JP2005288358A - Electrolytic wastewater treatment system, electrolytic control device, electrolytic wastewater treatment method, program and storage medium - Google Patents

Electrolytic wastewater treatment system, electrolytic control device, electrolytic wastewater treatment method, program and storage medium Download PDF

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JP2005288358A
JP2005288358A JP2004108489A JP2004108489A JP2005288358A JP 2005288358 A JP2005288358 A JP 2005288358A JP 2004108489 A JP2004108489 A JP 2004108489A JP 2004108489 A JP2004108489 A JP 2004108489A JP 2005288358 A JP2005288358 A JP 2005288358A
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electrolytic
electrolysis
tank
residual chlorine
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JP4518826B2 (en
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Kenji Tokumasa
賢治 徳政
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Chugoku Electric Power Co Inc
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<P>PROBLEM TO BE SOLVED: To provide a movable electrolytic wastewater treatment system for automated wastewater treatment, an electrolytic control device, an electrolytic wastewater treatment method, a program and a storage medium. <P>SOLUTION: The electrolytic wastewater treatment system is equipped with a wastewater tank 400 for storing wastewater, an electrolytic cell 500 equipped with a chloride ion tank for storing a solution added to wastewater and containing chloride ions for regulating the concentration of chloride ions of wastewater and an electrolytic device for electrolyzing the solution discharged from a wastewater tank, a residual chlorine measuring instrument 600 for measuring the concentration of residual chlorine of the electrolytic solution in the electrolytic cell during electrolysis, an electrolytic cell water level measuring intrument 530 for measuring the water level of the electrolytic solution of the electrolytic cell and the electrolysis control device 100 for controlling the discharge of the solution from the chloride ion tank, the discharge of the solution from the wastewater tank, electrolytic treatment due to the electrolytic device, the measurement treatment of the residual chlorine measuring instrument and the discharge of the electrolytic from the electrolytic cell. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、電解排水処理システム、電解制御装置、電解排水処理方法、プログラム、及び記憶媒体に関する。   The present invention relates to an electrolytic wastewater treatment system, an electrolytic control device, an electrolytic wastewater treatment method, a program, and a storage medium.

発電所では、発電の様々な過程で多量の水が排水される。例えば、ボイラ・タービン系からのブロー排水、給水処理及び復水脱塩の再生排水、排煙脱硫装置からのブロー排水、冷却装置からの温排水などが挙げられるが、これらの排水は、それぞれ異なる場所で排水され、全ての排水を水質汚濁防止法に基づく排出基準以下にしてから海や河川などの公共用水域に排出しなければならない。   At power plants, large amounts of water are drained during various processes of power generation. For example, blow effluent from boiler / turbine system, regeneration effluent for feed water treatment and condensate demineralization, blow effluent from flue gas desulfurization equipment, warm effluent from cooling equipment, etc., but these effluents are different. It must be drained at the site, and all wastewater must be discharged below public standards based on the Water Pollution Control Law before being discharged into public water areas such as the sea and rivers.

そのような排水処理方法の一つとして、電気分解があり、特にフェライト電極を用いた電気分解装置が、排水のCODを低下させるために用いられてきた(例えば、特許文献1参照)
特開2003−126860号公報
One such wastewater treatment method is electrolysis, and in particular, an electrolyzer using a ferrite electrode has been used to reduce the COD of wastewater (see, for example, Patent Document 1).
JP 2003-126860 A

排水処理を行うために必要な排水設備や装置を運用する際、発電所のような多数の場所で排水が生じる場所では、全ての場所で排水設備や装置を設置するのは、コストやエネルギーの面から、非常に効率が悪い。また、排水処理機能を備えている所でも、多量の排水が生成されたときなどは、その処理に追加の工数を必要とする。   When operating drainage facilities and equipment necessary for wastewater treatment, in places where drainage occurs in many places, such as power plants, installing drainage equipment and equipment in all locations is a cost and energy issue. From the aspect, it is very inefficient. Even where a wastewater treatment function is provided, when a large amount of wastewater is generated, additional man-hours are required for the treatment.

従って、そのような場合、移動式の排水設備や装置が好ましいが、移動式システムを運用する場合、各処理をマニュアルで行っていたのでは効率的でない。   Therefore, in such a case, a mobile drainage facility or apparatus is preferable. However, when a mobile system is operated, it is not efficient if each processing is performed manually.

本発明は以上のような事情に鑑みてなされたものであり、自動化排水処理を実行するための移動可能な電解排水処理システム、自動化排水処理を制御する電解制御装置、自動化排水処理を行うための電解排水処理方法、電解制御装置に自動化排水処理を行わせるためのプログラム及びそのプログラムを読み取り可能に格納した記憶媒体を提供することを目的とする。   The present invention has been made in view of the circumstances as described above, a movable electrolytic wastewater treatment system for performing automated wastewater treatment, an electrolytic control device for controlling automated wastewater treatment, and for performing automated wastewater treatment. It is an object of the present invention to provide an electrolytic wastewater treatment method, a program for causing an electrolytic control apparatus to perform automated wastewater treatment, and a storage medium storing the program in a readable manner.

上記課題を解決すべく、本発明に係る電解排水処理システムは、排水を貯蔵するための排水貯槽と、前記排水に添加することにより、前記排水の塩化物イオン濃度を調節するための塩化物イオンを含む溶液を貯蔵するための塩化物イオン槽と、前記排水槽から排出される溶液を電気分解するための電解装置を備える電解槽と、前記電解槽内の電解溶液の残留塩素濃度を、電気分解中に測定するための残留塩素測定装置と、前記電解槽の電解溶液の水位を測定するための電解槽水位測定装置と、前記塩化物イオン槽からの溶液の排出、前記排水貯槽からの溶液の排出、前記電解装置による電気分解処理、前記残留塩素測定装置の測定処理、前記電解槽水位測定装置の測定処理、及び前記電解槽からの電解溶液の排出、を制御するための電解制御装置と、を備えることとする。なお、前記電解槽内の電解溶液の塩化物濃度は3%以上であることが好ましい。また、前記残留塩素測定装置は、前記電解槽中の電解溶液の残留塩素濃度を測定することとしてもよい。   In order to solve the above problems, an electrolytic wastewater treatment system according to the present invention includes a drainage storage tank for storing wastewater, and chloride ions for adjusting chloride ion concentration of the wastewater by adding to the wastewater. A chloride ion tank for storing a solution containing, an electrolytic tank equipped with an electrolyzer for electrolyzing the solution discharged from the drain tank, and a residual chlorine concentration of the electrolytic solution in the electrolytic tank, Residual chlorine measuring device for measuring during decomposition, electrolytic cell water level measuring device for measuring the water level of the electrolytic solution in the electrolytic cell, discharge of the solution from the chloride ion bath, solution from the drainage storage tank Control for controlling discharge of water, electrolysis treatment by the electrolytic device, measurement processing of the residual chlorine measuring device, measurement processing of the electrolytic cell water level measuring device, and discharge of the electrolytic solution from the electrolytic cell And further comprising a location, a. The chloride concentration of the electrolytic solution in the electrolytic cell is preferably 3% or more. The residual chlorine measuring device may measure the residual chlorine concentration of the electrolytic solution in the electrolytic cell.

本発明に係る電解排水処理システムは、前記塩化物イオン槽及び前記排水貯槽からそれぞれ排出される溶液をろ過するためのろ過器をさらに備えることとしてもよいし、前記電解槽から排出される電解溶液の残留塩素を除去し、処理排水として排出する残留塩素処理装置を備えることとしてもよい。また、本発明に係る電解排水処理システムは、前記電解槽から排出される電解溶液を再び前記電解槽に戻す電解溶液の循環を行うための電解溶液循環装置をさらに備え、前記残留塩素測定装置は、前記電解溶液の循環中に前記電解溶液の残留塩素濃度を測定することにより、前記電解槽内の電解溶液の残留塩素濃度を、電気分解中に測定することとしてもよい。さらに、本発明に係る電解排水処理システムは、酸素を含む気体を前記電解槽内の電解溶液に供給する酸素供給装置をさらに備えることとしてもよいし、システム全体を移動するための移動手段をさらに備えることとしてもよい。   The electrolytic wastewater treatment system according to the present invention may further include a filter for filtering the solution discharged from the chloride ion tank and the wastewater storage tank, respectively, and the electrolytic solution discharged from the electrolytic tank. It is good also as providing the residual chlorine processing apparatus which removes the residual chlorine of this, and discharges | emits as processing waste water. The electrolytic wastewater treatment system according to the present invention further includes an electrolytic solution circulating device for circulating the electrolytic solution that returns the electrolytic solution discharged from the electrolytic bath to the electrolytic bath, and the residual chlorine measuring device is The residual chlorine concentration of the electrolytic solution in the electrolytic bath may be measured during electrolysis by measuring the residual chlorine concentration of the electrolytic solution during circulation of the electrolytic solution. Furthermore, the electrolytic waste water treatment system according to the present invention may further include an oxygen supply device that supplies a gas containing oxygen to the electrolytic solution in the electrolytic cell, and further includes a moving means for moving the entire system. It is good also as providing.

