decrease below the guaranteed temperature in the pressure vessel 1. The amount of cyan waste liquid can be decomposed sufficiently.

(2) 所定の処理温度以上になると蒸気投入弁11を閉じ
て温度の過上昇を防ぐようにしているので、無駄にエネ
ルギーを消費することがなくなり、燃料経費を節約でき
る。
(2) When the temperature exceeds a predetermined processing temperature, the steam injection valve 11 is closed to prevent the temperature from rising excessively, so that energy is not wastefully consumed and fuel cost can be saved.

なお保証温度より低い時に異常警報信号を発する異常警
報装置を判別手段に接続しておくと、蒸気投入源(例え
ばボイラ)あるいは蒸気配管系統の異常等の検出にな
り、保全の目安とすることができる。
If an abnormality alarm device that issues an abnormality alarm signal when the temperature is lower than the guaranteed temperature is connected to the determination means, it will detect an abnormality in the steam input source (for example, boiler) or the steam piping system, and can be used as a guideline for maintenance. it can.

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

第1図は本発明を適用したシアン廃液処理装置の全体配
管略図、第2図は分解処理工程中のシアン廃液の温度変
化を示すグラフ、第3図は制御装置内の各手段のブロッ
ク図である。1……圧力容器、2……シアン廃液供給
部、11……蒸気投入弁、12……加熱用蒸気供給源、
20……温度センサー、21……アクチュエータ、22
……制御装置、31……判別手段、32、35……信号
発信手段
FIG. 1 is a schematic diagram of the entire piping of a cyan waste liquid treatment apparatus to which the present invention is applied, FIG. 2 is a graph showing the temperature change of the cyan waste liquid during the decomposition treatment process, and FIG. 3 is a block diagram of each means in the control device. is there. 1 ... Pressure vessel, 2 ... Cyan waste liquid supply section, 11 ... Steam injection valve, 12 ... Heating steam supply source,
20 ... Temperature sensor, 21 ... Actuator, 22
...... Control device, 31 ...... Discrimination means, 32, 35 ...... Signal transmission means

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】圧力容器に蒸気投入弁を介して加熱用蒸気
供給源を接続し、シアン廃液を加熱保持して熱加水分解
するシアン廃液処理装置において、シアン廃液の温度を
検出する温度センサーと、温度センサーによる検出温度
が、保証温度より低い温度範囲か保証温度以上の範囲か
を判別すると共に所定処理温度以上になる時点と最適処
理下限温度以下になる時点を判別する判別手段と、最適
処理下限温度以下になる時点を検出した時に蒸気投入弁
のアクチュエータに開信号を発信し、所定処理温度以上
になる時点を検出した時に閉信号を発信する開閉信号発
信手段と、分解処理開始後保証温度以上の温度の時間の
みを積算する積算手段と、該積算手段による積算時間が
所定時間に達したときに蒸気投入弁のアクチュエータに
閉状態ロック信号を発信する信号発信手段とを備えたこ
とを特徴とするシアン分解処理装置。
1. A temperature sensor for detecting the temperature of a cyan waste liquid in a cyan waste liquid treatment device, wherein a heating steam supply source is connected to a pressure vessel via a steam injection valve to heat-hold and thermally hydrolyze the cyan waste liquid. A determination means for determining whether the temperature detected by the temperature sensor is lower than the guaranteed temperature or higher than the guaranteed temperature, and at the time when the temperature is equal to or higher than the predetermined processing temperature and equal to or lower than the optimum processing lower limit temperature; An open / close signal transmission means that sends an open signal to the actuator of the steam injection valve when the temperature below the lower limit temperature is detected, and a close signal when the time above the predetermined processing temperature is detected, and the guaranteed temperature after the start of the decomposition process. An integrating means for integrating only the time of the above temperature, and a closed state lock signal to the actuator of the steam injection valve when the integrating time by the integrating means reaches a predetermined time. Cyanide decomposition treatment apparatus characterized by comprising a signal transmitter for transmitting.
【請求項2】保証温度より低い温度範囲で警報を発する
異常警装置を判別手段に接続した特許請求の範囲第1項
記載のシアン分解処理装置。
2. The cyan decomposition processing device according to claim 1, further comprising an abnormality alarm device for issuing an alarm in a temperature range lower than the guaranteed temperature, which is connected to the discriminating means.
JP28363887A 1987-11-10 1987-11-10 Cyan waste liquid treatment device Expired - Lifetime JPH0630759B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28363887A JPH0630759B2 (en) 1987-11-10 1987-11-10 Cyan waste liquid treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28363887A JPH0630759B2 (en) 1987-11-10 1987-11-10 Cyan waste liquid treatment device

Publications (2)

Publication Number Publication Date
JPH01123687A JPH01123687A (en) 1989-05-16
JPH0630759B2 true JPH0630759B2 (en) 1994-04-27

Family

ID=17668115

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28363887A Expired - Lifetime JPH0630759B2 (en) 1987-11-10 1987-11-10 Cyan waste liquid treatment device

Country Status (1)

Country Link
JP (1) JPH0630759B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5160637A (en) * 1990-10-19 1992-11-03 Alcan International Limited Apparatus and method for hydrolysis of cyanide-containing liquids

Also Published As

Publication number Publication date
JPH01123687A (en) 1989-05-16

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