JP2003010850A - Electrolytic water making apparatus - Google Patents

Electrolytic water making apparatus

Info

Publication number
JP2003010850A
JP2003010850A JP2001196527A JP2001196527A JP2003010850A JP 2003010850 A JP2003010850 A JP 2003010850A JP 2001196527 A JP2001196527 A JP 2001196527A JP 2001196527 A JP2001196527 A JP 2001196527A JP 2003010850 A JP2003010850 A JP 2003010850A
Authority
JP
Japan
Prior art keywords
water
salt water
concentrated salt
water supply
electrolytic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001196527A
Other languages
Japanese (ja)
Inventor
Masato Miyaji
正人 宮地
Nobuo Achinami
信夫 阿知波
Kyoichiro Yoshida
恭一郎 吉田
Masahiro Fujita
昌浩 藤田
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.)
Hoshizaki Electric Co Ltd
Original Assignee
Hoshizaki Electric Co 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 Hoshizaki Electric Co Ltd filed Critical Hoshizaki Electric Co Ltd
Priority to JP2001196527A priority Critical patent/JP2003010850A/en
Publication of JP2003010850A publication Critical patent/JP2003010850A/en
Pending legal-status Critical Current

Links

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an electrolytic water making apparatus capable of rapidly starting the formation of electrolytic water having a desired effective chlorine concentration by simple constitution. SOLUTION: The electrolytic water making apparatus is equipped with an electrolytic cell 10 for electrolyzing supplied dilute saline water to make electrolytic water, a water supply channel 30 for continuously supplying water to the electrolytic cell 10 and a concentrated saline water supply channel 40 for supplying the concentrated saline water stored in the concentrated saline water tank 50 arranged under the electrolytic cell 10 to the water supply channel 30 by the operation of an electromotive pump 60. An electric control circuit 70 responds to the operation of a forming switch 71 to control the start and stop of the formation of electrolytic water but measures a time by a timer 72 during the stop of the formation of electrolytic water and operates the electromotive pump 60 at each time when a predetermined time is elapsed to send a predetermined amount of the concentrated saline water in a concentrated saline water tank 50 to the water supply channel 30 and the electrolytic cell 10 within a concentrated saline water supply passage 40 to perfectly fill the concentrated saline water supply passage 40 with concentrated saline water.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、希塩水を電気分解
して例えば殺菌などに用いる電解水を生成する電解水生
成装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolyzed water producing apparatus for electrolyzing dilute salt water to produce electrolyzed water used for sterilization or the like.

【0002】[0002]

【従来の技術】従来、この種の装置は、直流電圧が印加
される一対の電極を収容してなり、供給された希塩水を
電気分解して電解水を生成する電解槽と、電気的に開閉
制御可能な電磁バルブを介装してなり該電磁バルブの開
状態にて電解槽に連続的に水を供給する給水路と、電気
的に作動制御可能な電動ポンプを介装してなり該電動ポ
ンプの作動により電解槽の下方に配設した濃塩水タンク
内に貯えた濃塩水を給水路に供給する濃塩水供給路と、
電解水の生成を指示するための生成指示手段と、生成指
示手段により電解水の生成が指示されているとき電解槽
に所定濃度の希塩水を供給するように電磁バルブを開状
態に保つとともに電動ポンプを作動制御する電気制御回
路とを備え、電解槽にて所定濃度の希塩水を電気分解す
ることにより所定の有効塩素濃度を有する電解水を生成
するようにしている。
2. Description of the Related Art Conventionally, this type of apparatus contains a pair of electrodes to which a DC voltage is applied, and an electrolytic cell for electrolyzing the supplied dilute salt water to produce electrolyzed water An electromagnetic valve that can be controlled to open and close is provided, and a water supply channel that continuously supplies water to the electrolytic cell when the electromagnetic valve is open, and an electrically-operated electrically controllable pump are provided. A concentrated salt water supply passage for supplying the concentrated salt water stored in the concentrated salt water tank disposed below the electrolytic cell to the water supply passage by the operation of the electric pump,
Generation instruction means for instructing the generation of electrolyzed water, and an electromagnetic valve that keeps the electromagnetic valve open so as to supply dilute salt water of a predetermined concentration to the electrolytic cell when the generation instruction means instructs generation of electrolyzed water. An electric control circuit for controlling the operation of the pump is provided, and electrolytic water having a predetermined effective chlorine concentration is generated by electrolyzing dilute salt water having a predetermined concentration in the electrolytic cell.