また本発明に係る電解制御装置は、塩化物イオンを貯蔵する塩化物イオン槽と、排水を貯蔵する排水貯槽と、電解装置を備える電解槽と、電解溶液循環装置と、残留塩素測定装置と、を制御する電解制御装置であって、前記塩化物イオン槽及び前記排水貯槽から、それぞれ前記塩化物イオン溶液及び前記排水を、前記電解槽で電気分解するために設定された量だけ、電解槽へ排出させ、前記電解溶液循環装置を作動させて前記電解槽内の電解溶液を排出させ再び前記電解槽に戻す前記電解溶液の循環を行い、前記電解溶液の循環中に、前記残留塩素測定装置を使用して前記電解溶液水の残留塩素濃度を測定し、電気分解するために設定された電流及び電圧に従って前記電解装置に、前記電解溶液を電気分解させ、前記残留塩素濃度が所定の濃度以上になると、前記電解溶液循環装置及び前記電解装置を停止し、前記電解槽から電気分解された前記電解溶液を排出させることを特徴とする。なお、前記電気分解の処理回数が設定されている場合、既に行われた電気分解の回数が所定の回数に達しているならば、前記電気分解処理を終了し、所定の回数に達していないならば、再度電気分解を実施し、電気分解処理の回数が設定されていない場合、前記排水貯槽内の水量を検知し、前記排水貯槽に排水がある場合、再度電気分解を実施し、前記排水貯槽に排水がない場合、前記電気分解処理を終了することとしてもよい。   Moreover, the electrolytic control apparatus according to the present invention includes a chloride ion tank for storing chloride ions, a drainage storage tank for storing wastewater, an electrolytic tank provided with an electrolytic apparatus, an electrolytic solution circulation apparatus, a residual chlorine measuring apparatus, An electrolytic control device for controlling the electrolytic solution from the chloride ion tank and the waste water storage tank to the electrolytic tank by an amount set for electrolyzing the chloride ion solution and the waste water in the electrolytic tank, respectively. The electrolytic solution circulating device is discharged, the electrolytic solution in the electrolytic cell is discharged, the electrolytic solution is circulated back to the electrolytic cell, and the residual chlorine measuring device is circulated during the circulation of the electrolytic solution. The residual chlorine concentration of the electrolytic solution water is measured and electrolyzed by the electrolyzer according to the current and voltage set for electrolysis, and the residual chlorine concentration is a predetermined concentration. It becomes equal to or larger than, the electrolytic solution circulating apparatus and the electrolyzer is stopped, and wherein the discharging said electrolytic solution is electrolyzed from the electrolytic cell. When the number of times of electrolysis is set, if the number of times of electrolysis that has already been performed has reached a predetermined number, the electrolysis process is terminated, and if the number of times of electrolysis has not been reached For example, when the electrolysis is performed again and the number of times of electrolysis is not set, the amount of water in the drainage storage tank is detected, and when there is drainage in the drainage storage tank, the electrolysis is performed again, and the drainage storage tank If there is no drainage, the electrolysis process may be terminated.

さらに、本発明に係る電解排水処理方法は、塩化物イオンを貯蔵する塩化物イオン槽と、排水を貯蔵する排水貯槽と、電解装置を備える電解槽と、電解溶液循環装置と、残留塩素測定装置と、を備える電解排水処理システムにおける電解排水処理方法であって、前記塩化物イオン槽及び前記排水貯槽から、それぞれ前記塩化物イオン溶液及び前記排水を、前記電解槽で電気分解するために設定された量だけ、電解槽へ排出させる工程と、前記電解溶液循環装置を作動させて前記電解槽内の電解溶液を排出させ再び前記電解槽にもどす前記電解溶液の循環を行い、前記電解溶液の循環中に、前記残留塩素測定装置を使用して前記排水の残留塩素濃度を測定する工程と、電気分解するために設定された電流、電圧に従って電解装置に対し前記電解溶液を電気分解させる工程と、前記残留塩素濃度が所定の濃度以上になると、前記電解溶液循環装置及び前記電解装置を停止し、前記電解槽から電気分解された電解溶液を排出させる工程と、を含むこととする。なお、前記電気分解の処理回数が設定されている場合、既に行われた電気分解の回数が所定の回数に達しているならば、前記電気分解処理を終了し、所定の回数に達していないならば、再度電気分解を実施する工程と、電気分解処理の回数が設定されていない場合、前記排水貯槽内の水量を検知し、前記排水貯槽に排水がある場合、再度電気分解を実施し、前記排水貯槽に排水がない場合、前記電気分解処理を終了する工程を、前記電解排水処理方法にさらに含ませることとしてもよい。   Furthermore, an electrolytic wastewater treatment method according to the present invention includes a chloride ion tank for storing chloride ions, a wastewater storage tank for storing wastewater, an electrolytic tank provided with an electrolytic device, an electrolytic solution circulation device, and a residual chlorine measuring device. And an electrolytic wastewater treatment method in an electrolytic wastewater treatment system, wherein the chloride ion solution and the wastewater are respectively electrolyzed in the electrolytic tank from the chloride ion tank and the wastewater storage tank. A step of discharging the electrolytic solution to the electrolytic bath, and circulating the electrolytic solution by operating the electrolytic solution circulating device to discharge the electrolytic solution in the electrolytic bath and return it to the electrolytic bath again. During the process of measuring the residual chlorine concentration of the wastewater using the residual chlorine measuring device, the electrolysis apparatus is electrolyzed according to the current and voltage set for electrolysis. A step of electrolyzing the liquid, and a step of stopping the electrolytic solution circulation device and the electrolytic device and discharging the electrolyzed electrolytic solution from the electrolytic cell when the residual chlorine concentration exceeds a predetermined concentration. To include. When the number of times of electrolysis is set, if the number of times of electrolysis that has already been performed has reached a predetermined number, the electrolysis process is terminated, and if the number of times of electrolysis has not been reached For example, if the number of times of electrolysis treatment is not set and the step of performing electrolysis again, the amount of water in the drainage storage tank is detected, and when there is drainage in the drainage storage tank, the electrolysis is performed again, When there is no drainage in the drainage storage tank, the step of terminating the electrolysis treatment may be further included in the electrolytic wastewater treatment method.

本発明に係るプログラムは、塩化物イオンを貯蔵する塩化物イオン槽と、排水を貯蔵する排水貯槽と、電解装置を備える電解槽と、電解溶液循環装置と、残留塩素測定装置と、を備える電解排水処理システムを制御する電解制御装置に、電解排水処理方法を行わせるためのプログラムであって、電解制御装置に、前記塩化物イオン槽及び前記排水貯槽から、それぞれ前記塩化物イオン溶液及び前記排水を、前記電解槽で電気分解するために設定された量だけ、電解槽へ排出させる工程と、前記電解溶液循環装置を作動させて前記電解槽内の電解溶液を排出させ再び前記電解槽に戻す前記電解溶液の循環を行い、前記電解溶液の循環中に、前記残留塩素測定装置を使用して前記排水の残留塩素濃度を測定する工程と、電気分解するために設定された電流、電圧に従って前記電解装置に前記電解溶液を電気分解させる工程と、前記残留塩素濃度が所定の濃度以上になると、前記電気供給及び前記電解溶液循環装置の作動を停止し、前記電解槽から電気分解された電解溶液を排出させる工程と、を実行させることを特徴とする。なお、前記電気分解の処理回数が設定されている場合、既に行われた電気分解の回数が所定の回数に達しているならば、前記電気分解処理を終了し、所定の回数に達していないならば、再度電気分解を実施する工程と、電気分解処理の回数が設定されていない場合、前記排水貯槽内の水量を検知し、前記排水貯槽に排水がある場合、再度電気分解を実施し、前記排水貯槽に排水がない場合、前記電気分解処理を終了する工程を、電解制御装置にさらに実行させることとしてもよい。   The program according to the present invention includes a chloride ion tank that stores chloride ions, a drainage storage tank that stores wastewater, an electrolytic tank that includes an electrolytic device, an electrolytic solution circulation device, and a residual chlorine measuring device. A program for causing an electrolytic control apparatus for controlling a wastewater treatment system to perform an electrolytic wastewater treatment method, wherein the electrolytic control apparatus includes the chloride ion solution and the wastewater from the chloride ion tank and the wastewater storage tank, respectively. Is discharged to the electrolytic cell by an amount set for electrolysis in the electrolytic cell, and the electrolytic solution circulating device is operated to discharge the electrolytic solution in the electrolytic cell and return it to the electrolytic cell again. The electrolytic solution is circulated, and during the electrolytic solution circulation, the residual chlorine measuring device is used to measure the residual chlorine concentration of the wastewater, and is set for electrolysis. A step of electrolyzing the electrolytic solution in the electrolytic device according to a current and a voltage, and when the residual chlorine concentration exceeds a predetermined concentration, the operation of the electric supply and the electrolytic solution circulation device is stopped, and And a step of discharging the electrolyzed electrolytic solution. When the number of times of electrolysis is set, if the number of times of electrolysis that has already been performed has reached a predetermined number, the electrolysis process is terminated, and if the number of times of electrolysis has not been reached For example, if the number of times of electrolysis treatment is not set and the step of performing electrolysis again, the amount of water in the drainage storage tank is detected, and when there is drainage in the drainage storage tank, the electrolysis is performed again, When there is no drainage in the drainage storage tank, the step of terminating the electrolysis process may be further performed by the electrolysis control device.

本発明にかかる記憶媒体は、前記プログラムを、電解制御装置によって読み取り可能に格納している。   The storage medium according to the present invention stores the program so as to be readable by the electrolysis control device.

本発明により、自動化排水処理を実行するための移動可能な電解排水処理システム、自動化排水処理を制御する電解制御装置、自動化排水処理を行うための電解排水処理方法、電解制御装置に自動化排水処理を行わせるためのプログラム及びそのプログラムを読み取り可能に格納した記憶媒体を提供することが可能になった。   According to the present invention, a movable electrolytic wastewater treatment system for performing automated wastewater treatment, an electrolytic control device for controlling automated wastewater treatment, an electrolytic wastewater treatment method for performing automated wastewater treatment, and an automated wastewater treatment for an electrolytic control device. It has become possible to provide a program to be executed and a storage medium storing the program in a readable manner.

以下、本発明の好ましい実施の形態につき、添付図面を用いて詳細に説明する。なお、本発明の目的、特徴、利点、及びそのアイデアは、本明細書の記載により、当業者には明らかであり、本明細書の記載から、当業者であれば、容易に本発明を再現できる。以下に記載された発明の実施の形態及び具体的に実施例などは、本発明の好ましい実施態様を示すものであり、例示又は説明のために示されているのであって、本発明をそれらに限定するものではない。本明細書で開示されている本発明の意図並びに範囲内で、本明細書の記載に基づき、様々な改変並びに修飾ができることは、当業者にとって明らかである。   Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. The objects, features, advantages, and ideas of the present invention will be apparent to those skilled in the art from the description of the present specification, and those skilled in the art can easily reproduce the present invention from the description of the present specification. it can. The embodiments and specific examples of the invention described below show preferred embodiments of the present invention, and are shown for illustration or explanation. It is not limited. It will be apparent to those skilled in the art that various modifications and variations can be made based on the description of the present specification within the spirit and scope of the present invention disclosed herein.

===電解排水処理システムの構成図===
図1は本発明の一実施例として説明する電解排水処理システム1000の構成図を示す。
=== Configuration diagram of electrolytic wastewater treatment system ===
FIG. 1 shows a configuration diagram of an electrolytic wastewater treatment system 1000 described as an embodiment of the present invention.

図1に示すように、本発明に係る電解排水処理システム1000は、塩化物イオンを含む溶液を貯蔵する塩化物イオン槽である海水貯槽200、20%塩化ナトリウム水溶液タンク300、排水を貯蔵する排水貯槽400、各貯槽及びタンク内の溶液又は排水を汲み上げるそれぞれのポンプである海水注入ポンプ210、塩化ナトリウム水溶液注入ポンプ310、排水処理ポンプ410、各貯槽及びタンクから排出された溶液又は排水をろ過するろ過器800、海水貯槽200、20%塩化ナトリウム水溶液タンク300、及び排水貯槽400から排出される溶液を電気分解する電解槽500、電解槽500から排出された電解溶液を再び電解槽に戻すための電解溶液循環装置としての電解溶液処理ポンプ510、酸素を含む気体を供給する酸素供給装置としてのバブリング用コンプレッサー520、電解槽の電解溶液の水位を測定する電解槽水位測定装置530、電解槽500の電解溶液の残留塩素濃度を測定する残留塩素測定装置600、電解槽500から排出された電解溶液の残留塩素を除去する残留塩素処理器700、そして電解排水処理システム1000を制御する電解制御装置100などを備えている。   As shown in FIG. 1, an electrolytic wastewater treatment system 1000 according to the present invention includes a seawater storage tank 200 that is a chloride ion tank that stores a solution containing chloride ions, a 20% sodium chloride aqueous solution tank 300, and a wastewater that stores wastewater. The tank 400, the seawater injection pump 210, the sodium chloride aqueous solution injection pump 310, the wastewater treatment pump 410, which are the pumps for pumping up the solution or waste water in each storage tank and tank, and the solution or waste water discharged from each storage tank and tank are filtered. Electrolyzer 500 for electrolyzing the solution discharged from filter 800, seawater storage tank 200, 20% sodium chloride aqueous solution tank 300, and drainage storage tank 400, and for returning the electrolytic solution discharged from electrolytic tank 500 back to the electrolytic tank Electrolytic solution treatment pump 510 as an electrolytic solution circulation device, supplying gas containing oxygen From the bubbling compressor 520 as an element supply device, the electrolytic cell water level measuring device 530 that measures the water level of the electrolytic solution in the electrolytic cell, the residual chlorine measuring device 600 that measures the residual chlorine concentration of the electrolytic solution in the electrolytic cell 500, and the electrolytic cell 500 A residual chlorine treatment device 700 that removes residual chlorine from the discharged electrolytic solution, an electrolysis control device 100 that controls the electrolytic wastewater treatment system 1000, and the like are provided.

電解制御装置100は、電線1、2、3を介してそれぞれ海水注入ポンプ210、塩化ナトリウム水溶液注入ポンプ310、排水処理ポンプ410に接続していて、電線4、5、6は、それぞれ電解槽排水バルブ710、残留塩素測定装置600、電解槽水位測定装置530に接続しており、電線7、8は、それぞれ電解溶液処理ポンプ510、バブリング用コンプレッサー520に接続しており、電線9は電解槽500に接続している。   The electrolysis control apparatus 100 is connected to a seawater injection pump 210, a sodium chloride aqueous solution injection pump 310, and a wastewater treatment pump 410 via electric wires 1, 2, and 3, respectively. The valve 710, the residual chlorine measuring device 600, and the electrolytic cell water level measuring device 530 are connected. The electric wires 7 and 8 are connected to the electrolytic solution treatment pump 510 and the bubbling compressor 520, respectively. The electric wire 9 is connected to the electrolytic cell 500. Connected to.

海水注入ポンプ210は、海水貯槽200と配管20で接続しており、配管20には弁220が設けられ、海水貯槽200の海水を配管21に汲み上げることができる。塩化ナトリウム水溶液注入ポンプ310は、20%塩化ナトリウム水溶液タンク300と配管30で接続し、その配管30には弁320が設けられ、20%塩化ナトリウム水溶液タンク300の塩化物イオンを含んだ溶液を配管31に汲み上げることができる。排水処理ポンプ410は排水貯槽400と配管40で接続し、その配管40には弁420が設けられ、配管41に排水貯槽400の排水を汲み上げることができる。配管21、31、そして41は、配管10に結合している。配管10は、配管11を介してろ過器800に接続している。すなわち、ろ過器800には、海水、塩化物イオンを含んだ溶液、及び排水が配管10、11を通って流入する。   The seawater injection pump 210 is connected to the seawater storage tank 200 by a pipe 20, and the pipe 20 is provided with a valve 220, and the seawater in the seawater storage tank 200 can be pumped into the pipe 21. The sodium chloride aqueous solution injection pump 310 is connected to a 20% sodium chloride aqueous solution tank 300 by a pipe 30, and the pipe 30 is provided with a valve 320, and a solution containing chloride ions in the 20% sodium chloride aqueous solution tank 300 is piped. Can be pumped to 31. The drainage treatment pump 410 is connected to the drainage storage tank 400 by a pipe 40, and a valve 420 is provided in the pipe 40, and the drainage of the drainage storage tank 400 can be pumped into the pipe 41. The pipes 21, 31 and 41 are coupled to the pipe 10. The pipe 10 is connected to the filter 800 via the pipe 11. That is, seawater, a solution containing chloride ions, and drainage flow into the filter 800 through the pipes 10 and 11.