【0003】[0003]

【発明が解決しようとする課題】上記従来装置において
は、電解水の生成の停止中、電解槽より下流の希塩水
が、時間の経過とともに自重により濃塩水タンク側に逆
流して濃塩水供給路中に溜ることがあった。この場合、
電解水の生成を再開したとき、しばらくの間は、電動ポ
ンプを作動させても、濃塩水供給路から給水路に上記逆
流して溜った希塩水しか供給できず濃塩水を供給できな
いことになる。したがって、このとき、電解槽に供給す
る希塩水の濃度を所望の濃度まで速やかに上げることが
できなかったため、所望の有効塩素濃度を有する電解水
の生成を速やかに再開することができなかった。一方、
これを回避するために濃塩水供給管に逆止弁を介装する
と、電動ポンプ内に侵入した空気を抜くための空気抜き
路なども必要となり構成が複雑になる。
In the above-mentioned conventional apparatus, while the production of electrolyzed water is stopped, the dilute salt water downstream from the electrolyzer flows backward to the concentrated salt water tank side due to its own weight with the passage of time, and the concentrated salt water supply passage is provided. There was something that could accumulate inside. in this case,
When the generation of electrolyzed water is restarted, even if the electric pump is operated for a while, only the diluted salt water accumulated by the above-mentioned backward flow from the concentrated salt water supply passage can be supplied, and the concentrated salt water cannot be supplied. . Therefore, at this time, the concentration of the dilute salt water supplied to the electrolytic cell could not be quickly raised to the desired concentration, and therefore the production of the electrolytic water having the desired effective chlorine concentration could not be restarted promptly. on the other hand,
If a check valve is provided in the concentrated salt water supply pipe in order to avoid this, an air vent passage for exhausting air that has entered the electric pump is also required, which complicates the configuration.

【0004】[0004]

【発明の概要】本発明は上記問題に対処しようとするも
ので、その目的は、所望の有効塩素濃度を有する電解水
の生成を速やかに開始する電解水生成装置を簡単な構成
により提供することにある。
SUMMARY OF THE INVENTION The present invention is intended to solve the above problems, and an object thereof is to provide an electrolyzed water producing apparatus for promptly starting production of electrolyzed water having a desired effective chlorine concentration with a simple structure. It is in.

【0005】本発明の第1の構成上の特徴は、前記電解
槽、給水路、濃塩水供給路、生成指示手段、及び電気制
御回路を備えた電解水生成装置において、前記電気制御
回路が、電解水の生成の停止中、所定時間毎に電動ポン
プを作動させて濃塩水タンク内の濃塩水を所定量だけ濃
塩水供給路中にて給水路及び電解槽側に送ることにあ
る。これによれば、電解水の生成の停止中、所定時間毎
に濃塩水タンク内の濃塩水を濃塩水供給路中にて給水路
及び電解槽側に送るようにしているため、時間の経過と
ともに濃塩水タンク側に逆流して濃塩水供給路中に溜っ
た希塩水を給水路より下流に送り返して、濃塩水供給路
中を常に濃塩水により満たしておくことが可能となる。
これにより、電解水の生成の再開時、濃塩水供給路から
給水路に速やかに濃塩水を供給して電解槽に供給する希
塩水の濃度を速やかに所望の濃度まで上げることが可能
となるため、速やかに所望の有効塩素濃度を有する電解
水の生成を再開できるようになる。この場合、逆止弁、
空気抜き路なども必要ないため、装置の構成も簡単であ
る。
A first structural feature of the present invention is that in the electrolyzed water producing apparatus provided with the electrolyzer, the water supply passage, the concentrated salt water supply passage, the production instructing means, and the electric control circuit, the electric control circuit comprises: The electric pump is operated every predetermined time while the production of the electrolyzed water is stopped, and the predetermined amount of the concentrated salt water in the concentrated salt water tank is sent to the water supply passage and the electrolytic cell side in the concentrated salt water supply passage. According to this, since the concentrated salt water in the concentrated salt water tank is sent to the water supply path and the electrolytic cell side in the concentrated salt water supply path at predetermined time intervals while the generation of the electrolyzed water is stopped, the time elapses. The diluted salt water that flows back to the concentrated salt water tank side and collects in the concentrated salt water supply path can be sent back to the downstream side of the water supply path to constantly fill the concentrated salt water supply path with the concentrated salt water.
As a result, when the generation of electrolyzed water is restarted, it is possible to rapidly supply the concentrated salt water from the concentrated salt water supply passage to the water supply passage to quickly raise the concentration of the diluted salt water supplied to the electrolytic cell to the desired concentration. Therefore, the generation of electrolyzed water having a desired effective chlorine concentration can be promptly restarted. In this case, the check valve,
The structure of the device is simple because there is no need for an air vent passage.