電解槽500は、酸素を含む気体を供給する酸素供給装置としてのバブリング用コンプレッサー520と、電解槽の電解溶液の水位を測定する電解槽水位測定装置530と、電解槽500から排出された排水を電解溶液処理ポンプ510を用いて再び電解槽500に戻すことができる循環路の配管13とを備えている。この配管13は、ろ過器800から排水を取り入れるための配管12、電解槽500からの排水を残留塩素処理器700に排出するための配管14、に接続するとともに、電解溶液処理ポンプ510が設置されていて、残留塩素濃度測定装置600とチューブ60を介して接続している。電解槽排水バルブ710は、配管14に設置されていて、電解槽500からの電解溶液が残留塩素処理器700への排出を制御する。残留塩素処理器700は、電解槽500からの電解溶液の残留塩素を除去し、処理排水として排出する。   The electrolytic cell 500 includes a bubbling compressor 520 as an oxygen supply device that supplies a gas containing oxygen, an electrolytic cell water level measuring device 530 that measures the water level of the electrolytic solution in the electrolytic cell, and the waste water discharged from the electrolytic cell 500. And a circulation line pipe 13 that can be returned to the electrolytic cell 500 by using an electrolytic solution treatment pump 510. This pipe 13 is connected to the pipe 12 for taking in the waste water from the filter 800 and the pipe 14 for discharging the waste water from the electrolytic cell 500 to the residual chlorinator 700, and an electrolytic solution treatment pump 510 is installed. The residual chlorine concentration measuring device 600 is connected to the tube 60 through the tube 60. The electrolytic cell drain valve 710 is installed in the pipe 14 and controls discharge of the electrolytic solution from the electrolytic cell 500 to the residual chlorine processor 700. The residual chlorine treatment device 700 removes residual chlorine from the electrolytic solution from the electrolytic cell 500 and discharges it as treated waste water.

===電解制御装置操作パネル===
図2は本発明の一実施例として説明する電解制御装置100の操作パネルを示す。
=== Electrolytic control device operation panel ===
FIG. 2 shows an operation panel of the electrolysis control apparatus 100 described as an embodiment of the present invention.

図2に示すように、電解制御装置100の操作パネルは、各装置の稼働状況を示す表示器等(操作パネル上部)と電解排水処理装置1000の現在状況を表示する画面表示ディスプレイ(操作パネル下部)で構成されている。   As shown in FIG. 2, the operation panel of the electrolysis control apparatus 100 includes a display unit (upper part of the operation panel) indicating the operation status of each apparatus and a screen display (lower part of the operation panel) that displays the current state of the electrolytic waste water treatment apparatus 1000. ).

操作パネル上部の長方形は、電解制御装置100が制御している各装置の稼働状況を示す表示器等である。例えば、電解処理ポンプ510が稼働しているときは、電解処理ポンプ表示器が点灯する。この表示器が電解処理ポンプ510を手動で制御できるように、ボタン式(ボタンを押すことでON/OFFを制御する)にすることもできる。   The rectangle at the top of the operation panel is a display or the like indicating the operating status of each apparatus controlled by the electrolysis control apparatus 100. For example, when the electrolytic treatment pump 510 is operating, the electrolytic treatment pump indicator is turned on. It can also be a button type (ON / OFF is controlled by pressing a button) so that the display can manually control the electrolytic treatment pump 510.

また、操作パネル下部の画面表示ディスプレイ左側には、モニターされた電解排水処理装置1000の現在状況が表示される。例えば、電流、電圧の欄には、それぞれ1A、1Vのような現在の電気供給状況が表示される。   Further, the current status of the monitored electrolytic wastewater treatment apparatus 1000 is displayed on the left side of the screen display display at the bottom of the operation panel. For example, the current supply status such as 1A and 1V is displayed in the current and voltage columns, respectively.

操作パネル下部の画面表示ディスプレイ右側には、電解制御装置100において、排出量プログラム、終了処理プログラム、条件設定プログラムの設定を行う時に、各プログラムの設定内容が表示される。また、一旦設定したプログラムは、プログラム番号によって保存することができ、その番号で再び呼び出せるようにしてもよい。   On the right side of the screen display at the bottom of the operation panel, when the electrolysis control apparatus 100 sets the discharge amount program, the end processing program, and the condition setting program, the setting contents of each program are displayed. The program once set can be stored by the program number and can be called again by the number.

===各種条件設定===
電解槽500に排出する排水の塩化物濃度が3%以上になるように、排水貯槽400、20%塩化ナトリウム水溶液タンク300、海水貯槽200からの排出量を決定する。通常、排水貯槽400の排水と20%塩化ナトリウム水溶液タンク300の溶液を混合して塩化物濃度が3%以上になればよい。排水中の塩化物濃度は、一般的には不明なので、20%塩化ナトリウム水溶液を全体の溶液量の15%添加するようにしておくとよい。
=== Various condition settings ===
The discharge amounts from the drainage storage tank 400, the 20% sodium chloride aqueous solution tank 300, and the seawater storage tank 200 are determined so that the chloride concentration of the drainage discharged to the electrolytic tank 500 is 3% or more. Usually, the waste water in the waste water storage tank 400 and the solution in the 20% sodium chloride aqueous solution tank 300 may be mixed so that the chloride concentration becomes 3% or more. Since the chloride concentration in the waste water is generally unknown, it is preferable to add a 20% sodium chloride aqueous solution to 15% of the total solution amount.

電解排水処理を繰り返す処理回数をプログラムする。処理回数は任意の数でよいが、この設定をブランクにしておくことで、排水貯槽400の排水がなくなるまでという設定が行われる。電解処理の自動化の面からは、ブランクにしておくのが好ましい。 Program the number of times to repeat electrolytic wastewater treatment. The number of treatments may be any number, but by setting this setting to be blank, setting is made until the drainage of the drainage storage tank 400 is exhausted. From the viewpoint of automation of the electrolytic treatment, it is preferable to leave it blank.

電気分解の条件は特に限定しないが、定電流で、電流密度10〜1000A/dmであることが好ましく、経済的観点からは、20〜300A/dmであることがさらに好ましい。その際、電圧は1V以上になるように制御するのが好ましい。 Conditions of the electrolysis is not particularly limited, a constant current is preferably a current density 10~1000A / dm 2, from the economic point of view, further preferably 20~300A / dm 2. At that time, it is preferable to control the voltage to be 1 V or more.

===電解排水処理システムの処理手順===
本発明の一実施例として説明する電解排水処理システム1000の処理の手順を、図3のフローチャートを参考にしながら、詳細に述べる。
=== Procedure of electrolytic wastewater treatment system ===
The procedure of the electrolytic wastewater treatment system 1000 described as an embodiment of the present invention will be described in detail with reference to the flowchart of FIG.

まず、電解排水処理システム1000の電解制御装置100の電源を入れる。   First, the electrolysis control apparatus 100 of the electrolytic wastewater treatment system 1000 is turned on.

海水海水量注入ポンプ210、塩化ナトリウム水溶液注入ポンプ310、排水処理ポンプ410が、海水、20%塩化ナトリウム水溶液、及び排水を、事前に設定された量だけ汲み上げ、配管10、11を通じて、ろ過器800に注入する。これらの溶液に固形物(例えば、木片などの海のゴミ)が含まれていることがあるので、ろ過器800にてその固形物を除去した後、配管12、13を通じて電解槽500に注入する(S101)。   Seawater seawater injection pump 210, sodium chloride aqueous solution injection pump 310, and wastewater treatment pump 410 pump seawater, 20% aqueous sodium chloride solution, and wastewater by a preset amount, and filter 800 through pipes 10 and 11. Inject. Since these solutions may contain solids (for example, marine debris such as wood chips), the solids are removed by the filter 800 and then injected into the electrolytic cell 500 through the pipes 12 and 13. (S101).