【0006】本発明の第2の構成上の特徴は、前記第1
の特徴を有する電気制御回路において、電気制御回路
が、前記電解水の生成の停止中における電動ポンプの作
動が完了する毎に、前記電磁バルブを開いて前記電解槽
内を水で満たすことにある。これによれば、電解水の生
成の停止中、前記電動ポンプの作動により濃塩水が電解
槽より下流まで送られた場合にも、同電動ポンプの作動
の完了後に電解槽内が水で満たされる。したがって、電
解水の生成の再開時に電解槽内が濃塩水で満たされてい
て両電極間に過度の電流が流れることが回避されるた
め、電極の劣化が抑制される。
A second structural feature of the present invention is the above first feature.
In the electric control circuit having the above feature, the electric control circuit opens the electromagnetic valve to fill the inside of the electrolytic cell with water every time the operation of the electric pump is completed while the generation of the electrolytic water is stopped. . According to this, even when concentrated salt water is sent to the downstream of the electrolytic cell by the operation of the electric pump while the production of the electrolytic water is stopped, the electrolytic cell is filled with water after the operation of the electric pump is completed. . Therefore, it is possible to prevent the electrolytic bath from being filled with concentrated salt water and flowing an excessive current between the electrodes when the generation of the electrolyzed water is restarted, so that the deterioration of the electrodes is suppressed.

【0007】本発明の第3の構成上の特徴は、前記電解
槽、給水路、濃塩水供給路、及び生成指示手段、並びに
生成指示手段により電解水の生成が指示されているとき
電解槽に所定濃度の希塩水を供給するように電磁バルブ
を開状態に保つとともに電動ポンプを作動制御する電気
制御回路とを備えた電解水生成装置において、濃塩水供
給路に、濃塩水タンクから給水路に供給される濃塩水を
一時的に貯える濃塩水貯留部を介装したことにある。こ
れによれば、電解水の生成の停止中、電解槽より下流の
希塩水が時間の経過とともに濃塩水タンク側に逆流して
濃塩水供給路中に溜った場合においても、濃塩水供給路
中には濃塩水貯留部によって比較的多量の濃塩水が貯え
られているため、濃塩水供給路中の塩水の濃度は比較的
高いまま保たれる。したがって、電解水の生成の再開
時、速やかに所望の有効塩素濃度を有する電解水の生成
を開始できる。この場合、逆止弁、空気抜き路などが必
要ないため、装置の構成も比較的簡単である。
A third structural feature of the present invention is that the electrolytic cell, the water supply channel, the concentrated salt water supply channel, the production instructing means, and the electrolytic cell when the production instructing means instructs the production of electrolyzed water. In an electrolyzed water generator equipped with an electric control circuit that keeps an electromagnetic valve open to supply a predetermined concentration of diluted salt water and controls the operation of an electric pump, from a concentrated salt water supply channel to a water supply channel from a concentrated salt water tank. This is because the concentrated salt water storage unit that temporarily stores the supplied concentrated salt water is installed. According to this, even when the diluted salt water downstream of the electrolytic cell flows backward to the concentrated salt water tank side and accumulates in the concentrated salt water supply passage with the passage of time while the production of the electrolytic water is stopped, Since a relatively large amount of concentrated salt water is stored in the concentrated salt water storage section, the concentration of salt water in the concentrated salt water supply channel is kept relatively high. Therefore, when the production of electrolyzed water is restarted, the production of electrolyzed water having a desired effective chlorine concentration can be promptly started. In this case, since a check valve, an air vent passage, etc. are not required, the structure of the device is relatively simple.

【0008】[0008]

【発明の実施の形態】a.第1の実施形態 以下、本発明の第1の実施形態について図面を参照して
説明する。図1に示した電解水生成装置は、電解槽1
0、直流電源装置20、給水路30、濃塩水供給路4
0、濃塩水タンク50、電動ポンプ60、及び電気制御
回路70を備えている。
DETAILED DESCRIPTION OF THE INVENTION a. First Embodiment Hereinafter, a first embodiment of the present invention will be described with reference to the drawings. The electrolyzed water generator shown in FIG.
0, DC power supply 20, water supply channel 30, concentrated salt water supply channel 4
0, a concentrated salt water tank 50, an electric pump 60, and an electric control circuit 70.

【0009】電解槽10は、内部が隔膜11によって一
対の電極室12,13に区画されており、各電極室1
2,13内に一対の電極14,15をそれぞれ収容して
いる。両電極14,15間には直流電源装置20によっ
て直流電圧が印加されるようになっており、この電圧印
加によって電解槽10は各電極室12,13内に供給さ
れた希塩水を電気分解して酸性及びアルカリ性の電解水
を生成する。各電極室12,13にて生成された電解水
は、それぞれ導出管16,17を通して外部に注出され
る。直流電源装置20から両電極14,15への電圧の
供給路には、分流器21を介して、両電極14,15間
を流れる電流を計測する電流計22が接続されている。
The inside of the electrolytic cell 10 is divided into a pair of electrode chambers 12 and 13 by a diaphragm 11, and each electrode chamber 1
A pair of electrodes 14 and 15 are housed in 2 and 13, respectively. A DC voltage is applied between the electrodes 14 and 15 by a DC power supply device 20, and the electrolytic cell 10 electrolyzes the diluted salt water supplied into the electrode chambers 12 and 13 by the voltage application. To produce acidic and alkaline electrolyzed water. The electrolyzed water generated in the electrode chambers 12 and 13 is discharged to the outside through the outlet pipes 16 and 17, respectively. An ammeter 22 that measures a current flowing between the electrodes 14 and 15 is connected to a voltage supply path from the DC power supply device 20 to the electrodes 14 and 15 via a shunt 21.