次に、電解制御装置100は電解装置(例えば、電極)540による電気分解処理を制御する。具体的には、電解制御装置100は、電線9を利用して電解槽500に備えられた電解装置540に、電気分解するために設定された電流、電圧に従って電気を供給し、電気分解を始める(S102)。また、電解溶液処理ポンプ510を作動させることにより、電解槽500から排出される電解液を配管13を用いて循環させる(S102)。その上、バブリング用コンプレッサー520も作動させ、電解槽500の酸素濃度を高めて電気分解を促進するために、酸素を含む気体を電解溶液に供給する。電解溶液処理ポンプ510によって配管13内を循環している電解槽500の電解溶液の残留塩素濃度を残留塩素測定装置600を用いて測定する(S103)。こうして残留塩素濃度を測定し、測定した濃度が所定値以上かどうか判断する(S104)ことによって、実施例1〜4に記載されているように、電気分解の終了点を判断することができる。即ち、電解制御装置100は、所定値未満の場合は、再度塩素濃度を測定し、所定値以上の場合は、電気分解と電解溶液処理ポンプ510を停止する(S105)。そして、電気分解された電解槽500の溶液を残留塩素処理器700に排出するため電解排水バルブ710を開栓する(S106)と、配管13を循環していた電解液は、配管14を通って残留塩素処理器700に排出される。電解制御装置100は、電解槽水位測定装置530によって検知される電解槽500の水位が所定の水位(例えば、電解槽が空であることを示す0)に達したかどうか確認し(S107)、電解槽500内の溶液が全て排出されたことを電解槽水位測定装置530によって確認したら、電解排水バルブ710を閉栓し(S108)、電解溶液の残留塩素処理器700への排出は停止する。   Next, the electrolysis control apparatus 100 controls the electrolysis process by the electrolysis apparatus (for example, electrode) 540. Specifically, the electrolysis control apparatus 100 supplies electricity to the electrolysis apparatus 540 provided in the electrolysis tank 500 using the electric wire 9 according to the current and voltage set for electrolysis, and starts electrolysis. (S102). Further, by operating the electrolytic solution treatment pump 510, the electrolytic solution discharged from the electrolytic cell 500 is circulated using the pipe 13 (S102). In addition, the bubbling compressor 520 is also operated to supply oxygen-containing gas to the electrolytic solution in order to increase the oxygen concentration in the electrolytic cell 500 and promote electrolysis. The residual chlorine concentration of the electrolytic solution in the electrolytic bath 500 circulating in the pipe 13 is measured using the residual chlorine measuring device 600 by the electrolytic solution treatment pump 510 (S103). By measuring the residual chlorine concentration and determining whether the measured concentration is equal to or higher than a predetermined value (S104), the end point of the electrolysis can be determined as described in Examples 1 to 4. That is, the electrolysis control apparatus 100 measures the chlorine concentration again when it is less than the predetermined value, and stops the electrolysis and the electrolytic solution treatment pump 510 when it is greater than the predetermined value (S105). Then, when the electrolytic drain valve 710 is opened to discharge the electrolyzed electrolytic cell 500 solution to the residual chlorinator 700 (S106), the electrolytic solution circulating in the pipe 13 passes through the pipe 14. It is discharged to the residual chlorine processor 700. The electrolysis control device 100 confirms whether or not the water level of the electrolyzer 500 detected by the electrolyzer water level measuring device 530 has reached a predetermined water level (for example, 0 indicating that the electrolyzer is empty) (S107), When the electrolytic cell water level measuring device 530 confirms that all the solution in the electrolytic cell 500 has been discharged, the electrolytic drain valve 710 is closed (S108), and the discharge of the electrolytic solution to the residual chlorinator 700 is stopped.

残留塩素処理器700では、排出された電解液中の残留塩素を、例えば、カーボンファイバー、ゼオライト、活性炭等を用いて除去する。これにより、塩素臭や配管などに用いられる金属の腐食の原因となる酸化力のある形の残留塩素、例えば、遊離残留塩素(次亜塩素酸や次亜塩素酸イオン)、結合残留塩素(アンモニアや有機性窒素化合物等と結合した塩素)を取り除くことができ、環境に対してより好ましい処理排水を排出することができる。   In the residual chlorine treatment device 700, residual chlorine in the discharged electrolyte solution is removed using, for example, carbon fiber, zeolite, activated carbon or the like. As a result, residual chlorine in an oxidative form that causes corrosion of metals used in pipes, etc., such as free residual chlorine (hypochlorous acid and hypochlorite ions), combined residual chlorine (ammonia) And chlorine combined with organic nitrogen compounds, etc., and wastewater that is more favorable to the environment can be discharged.

電解排水処理が完了すると、電解制御装置100は、終了処理が処理回数で設定されているプログラムかどうか判断する(S109)。もし、処理回数で判断するプログラムであるならば、現在の処理回数が設定した回数に到達したかどうか判断し(S110)、設定した回数に到達していなければ、回数を1つ増加させ、再び上記電解排水処理を繰り返すために、排水貯槽400に排水が存在するか判断する(S111)。これは、排水が存在していないのに、電解排水処理が実施されるのを防ぐためである。到達していた場合は、電解制御装置100の電源を切り、電解排水処理を終了する。一方、処理回数で判断しないプログラムの場合は、排水貯槽400の排水が無くなるまで電解排水処理を実施するので、排水貯槽400に排水が存在するかどうか確認する(S111)。排水が存在するならば、再び上記電解排水処理を繰り返すために、S101に戻り、排水が存在しないならば、電解排水処理を終了し、電解制御装置100の電源を切る。   When the electrolytic drainage process is completed, the electrolysis control apparatus 100 determines whether the end process is a program set by the number of processes (S109). If it is a program for judging by the number of processing times, it is judged whether or not the current number of processing times has reached the set number of times (S110). If the set number of times has not been reached, the number of times is increased by one, and again. In order to repeat the electrolytic waste water treatment, it is determined whether there is waste water in the waste water storage tank 400 (S111). This is to prevent the electrolytic waste water treatment from being carried out even though there is no waste water. When it has reached, the power of the electrolysis control device 100 is turned off, and the electrolytic drainage treatment is finished. On the other hand, in the case of a program that does not judge based on the number of treatments, since the electrolytic drainage treatment is performed until the drainage of the drainage storage tank 400 is exhausted, it is confirmed whether or not there is drainage in the drainage storage tank 400 (S111). If there is drainage, the process returns to S101 to repeat the electrolytic drainage process again. If there is no drainage, the electrolytic drainage process is terminated and the electrolysis control apparatus 100 is turned off.

===電解排水処理システムの移動手段===
電解排水処理システムを移動可能にするための手段として、電解排水処理システムを搭載することができ、原動機等の動力を用いて任意の目的地まで移動することが可能な乗り物又は運搬具であれば何でもよい。例えば、貨物運搬用の自動車、飛行機、船舶、などが挙げられるが、これらに限定されない。
=== Moving means of electrolytic wastewater treatment system ===
As a means for making the electrolytic wastewater treatment system movable, an electrolytic wastewater treatment system can be mounted, and any vehicle or vehicle that can move to any destination using power such as a prime mover Anything Examples thereof include, but are not limited to, a car for carrying cargo, an airplane, a ship, and the like.

海水を含む排水(クラゲを溶解した溶液でCODを304mg/L含有する)4リットルに、Cannon電極(Φ32×600L)テスト機で電流を48A通電を行い経時的に水質測定と電解時間毎のCODを計測した。その結果を表1及び図4に示す。

Figure 2005288358
Wastewater containing seawater (solution containing jellyfish and containing 304 mg / L of COD) was energized with a Cannon electrode (Φ32 x 600 L) tester with a current of 48 A to measure water quality over time and COD for each electrolysis time Was measured. The results are shown in Table 1 and FIG.
Figure 2005288358

表1及び図4に示すように、残留塩素が1,000(mg/L)以上になると、目標処理COD 50(mg/L)以下になることが確認できる。すなわち、残留塩素が1,000(mg/L)以上になった時に、電気分解を止めるように制御することができる。   As shown in Table 1 and FIG. 4, it can be confirmed that when the residual chlorine is 1,000 (mg / L) or more, the target treatment COD 50 (mg / L) or less. That is, it can be controlled to stop the electrolysis when the residual chlorine becomes 1,000 (mg / L) or more.

排水(煙道水洗水3.4リットルにNaCl20%0.6リットルを含有する)4リットル(NaCl濃度3%)に、Cannon電極(Φ32×600L)テスト機で電流を48A通電を行い経時的に水質測定と電解時間毎のアンモニアを計測した。それらの結果を表2及び図5に示す。

Figure 2005288358
Drainage (contains 0.6 liters of NaCl 20% in 3.4 liters of flue flush water) 4 liters (NaCl concentration 3%) with a Cannon electrode (Φ32 × 600L) tester with 48 A current applied over time Ammonia was measured for each water quality measurement and electrolysis time. The results are shown in Table 2 and FIG.
Figure 2005288358

表2及び図5に示すように、残留塩素が100(mg/L)以上になると,目標処理アンモニア 50(mg/L)以下にすることが確認できる。すなわち、残留塩素が100(mg/L)になった時に,電気分解を止めるように制御することができる。   As shown in Table 2 and FIG. 5, when the residual chlorine is 100 (mg / L) or more, it can be confirmed that the target treated ammonia is 50 (mg / L) or less. That is, it can be controlled to stop electrolysis when the residual chlorine reaches 100 (mg / L).