【0010】給水路30は、図示しない外部給水源から
圧送される水を電解槽10の各電極室12,13に導く
管である。給水路30には、電気的に開閉制御されて開
状態にて前記外部給水源の水を電解槽10に供給すると
ともに閉状態にて前記水を閉止する電磁バルブ31と、
給水路30を通って電解槽10に供給される水の量を検
出する流量センサ32とが介装されている。
The water supply passage 30 is a pipe for guiding water pumped from an external water supply source (not shown) to the electrode chambers 12, 13 of the electrolytic cell 10. In the water supply passage 30, an electromagnetic valve 31 that is electrically controlled to be opened and closed to supply the water from the external water supply source to the electrolytic cell 10 in the open state and close the water in the closed state,
A flow rate sensor 32 that detects the amount of water supplied to the electrolytic cell 10 through the water supply passage 30 is interposed.

【0011】濃塩水供給路40は、濃塩水タンク50内
に貯えた濃塩水中に一端を開口するとともに他端を電動
ポンプ60に接続した吸い込み管41と、電動ポンプ6
0と電解槽10の近傍の給水路20とを接続した供給管
42とを備えており、電解槽10の下方に配設した濃塩
水タンク50内の濃塩水を電動ポンプ60の作動により
給水路30に供給するものである。
The concentrated salt water supply passage 40 has a suction pipe 41 having one end opened to the concentrated salt water stored in the concentrated salt water tank 50 and the other end connected to the electric pump 60, and the electric pump 6.
0 and a supply pipe 42 that connects the water supply passage 20 near the electrolysis tank 10 to each other. The concentrated salt water in the concentrated salt water tank 50 disposed below the electrolysis tank 10 is supplied by the electric pump 60. It supplies to 30.

【0012】電動ポンプ60は、バルブハウジング61
と協働してポンプ室62を画定するダイヤフラム63を
備えている。ダイヤフラム63は、ソレノイド64に対
して通電及び非通電が繰返されたとき往復動するように
なっており、同ダイヤフラム62の往復動によって、電
動ポンプ60は、濃塩水タンク50内の濃塩水を吸い込
み管41を通して吸入口65からポンプ室62内に吸入
するとともに吐出口66から吐出し供給管42を通して
給水路20に供給する。このとき、濃塩水の単位時間当
たりの送水量は、上記通電及び非通電の繰返し周期の調
整によって制御される。ポンプ室62と吸入口65の間
には、電動ポンプ60の作動時に吸入口65からポンプ
室62方向への流れのみを許容する逆止弁67が設けら
れている。また、ポンプ室62と吐出口66の間には、
電動ポンプ60の作動時にポンプ室62から吐出口66
方向への流れのみを許容する逆止弁68が設けられてい
る。各逆止弁67,68は電動ポンプ60の非作動時に
おいては両方向の流れを許容するものであり、これによ
り電動ポンプ60はポンプ室63内に空気が侵入した場
合においても同空気を特に抜く必要なく必要な吐出圧を
得られるようになっている。
The electric pump 60 includes a valve housing 61.
And a diaphragm 63 which cooperates with and defines a pump chamber 62. The diaphragm 63 is adapted to reciprocate when the solenoid 64 is repeatedly energized and de-energized. By the reciprocating motion of the diaphragm 62, the electric pump 60 sucks the concentrated salt water in the concentrated salt water tank 50. The water is sucked into the pump chamber 62 from the suction port 65 through the pipe 41 and discharged from the discharge port 66 to be supplied to the water supply passage 20 through the supply pipe 42. At this time, the amount of concentrated salt water to be sent per unit time is controlled by adjusting the repeating cycle of energization and de-energization. A check valve 67 is provided between the pump chamber 62 and the suction port 65 to allow only the flow from the suction port 65 toward the pump chamber 62 when the electric pump 60 is operated. Further, between the pump chamber 62 and the discharge port 66,
From the pump chamber 62 to the discharge port 66 when the electric pump 60 operates.
A check valve 68 is provided which allows only directional flow. Each of the check valves 67 and 68 allows a flow in both directions when the electric pump 60 is not in operation, so that the electric pump 60 particularly bleeds air when it enters the pump chamber 63. The required discharge pressure can be obtained without need.