排水(煙道水洗水3.7リットルにNaCl20%0.3リットルを含有する)4リットル(NaCl濃度1.5%)に、Cannon電極(Φ32×600L)テスト機で電流を48A通電を行い経時的に水質測定と電解時間毎のアンモニアを計測した。それらの結果を表3及び図6に示す。

Figure 2005288358
Drainage (containing 0.1% NaCl 20% in 3.7 liters of flue flush water) 4 liters (NaCl concentration 1.5%) was energized with a Cannon electrode (Φ32 × 600L) tester at 48A. In particular, water quality was measured and ammonia was measured at every electrolysis time. The results are shown in Table 3 and FIG.
Figure 2005288358

表3及び図6に示すように、NaCl濃度1.5%の場合、3%に比べ処理時間がかかり、効率的にアンモニアの処理ができないことが確認できる。   As shown in Table 3 and FIG. 6, when the NaCl concentration is 1.5%, it takes more time than 3%, and it can be confirmed that the ammonia treatment cannot be performed efficiently.

排水(煙道水洗水1.7リットルに、水1.7リットルとNaCl20%0.6リットルを含有する)4リットル(NaCl濃度3%に調整した2倍希釈排水)に、Cannon電極(Φ32×600L)テスト機で電流を48A通電を行い経時的に水質測定と電解時間毎のアンモニアを計測した。それらの結果を表4及び図7に示す。

Figure 2005288358
Drainage (containing 1.7 liters of flue flush water, 1.7 liters of water and 0.6 liters of NaCl 20%) 4 liters (double diluted effluent adjusted to 3% NaCl concentration), Cannon electrode (Φ32 × 600L) A current of 48 A was applied with a test machine, and water quality was measured over time and ammonia was measured at every electrolysis time. The results are shown in Table 4 and FIG.
Figure 2005288358

表4及び図7に示すように、2倍希釈しNaCl濃度3%の場合、残留塩素が100(mg/L)になるように電解を制御すれば、希釈しない場合より効率的なアンモニア処理を行うことが確認できる。   As shown in Table 4 and FIG. 7, when the electrolysis is controlled so that the residual chlorine is 100 (mg / L) when diluted twice and the NaCl concentration is 3%, more efficient ammonia treatment can be achieved than without dilution. I can confirm that I do it.

上記実施例1〜4により、電解槽500に注入する溶液は、塩化物濃度が3%以上であることが望ましく、残留塩素濃度は、COD処理を目的とする場合は、1000(mg/L)を所定の濃度とし、アンモニア処理を目的とする場合は、100(mg/L)を所定の濃度とすることが好ましい。もし、COD処理とアンモニア処理の両方を目的とする場合は、1000(mg/L)を所定の濃度とすることが好ましい。   According to the above Examples 1 to 4, the solution injected into the electrolytic cell 500 desirably has a chloride concentration of 3% or more, and the residual chlorine concentration is 1000 (mg / L) for the purpose of COD treatment. Is a predetermined concentration, and 100 (mg / L) is preferably a predetermined concentration when ammonia treatment is intended. If both COD treatment and ammonia treatment are intended, 1000 (mg / L) is preferably set to a predetermined concentration.

本発明の一実施例として説明する電解排水処理システム1000の構成を示す図である。It is a figure which shows the structure of the electrolytic waste water treatment system 1000 demonstrated as one Example of this invention. 本発明の一実施例として説明する電解制御装置100の操作パネルを示す図である。It is a figure which shows the operation panel of the electrolysis control apparatus 100 demonstrated as one Example of this invention. 本発明の一実施例として説明する電解排水処理システム1000の処理手順を示すフローチャートである。It is a flowchart which shows the process sequence of the electrolytic waste water treatment system 1000 demonstrated as one Example of this invention. 実施例1の、電解時間に対する残留塩素及びCODの計測結果を示す図である。It is a figure which shows the measurement result of the residual chlorine with respect to the electrolysis time of Example 1, and COD. 実施例2の、電解時間に対する残留塩素及びCODの計測結果を示す図である。It is a figure which shows the measurement result of the residual chlorine with respect to the electrolysis time of Example 2, and COD. 実施例3の、電解時間に対する残留塩素及びCODの計測結果を示す図である。It is a figure which shows the measurement result of the residual chlorine with respect to electrolysis time of Example 3, and COD. 実施例4の、電解時間に対する残留塩素及びCODの計測結果を示す図である。It is a figure which shows the measurement result of the residual chlorine and COD with respect to the electrolysis time of Example 4.

符号の説明Explanation of symbols

1〜9 電線
10〜14 配管
20〜21 配管
30〜31 配管
40〜41 配管
60 チューブ
100 電解制御装置
200 海水貯槽
210 海水注入ポンプ
220 弁
300 20%塩化ナトリウム水溶液タンク
310 塩化ナトリウム水溶液注入ポンプ
320 弁
400 排水貯槽
410 排水処理ポンプ
420 弁
500 電解槽
510 電解溶液処理ポンプ
520 バブリング用コンプレッサー
530 電解槽水位測定装置
540 電解装置
600 残留塩素測定装置
700 残留塩素処理器
710 電解排水バルブ
1000 電解排水処理システム
1-9 Electric wire 10-14 Piping 20-21 Piping 30-31 Piping 40-41 Piping 60 Tube 100 Electrolytic control device 200 Seawater storage tank 210 Seawater infusion pump 220 Valve 300 20% sodium chloride aqueous solution tank 310 Sodium chloride aqueous solution infusion pump 320 Valve 400 Wastewater storage tank 410 Wastewater treatment pump 420 Valve 500 Electrolytic tank 510 Electrolytic solution treatment pump 520 Compressor for bubbling 530 Electrolyzer water level measuring device 540 Electrolytic device 600 Residual chlorine measuring device 700 Residual chlorine processor 710 Electrolytic drainage valve 1000 Electrolytic wastewater treatment system

Claims (15)

排水を貯蔵するための排水貯槽と、
前記排水に添加することにより、前記排水の塩化物イオン濃度を調節するための塩化物イオンを含む溶液を貯蔵するための塩化物イオン槽と、
前記排水槽から排出される溶液を電気分解するための電解装置を備える電解槽と、
前記電解槽内の電解溶液の残留塩素濃度を、電気分解中に測定するための残留塩素測定装置と、
前記電解槽の電解溶液の水位を測定するための電解槽水位測定装置と、
前記塩化物イオン槽からの溶液の排出、前記排水貯槽からの溶液の排出、前記電解装置による電気分解処理、前記残留塩素測定装置の測定処理、前記電解槽水位測定装置の測定処理、及び前記電解槽からの電解溶液の排出、を制御するための電解制御装置と、
を備える電解排水処理システム。
A waste water storage tank for storing waste water;
A chloride ion tank for storing a solution containing chloride ions for adjusting the chloride ion concentration of the wastewater by adding to the wastewater;
An electrolysis tank comprising an electrolysis device for electrolyzing the solution discharged from the drainage tank;
A residual chlorine measuring device for measuring the residual chlorine concentration of the electrolytic solution in the electrolytic cell during electrolysis;
An electrolyzer water level measuring device for measuring the water level of the electrolytic solution in the electrolyzer;
Discharge of the solution from the chloride ion tank, discharge of the solution from the waste water storage tank, electrolysis treatment by the electrolytic device, measurement processing of the residual chlorine measuring device, measurement processing of the electrolytic bath water level measuring device, and the electrolysis An electrolysis control device for controlling discharge of the electrolytic solution from the tank;
An electrolytic wastewater treatment system comprising:
前記電解槽内の電解溶液の塩化物濃度が3%以上であることを特徴とする請求項1に記載の電解排水処理システム。   The electrolytic waste water treatment system according to claim 1, wherein a chloride concentration of the electrolytic solution in the electrolytic cell is 3% or more. 前記残留塩素測定装置は、前記電解槽中の電解溶液の残留塩素濃度を測定することによって、前記電気分解の終了点を決定することを特徴とする請求項1又は2に記載の電解排水処理システム。   The electrolytic wastewater treatment system according to claim 1 or 2, wherein the residual chlorine measuring device determines an end point of the electrolysis by measuring a residual chlorine concentration of an electrolytic solution in the electrolytic cell. . 前記塩化物イオン槽及び前記排水貯槽からそれぞれ排出される溶液をろ過するためのろ過器を備えることを特徴とする請求項1から3のいずれかに記載の電解排水処理システム。   The electrolytic wastewater treatment system according to any one of claims 1 to 3, further comprising a filter for filtering a solution discharged from each of the chloride ion tank and the wastewater storage tank. 前記電解槽から排出される電解溶液の残留塩素を除去し、処理排水として排出する残留塩素処理装置を備えることを特徴とする請求項1から4のいずれかに記載の電解排水処理システム。   5. The electrolytic waste water treatment system according to claim 1, further comprising a residual chlorine treatment device that removes residual chlorine from the electrolytic solution discharged from the electrolytic tank and discharges the residual chlorine as treated waste water. 前記電解槽から排出される電解溶液を再び前記電解槽に戻す電解溶液の循環を行うための電解溶液循環装置を備え、
前記残留塩素測定装置が、前記電解溶液の循環中に前記電解溶液の残留塩素濃度を測定することにより、前記電解槽内の電解溶液の残留塩素濃度を、電気分解中に測定することを特徴とする請求項1から5のいずれかに記載の電解排水処理システム。
An electrolytic solution circulation device for circulating the electrolytic solution that returns the electrolytic solution discharged from the electrolytic cell to the electrolytic cell again,
The residual chlorine measuring device measures the residual chlorine concentration of the electrolytic solution in the electrolytic cell during electrolysis by measuring the residual chlorine concentration of the electrolytic solution during circulation of the electrolytic solution. The electrolytic waste water treatment system according to any one of claims 1 to 5.
酸素を含む気体を前記電解槽内の電解溶液に供給する酸素供給装置を備えることを特徴とする請求項1から6のいずれかに記載の電解排水処理システム。   The electrolytic waste water treatment system according to any one of claims 1 to 6, further comprising an oxygen supply device that supplies a gas containing oxygen to the electrolytic solution in the electrolytic cell. システム全体を移動するための移動手段を備えていることを特徴とする請求項1〜7のいずれかに記載の電解排水処理システム。   The electrolytic wastewater treatment system according to any one of claims 1 to 7, further comprising moving means for moving the entire system. 塩化物イオンを貯蔵する塩化物イオン槽と、排水を貯蔵する排水貯槽と、電解装置を備える電解槽と、電解溶液循環装置と、残留塩素測定装置と、を制御する電解制御装置であって、
前記塩化物イオン槽及び前記排水貯槽から、それぞれ前記塩化物イオン溶液及び前記排水を、前記電解槽で電気分解するために設定された量だけ、電解槽へ排出させ、
前記電解溶液循環装置を作動させて前記電解槽内の電解溶液を排出させ再び前記電解槽に戻す前記電解溶液の循環を行い、
前記電解溶液の循環中に、前記残留塩素測定装置を使用して前記電解溶液水の残留塩素濃度を測定し、
電気分解するために設定された電流及び電圧に従って前記電解装置に、前記電解溶液を電気分解させ、
前記残留塩素濃度が所定の濃度以上になると、前記電解溶液循環装置及び前記電解装置を停止し、
前記電解槽から電気分解された前記電解溶液を排出させる電解制御装置。
An electrolytic control device for controlling a chloride ion tank for storing chloride ions, a waste water storage tank for storing waste water, an electrolytic tank equipped with an electrolytic device, an electrolytic solution circulation device, and a residual chlorine measuring device,
From the chloride ion tank and the waste water storage tank, respectively, the chloride ion solution and the waste water are discharged into the electrolytic tank by an amount set for electrolysis in the electrolytic tank,
Operate the electrolytic solution circulation device to discharge the electrolytic solution in the electrolytic tank and circulate the electrolytic solution back to the electrolytic tank again,
During the circulation of the electrolytic solution, the residual chlorine concentration is measured using the residual chlorine measuring device,
Causing the electrolyzer to electrolyze the electrolytic solution according to a current and voltage set for electrolysis,
When the residual chlorine concentration is equal to or higher than a predetermined concentration, the electrolytic solution circulation device and the electrolytic device are stopped,
An electrolysis control device for discharging the electrolyzed electrolytic solution from the electrolytic cell.
電気分解処理の回数が設定されている場合、既に行われた電気分解の回数が所定の回数に達しているならば、前記電気分解処理を終了し、所定の回数に達していないならば、再度電気分解を実施し、
電気分解処理の回数が設定されていない場合、前記排水貯槽内の水量を検知し、前記排水貯槽に排水がある場合、再度電気分解を実施し、前記排水貯槽に排水がない場合、前記電気分解処理を終了する、
ことを特徴とする請求項9に記載の電解制御装置。
When the number of times of electrolysis is set, if the number of times of electrolysis that has already been performed has reached a predetermined number of times, the electrolysis process is terminated. Perform electrolysis,
When the number of times of electrolysis treatment is not set, the amount of water in the drainage storage tank is detected, and when there is drainage in the drainage storage tank, electrolysis is performed again, and when there is no drainage in the drainage storage tank, the electrolysis End the process,
The electrolysis control apparatus according to claim 9.
塩化物イオンを貯蔵する塩化物イオン槽と、排水を貯蔵する排水貯槽と、電解装置を備える電解槽と、電解溶液循環装置と、残留塩素測定装置と、を備える電解排水処理システムにおける電解排水処理方法であって、
前記塩化物イオン槽及び前記排水貯槽から、それぞれ前記塩化物イオン溶液及び前記排水を、前記電解槽で電気分解するために設定された量だけ、電解槽へ排出させる工程と、
前記電解溶液循環装置を作動させて前記電解槽内の電解溶液を排出させ再び前記電解槽にもどす前記電解溶液の循環を行い、前記電解溶液の循環中に、前記残留塩素測定装置を使用して前記排水の残留塩素濃度を測定する工程と、
電気分解するために設定された電流、電圧に従って電解装置に対し前記電解溶液を電気分解させる工程と、
前記残留塩素濃度が所定の濃度以上になると、前記電解溶液循環装置及び前記電解装置を停止し、前記電解槽から電気分解された電解溶液を排出させる工程と、
を含むことを特徴とする電解排水処理方法。
Electrolytic wastewater treatment in an electrolytic wastewater treatment system comprising a chloride ion tank for storing chloride ions, a wastewater storage tank for storing wastewater, an electrolytic tank provided with an electrolytic device, an electrolytic solution circulation device, and a residual chlorine measuring device A method,
Discharging the chloride ion solution and the waste water from the chloride ion tank and the waste water storage tank to the electrolytic tank by an amount set for electrolysis in the electrolytic tank, respectively;
Operate the electrolytic solution circulation device to discharge the electrolytic solution in the electrolytic cell and return the electrolytic solution to the electrolytic cell again. During the circulation of the electrolytic solution, the residual chlorine measuring device is used. Measuring the residual chlorine concentration of the waste water;
Electrolyzing the electrolytic solution to an electrolyzer according to a current and voltage set for electrolysis;
When the residual chlorine concentration is equal to or higher than a predetermined concentration, stopping the electrolytic solution circulation device and the electrolytic device, and discharging the electrolytic solution electrolyzed from the electrolytic cell;
Electrolytic waste water treatment method characterized by including.
電気分解処理の回数が設定されている場合、既に行われた電気分解の回数が所定の回数に達しているならば、前記電気分解処理を終了し、所定の回数に達していないならば、再度電気分解を実施する工程と、
電気分解処理の回数が設定されていない場合、前記排水貯槽内の水量を検知し、前記排水貯槽に排水がある場合、再度電気分解を実施し、前記排水貯槽に排水がない場合、前記電気分解処理を終了する工程と、
を含むことを特徴とする請求項11に記載の電解排水処理方法。
When the number of times of electrolysis is set, if the number of times of electrolysis that has already been performed has reached a predetermined number of times, the electrolysis process is terminated. Performing the electrolysis; and
When the number of times of electrolysis treatment is not set, the amount of water in the drainage storage tank is detected, and when there is drainage in the drainage storage tank, electrolysis is performed again, and when there is no drainage in the drainage storage tank, the electrolysis A step of ending the processing;
The electrolytic waste water treatment method according to claim 11, comprising:
塩化物イオンを貯蔵する塩化物イオン槽と、排水を貯蔵する排水貯槽と、電解装置を備える電解槽と、電解溶液循環装置と、残留塩素測定装置と、を備える電解排水処理システムを制御する電解制御装置に、電解排水処理方法を行わせるためのプログラムであって、電解制御装置に、
前記塩化物イオン槽及び前記排水貯槽から、それぞれ前記塩化物イオン溶液及び前記排水を、前記電解槽で電気分解するために設定された量だけ、電解槽へ排出させる工程と、
前記電解溶液循環装置を作動させて前記電解槽内の電解溶液を排出させ再び前記電解槽に戻す前記電解溶液の循環を行い、前記電解溶液の循環中に、前記残留塩素測定装置を使用して前記排水の残留塩素濃度を測定する工程と、
電気分解するために設定された電流、電圧に従って前記電解装置に前記電解溶液を電気分解させる工程と、
前記残留塩素濃度が所定の濃度以上になると、前記電気供給及び前記電解溶液循環装置の作動を停止し、前記電解槽から電気分解された電解溶液を排出させる工程と、
を実行させるプログラム。
Electrolysis for controlling an electrolytic wastewater treatment system comprising a chloride ion tank for storing chloride ions, a drainage storage tank for storing wastewater, an electrolytic tank provided with an electrolytic device, an electrolytic solution circulation device, and a residual chlorine measuring device. A program for causing a control device to perform an electrolytic wastewater treatment method.
Discharging the chloride ion solution and the waste water from the chloride ion tank and the waste water storage tank to the electrolytic tank by an amount set for electrolysis in the electrolytic tank, respectively;
Operate the electrolytic solution circulation device to discharge the electrolytic solution in the electrolytic cell and return the electrolytic solution to the electrolytic cell again, and use the residual chlorine measuring device during the circulation of the electrolytic solution. Measuring the residual chlorine concentration of the waste water;
Electrolyzing the electrolytic solution in the electrolyzer according to a current and voltage set for electrolysis;
When the residual chlorine concentration is equal to or higher than a predetermined concentration, stopping the operation of the electricity supply and the electrolytic solution circulation device, and discharging the electrolyzed electrolytic solution from the electrolytic cell;
A program that executes
前記電解制御装置に、
電気分解処理の回数が設定されている場合、既に行われた電気分解の回数が所定の回数に達しているならば、前記電気分解処理を終了し、所定の回数に達していないならば、再度電気分解を実施する工程と、
電気分解処理の回数が設定されていない場合、前記排水貯槽内の水量を検知し、前記排水貯槽に排水がある場合、再度電気分解を実施し、前記排水貯槽に排水がない場合、前記電気分解処理を終了する工程と、
をさらに実行させることを特徴とする請求項13に記載のプログラム。
In the electrolysis control device,
When the number of times of electrolysis is set, if the number of times of electrolysis that has already been performed has reached a predetermined number of times, the electrolysis process is terminated. Performing the electrolysis; and
When the number of times of electrolysis treatment is not set, the amount of water in the drainage storage tank is detected, and when there is drainage in the drainage storage tank, electrolysis is performed again, and when there is no drainage in the drainage storage tank, the electrolysis A step of ending the processing;
14. The program according to claim 13, further comprising:
請求項14又は15に記載のプログラムを、電解制御装置によって読み取り可能に格納した記憶媒体。   The storage medium which stored the program of Claim 14 or 15 so that reading by the electrolysis control apparatus was possible.
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CN103172145B (en) * 2013-04-10 2014-06-18 江苏龙腾工程设计有限公司 Rotary-type wastewater treating device
WO2016167271A1 (en) * 2015-04-17 2016-10-20 三菱重工環境・化学エンジニアリング株式会社 Hypochlorous acid supply device and boiler waste-water treatment method
CN105618005A (en) * 2016-03-29 2016-06-01 山西大学 Preparation method of magnetic chitosan
CN106277180A (en) * 2016-08-24 2017-01-04 哈尔滨工程大学 A kind of intensified by ultrasonic wave photoelectrocatalysis processes containing heavy metal and the device of persistent organic pollutant wastewater