【0013】電気制御回路70はマイクロコンピュータ
により構成されており、上記電源20、電流計22、電
磁バルブ31、流量センサ32、電動ポンプ60のソレ
ノイド64、及び電解水の生成を指示するための生成ス
イッチ71に接続されている。電気制御回路70は、各
センサ22,32及びスイッチ71からの入力に基づき
図2,3のフローチャートに対応したプログラムを実行
して、直流電源装置20、電磁バルブ31、及び電動ポ
ンプ25の作動を制御する。また、電気制御回路70に
は、電解水の生成の停止中に電動ポンプ60を作動させ
るタイミングを計測するためのタイマ72が内蔵されて
いる。
The electric control circuit 70 is composed of a microcomputer, and has the power source 20, the ammeter 22, the electromagnetic valve 31, the flow rate sensor 32, the solenoid 64 of the electric pump 60, and the generation for instructing the generation of the electrolyzed water. It is connected to the switch 71. The electric control circuit 70 executes the programs corresponding to the flowcharts of FIGS. 2 and 3 based on the inputs from the sensors 22, 32 and the switch 71 to operate the DC power supply device 20, the electromagnetic valve 31, and the electric pump 25. Control. Further, the electric control circuit 70 has a built-in timer 72 for measuring the timing of operating the electric pump 60 while the production of the electrolyzed water is stopped.

【0014】次に、上記のように構成した塩水処理装置
の動作を図2のフローチャートに沿って説明する。
Next, the operation of the salt water treatment device configured as described above will be described with reference to the flow chart of FIG.

【0015】最初、図示しない電源スイッチがオン操作
されると、電気制御回路70はステップ100にてプロ
グラムの実行を開始し、ステップ102の処理を繰返し
実行して生成スイッチ71のオン操作を待つ。このとき
生成スイッチ71がオン操作されると、電気制御回路7
0はステップ104以降の処理を順次実行して電解水の
生成を開始する。
First, when a power switch (not shown) is turned on, the electric control circuit 70 starts executing the program in step 100, and repeatedly executes the processing in step 102, and waits for the generation switch 71 to be turned on. At this time, when the generation switch 71 is turned on, the electrical control circuit 7
In 0, the processes of step 104 and thereafter are sequentially executed to start generation of electrolyzed water.

【0016】ステップ104においては、電動ポンプ6
0を所定時間だけ作動させて、濃塩水タンク50内の濃
塩水を濃塩水供給路40中にて給水路30及び電解槽1
0側に送る。この場合、電動ポンプ60は送水量が最大
になるように制御し、電動ポンプ60を作動させる時間
は、濃塩水供給路40中が完全に濃塩水により満たされ
るのに要する時間、すなわち濃塩水タンク50内の濃塩
水が少なくとも給水路30まで達するような時間に予め
設定されている。
In step 104, the electric pump 6
0 is operated for a predetermined time, and the concentrated salt water in the concentrated salt water tank 50 is fed into the concentrated salt water supply passage 40 in the water supply passage 30 and the electrolytic cell 1.
Send to 0 side. In this case, the electric pump 60 is controlled to maximize the amount of water to be fed, and the time for operating the electric pump 60 is the time required for the concentrated salt water supply passage 40 to be completely filled with concentrated salt water, that is, the concentrated salt water tank. The time is set in advance so that the concentrated salt water in 50 reaches at least the water supply channel 30.

【0017】ステップ106においては、電磁バルブ3
1を開いて電解槽10内への水の供給を開始する。そし
て、ステップ108の判定処理を繰返し実行して、流量
センサ32が所定の流量を検出するのを待つ。これは、
上記ステップ104にて濃塩水供給路40から送られて
給水路30及び電解槽10内に溜っている濃塩水をさら
に電解槽10より下流に送って、電解槽10が新たに外
部給水源から供給された水により満たされるのを待つた
めの処理である。したがって、上記流量センサ32より
検出する所定の流量は、濃塩水供給管42が合流してい
る位置より下流の給水路30中に溜っている水が電解槽
10まで達するのに要する流量に予め設定されている。
なお、外部給水源から圧送される水量が一定ならば、同
判定処理に代えて、電磁バルブ31を開いてから単に所
定時間経過するのを待つようにしてもよい。
In step 106, the electromagnetic valve 3
1 is opened and the supply of water into the electrolytic cell 10 is started. Then, the determination process of step 108 is repeatedly executed to wait for the flow rate sensor 32 to detect a predetermined flow rate. this is,
In step 104, the concentrated salt water supplied from the concentrated salt water supply passage 40 and accumulated in the water supply passage 30 and the electrolytic bath 10 is further sent downstream from the electrolytic bath 10, and the electrolytic bath 10 is newly supplied from the external water supply source. It is a process to wait for the water to be filled. Therefore, the predetermined flow rate detected by the flow rate sensor 32 is preset to the flow rate required for the water accumulated in the water supply passage 30 downstream from the position where the concentrated salt water supply pipe 42 joins to reach the electrolytic cell 10. Has been done.
If the amount of water pumped from the external water supply source is constant, instead of the determination process, it may be possible to simply wait for a predetermined time after opening the electromagnetic valve 31.

【0018】上記ステップ108の繰返し実行中、流量
センサ32が所定の流量を検出すると、電気制御回路7
0は、プログラムをステップ110に進めて、直流電源
装置20を作動させて電極14,15に対する電圧の印
加を開始するとともに、電動ポンプ60の作動させて給
水路30に対する濃塩水の供給を開始する。なお、この
作動開始時の電動ポンプ60の送水量は、予め初期設定
された量となるように制御される。これにより、外部給
水源から給水路20を通って供給される水に濃塩水が混
入して希塩水が生成され、同希塩水が電解槽10の各電
解室12,13に供給されて電気分解され電解水が生成
され始める。
When the flow rate sensor 32 detects a predetermined flow rate during the repeated execution of step 108, the electric control circuit 7
0 advances the program to step 110 to activate the DC power supply device 20 to start the application of voltage to the electrodes 14 and 15, and to activate the electric pump 60 to start the supply of concentrated salt water to the water supply passage 30. . The water supply amount of the electric pump 60 at the start of the operation is controlled so as to be a preset amount. As a result, the concentrated salt water is mixed with the water supplied from the external water supply source through the water supply passage 20 to generate diluted salt water, and the diluted salt water is supplied to the electrolysis chambers 12 and 13 of the electrolytic cell 10 for electrolysis. Then, electrolyzed water starts to be generated.

【0019】上記電解水の生成開始後、生成スイッチ7
1がオン状態を維持している間、電気制御回路70はス
テップ114における「YES」との判定のもとにステ
ップ112の処理を繰返し実行し続ける。ステップ11
2は、電流計22により計測される両電極14,15間
を流れる電流に基づいて電動ポンプ60の送水量を制御
する処理である。両電極14,15間を流れる電流が予
め設定された所定の電流値より大きかった場合は、電動
ポンプ60の送水量を減少させて給水路30に対する濃
塩水の供給量を減少させる。両電極14,15間を流れ
る電流が前記所定電流値より小さかった場合は、電動ポ
ンプ60の送水量を増加させて給水路30に対する濃塩
水の供給量を増加させる。これにより、電解槽10に供
給する希塩水の濃度が所定濃度に保たれて電解槽10に
おける電気分解の強度が常に一定に保たれるため、生成
される電解水の有効塩素濃度が常に一定に保たれる。
After the production of the electrolyzed water is started, the production switch 7
While 1 is maintained in the ON state, the electric control circuit 70 continues to repeatedly execute the process of step 112 based on the determination of “YES” in step 114. Step 11
2 is a process of controlling the water supply amount of the electric pump 60 based on the current flowing between the electrodes 14 and 15 measured by the ammeter 22. When the current flowing between the electrodes 14 and 15 is larger than a predetermined current value set in advance, the water supply amount of the electric pump 60 is reduced to reduce the supply amount of concentrated salt water to the water supply passage 30. When the current flowing between the electrodes 14 and 15 is smaller than the predetermined current value, the amount of water supplied by the electric pump 60 is increased to increase the amount of concentrated salt water supplied to the water supply passage 30. As a result, the concentration of the dilute salt water supplied to the electrolyzer 10 is kept at a predetermined concentration and the electrolysis strength in the electrolyzer 10 is always kept constant, so that the effective chlorine concentration of the electrolyzed water produced is always kept constant. To be kept.

【0020】上記ステップ112,114の繰返し実行
中、生成スイッチ71がオフ操作されると、電気制御回
路は、ステップ114における「NO」との判定のもと
にプログラムをステップ116へ進めて、電動ポンプ6
0及び直流電源装置20の作動を停止させるとともに電
磁バルブ31を閉じ上記電解水の生成を停止させる。ま
た、このとき、ステップ118にてタイマ72をリセッ
トスタートして時間を計測し始める。そして、以後、ス
テップ120,122の処理を繰返し実行して再び生成
スイッチ71がオン操作されるのを待つ。このとき生成
スイッチ71がオン操作されると、電気制御回路70
は、ステップ120における判定のもとに、ステップ1
24にて電磁バルブ60を開いて給水を開始した上で、
プログラムを前記ステップ110以降へ進めて再び電解
水の生成を開始する。
When the generation switch 71 is turned off during the repeated execution of the steps 112 and 114, the electric control circuit advances the program to step 116 based on the judgment of "NO" in step 114, and the electric motor is operated. Pump 6
0 and the operation of the DC power supply device 20 are stopped, and the electromagnetic valve 31 is closed to stop the generation of the electrolyzed water. At this time, the timer 72 is reset and started at step 118 to start measuring the time. Then, thereafter, the processes of steps 120 and 122 are repeatedly executed, and the process waits until the generation switch 71 is turned on again. At this time, when the generation switch 71 is turned on, the electrical control circuit 70
Based on the determination in step 120, step 1
After opening the electromagnetic valve 60 at 24 and starting water supply,
The program is advanced to step 110 and subsequent steps to start generation of electrolyzed water again.