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06480A (en) * 1992-06-16 1994-01-11 Kenji Nakamura Treatment of waste water
JPH07299465A (en) * 1994-05-10 1995-11-14 Nippon Shokubai Co Ltd Electrolytic treatment of waste water and anode used therefor
JPH08164391A (en) * 1994-12-14 1996-06-25 Matsushita Seiko Co Ltd Sterilized water forming machine
JPH08281271A (en) * 1995-04-14 1996-10-29 Osaka Prefecture Treating device of waste dyeing water and treatment of the same
JPH08308909A (en) * 1995-05-16 1996-11-26 Matsushita Seiko Co Ltd Sterilization liquor generating apparatus
JP2000308887A (en) * 1999-04-27 2000-11-07 Matsushita Electric Ind Co Ltd Water purifying device
WO2001030706A1 (en) * 1999-10-28 2001-05-03 Kazuto Hashizume Improved method and apparatus for water treatment
JP2001353489A (en) * 2000-06-14 2001-12-25 Babcock Hitachi Kk Nh3-containing waste water treatment device and treatment method
JP2002153878A (en) * 2000-11-20 2002-05-28 Fuji Electric Co Ltd Water quality maintenance equipment
JP2003103261A (en) * 2001-09-28 2003-04-08 Amano Corp Electrolytic washing water and method and apparatus for making the same
JP2003126860A (en) * 2001-10-22 2003-05-07 Omega:Kk Method and apparatus for treatment of waste liquid or waste water
JP2003225672A (en) * 2002-02-04 2003-08-12 Sanyo Electric Co Ltd Water treatment equipment
JP2004057926A (en) * 2002-07-29 2004-02-26 Sanyo Electric Co Ltd Wastewater treatment method and wastewater treatment equipment

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06480A (en) * 1992-06-16 1994-01-11 Kenji Nakamura Treatment of waste water
JPH07299465A (en) * 1994-05-10 1995-11-14 Nippon Shokubai Co Ltd Electrolytic treatment of waste water and anode used therefor
JPH08164391A (en) * 1994-12-14 1996-06-25 Matsushita Seiko Co Ltd Sterilized water forming machine
JPH08281271A (en) * 1995-04-14 1996-10-29 Osaka Prefecture Treating device of waste dyeing water and treatment of the same
JPH08308909A (en) * 1995-05-16 1996-11-26 Matsushita Seiko Co Ltd Sterilization liquor generating apparatus
JP2000308887A (en) * 1999-04-27 2000-11-07 Matsushita Electric Ind Co Ltd Water purifying device
WO2001030706A1 (en) * 1999-10-28 2001-05-03 Kazuto Hashizume Improved method and apparatus for water treatment
JP2001353489A (en) * 2000-06-14 2001-12-25 Babcock Hitachi Kk Nh3-containing waste water treatment device and treatment method
JP2002153878A (en) * 2000-11-20 2002-05-28 Fuji Electric Co Ltd Water quality maintenance equipment
JP2003103261A (en) * 2001-09-28 2003-04-08 Amano Corp Electrolytic washing water and method and apparatus for making the same
JP2003126860A (en) * 2001-10-22 2003-05-07 Omega:Kk Method and apparatus for treatment of waste liquid or waste water
JP2003225672A (en) * 2002-02-04 2003-08-12 Sanyo Electric Co Ltd Water treatment equipment
JP2004057926A (en) * 2002-07-29 2004-02-26 Sanyo Electric Co Ltd Wastewater treatment method and wastewater treatment equipment

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008212816A (en) * 2007-03-02 2008-09-18 West Japan Railway Technos Corp Wastewater treatment apparatus and method
JP2015503442A (en) * 2011-12-22 2015-02-02 スリーエム イノベイティブ プロパティズ カンパニー Filtration media containing metal sulfides
US9663387B2 (en) 2011-12-22 2017-05-30 3M Innovative Properties Company Filtration medium comprising a metal sulfide
WO2013176032A1 (en) * 2012-05-25 2013-11-28 三菱重工環境・化学エンジニアリング株式会社 Ammonia treatment system
JP2014000563A (en) * 2012-05-25 2014-01-09 Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd Ammonia treatment system
CN104379512A (en) * 2012-05-25 2015-02-25 三菱重工环境·化学工程株式会社 Ammonia treatment system
CN104379512B (en) * 2012-05-25 2017-06-13 三菱重工环境·化学工程株式会社 ammonia treatment system
KR101757525B1 (en) * 2012-05-25 2017-07-12 미츠비시 쥬코 칸쿄 카가쿠 엔지니어링 가부시키가이샤 Ammonia treatment system
CN103787466A (en) * 2014-01-24 2014-05-14 中南大学 Pulse enrichment device and method for quick treatment of high-concentration heavy metal wastewater
CN108439550A (en) * 2018-04-12 2018-08-24 长江大学 A kind of rotor stirred type three-dimensional electrochemical reaction unit

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