【0021】一方、上記ステップ120,122の処理
の繰返し実行中、すなわち電解水の生成の停止中、生成
スイッチ71が操作されずに同電解水の生成の停止が所
定時間Tだけ継続した場合、電気制御回路70は、タイ
マ72による計時値に基づくステップ122における判
定に基づいて、プログラムをステップ126以降へ進め
る。ステップ126〜ステップ130は、前記ステップ
104〜108と同様の処理である。ステップ126に
おいては、電動ポンプ60を所定時間だけ作動させて、
濃塩水タンク50内の濃塩水を所定量だけ濃塩水供給路
40中にて給水路30及び電解槽10側に送る。これに
より、電解水の生成の停止中に時間の経過とともに濃塩
水タンク50側に逆流して濃塩水供給路40中に溜った
希塩水が給水路30より下流に送り返されて、濃塩水供
給路40中が完全に濃塩水により満たされる。ステップ
128においては、電磁バルブ31を開いて電解槽10
内への水の供給を開始する。そして同給水開始後、ステ
ップ130の判定処理を繰返し実行して、電解槽10が
新たに外部給水源から供給された水により満たされるの
を待つ。
On the other hand, if the generation switch 71 is not operated and the generation of the electrolyzed water continues for a predetermined time T during the repeated execution of the processing of steps 120 and 122, that is, while the generation of the electrolyzed water is stopped, The electric control circuit 70 advances the program to step 126 and the subsequent steps based on the determination in step 122 based on the measured value by the timer 72. Steps 126 to 130 are the same processes as steps 104 to 108. In step 126, the electric pump 60 is operated for a predetermined time,
A predetermined amount of concentrated salt water in the concentrated salt water tank 50 is sent to the water supply passage 30 and the electrolytic cell 10 side in the concentrated salt water supply passage 40. As a result, the diluted salt water that flows back to the concentrated salt water tank 50 side and accumulates in the concentrated salt water supply path 40 with the passage of time while the production of the electrolyzed water is stopped is sent back to the downstream side from the water supply path 30, and the concentrated salt water supply path 40 is completely filled with concentrated brine. In step 128, the electromagnetic valve 31 is opened to open the electrolyzer 10.
Start supplying water to the inside. After the start of the water supply, the determination process of step 130 is repeatedly executed to wait until the electrolytic cell 10 is newly filled with the water supplied from the external water supply source.

【0022】上記ステップ130の繰返し実行中、流量
センサ32が前記所定の流量を検出すると、ステップ1
32にて電磁バルブ31を閉じて上記給水を停止した上
で、プログラムを前記ステップ118へ進めてタイマ7
2による計時を再び開始する。そして、以後、再び前記
ステップ120,122の処理を繰返し実行して、生成
スイッチ71がオン操作されるか又はタイマ71が所定
時間Tを計時するのを待つ。
When the flow rate sensor 32 detects the predetermined flow rate during the repeated execution of step 130, step 1
At 32, the electromagnetic valve 31 is closed to stop the water supply, and then the program is advanced to the step 118 to set the timer 7
The time counting by 2 is started again. Then, thereafter, the processes of steps 120 and 122 are repeatedly executed again, and the process waits until the generation switch 71 is turned on or the timer 71 counts a predetermined time T.

【0023】上記プログラムの実行により、電気制御回
路70は、生成スイッチ71の操作に応答して電解水の
生成及び停止を繰返し実行し続ける。この場合、電解水
の生成の停止中は、タイマ72により時間を計測して、
所定時間Tが経過する毎に、濃塩水タンク50内の濃塩
水を所定量だけ濃塩水供給路40中にて給水路30及び
電解槽10側に送り、濃塩水供給路40中を完全に濃塩
水により満たす。したがって、同実施形態においては、
電解水の生成の再開時、濃塩水供給路40から給水路3
0に速やかに濃塩水を供給して電解槽10に供給する希
塩水の濃度を速やかに所望の濃度まで上げることができ
るため、速やかに所望の有効塩素濃度を有する電解水の
生成を再開することができる。この場合、逆止弁、空気
抜き路なども必要ないため、装置の構成も簡単である。
また、濃塩水が定期的に流れることになるため、濃塩水
供給路40及び電動ポンプ60に濃塩水の塩が固着する
ことも回避できる。
By executing the above program, the electric control circuit 70 continues to repeatedly generate and stop the electrolyzed water in response to the operation of the generation switch 71. In this case, while the generation of electrolyzed water is stopped, the time is measured by the timer 72,
Every time the predetermined time T elapses, a predetermined amount of concentrated salt water in the concentrated salt water tank 50 is sent to the water supply passage 30 and the electrolytic cell 10 side in the concentrated salt water supply passage 40 to completely concentrate the concentrated salt water supply passage 40. Fill with salt water. Therefore, in the same embodiment,
When the generation of electrolyzed water is restarted, the concentrated salt water supply passage 40 to the water supply passage 3
Since the concentration of the diluted salt water supplied to the electrolyzer 10 can be rapidly increased to a desired concentration by rapidly supplying the concentrated salt water to 0, it is possible to promptly restart the generation of the electrolytic water having the desired effective chlorine concentration. You can In this case, since the check valve and the air vent passage are not required, the structure of the device is simple.
Further, since the concentrated salt water flows regularly, it is possible to avoid the salt adhered to the concentrated salt water supply passage 40 and the electric pump 60.

【0024】また、上記のように電解水の生成の停止中
に電動ポンプ60を作動させた場合には、同作動が完了
する毎に、電磁バルブ31を開いて電解槽10内を水で
満たすようにしている。これによれば、電解水の生成の
停止中、前記電動ポンプ60の作動により濃塩水が電解
槽10より下流まで送られた場合にも、同電動ポンプ6
0の作動の完了後に電解槽10内が水で満たされること
になる。したがって、電解水の生成の再開時に電解槽1
0内が濃塩水で満たされていて両電極14,15間に過
度の電流が流れることが回避されるため、電極の劣化が
抑制される。
When the electric pump 60 is operated while the production of electrolyzed water is stopped as described above, the electromagnetic valve 31 is opened to fill the electrolyzer 10 with water each time the operation is completed. I am trying. According to this, even when concentrated salt water is sent to the downstream of the electrolytic cell 10 by the operation of the electric pump 60 while the production of the electrolytic water is stopped, the electric pump 6 is also provided.
After completion of the operation of 0, the electrolytic cell 10 will be filled with water. Therefore, when the production of electrolyzed water is restarted, the electrolyzer 1
Since the inside of 0 is filled with concentrated salt water and an excessive current is prevented from flowing between the electrodes 14 and 15, deterioration of the electrodes is suppressed.

【0025】b.第2の実施形態 以下、本発明の第2の実施形態について図面を参照して
説明する。同実施形態は、図3に示したように、上記第
1の実施形態に係る電解水生成装置において、濃塩水供
給路40の供給管42に濃塩水を一時的に貯える濃塩水
貯留部43を介装したものである。同実施形態におい
て、電気制御回路70は、上記第1の実施形態と同様
に、生成スイッチ71がオン操作されたとき電磁バルブ
31を開くとともに直流電源装置20及び電動ポンプ6
0の作動を開始して電解水の生成を開始し、生成スイッ
チ71がオン状態を維持しているとき電流計22による
計測に基づき電動ポンプ60の送水量を制御して電解槽
10に供給する希塩水の濃度を一定に保ち、生成スイッ
チ71がオフ操作されたとき直流電源装置20及び電動
ポンプ60の作動を停止するとともに電磁バルブ31を
閉じて電解水の生成を停止する処理を繰返し実行する。
ただし、上記第1の実施形態にて実行した電解水の生成
の停止中における電動ポンプ60の作動制御及び電磁バ
ルブ31の開閉制御(ステップ104,108,11
8,122,126〜132)は、省略して実行しない
ようにしている。
B. Second Embodiment Hereinafter, a second embodiment of the present invention will be described with reference to the drawings. As shown in FIG. 3, in the same embodiment, in the electrolyzed water generating apparatus according to the first embodiment, a supply pipe 42 of the concentrated salt water supply passage 40 is provided with a concentrated salt water storage section 43 for temporarily storing concentrated salt water. It has been inserted. In the same embodiment, the electric control circuit 70 opens the electromagnetic valve 31 when the generation switch 71 is turned on and the DC power supply device 20 and the electric pump 6 as in the first embodiment.
When the generation switch 71 maintains the ON state, the amount of water supplied by the electric pump 60 is controlled and supplied to the electrolytic cell 10 when the generation switch 71 maintains the ON state. The concentration of the diluted salt water is kept constant, and when the generation switch 71 is turned off, the operation of the DC power supply device 20 and the electric pump 60 is stopped, and the electromagnetic valve 31 is closed to stop the generation of electrolytic water. .
However, the operation control of the electric pump 60 and the opening / closing control of the electromagnetic valve 31 during the stop of the production of the electrolyzed water executed in the first embodiment (steps 104, 108, 11).
8, 122, 126 to 132) are omitted so as not to be executed.

【0026】上記のように構成した同実施形態において
は、電解水の生成の停止中、電解槽10より下流の希塩
水が時間の経過とともに濃塩水タンク50側に逆流して
濃塩水供給路40中に溜った場合においても、濃塩水供
給路40中には濃塩水貯留部43によって比較的多量の
濃塩水が貯えられているため、濃塩水供給路40中の塩
水の濃度は比較的高いまま保たれる。したがって、電解
水の生成の再開時、速やかに所望の有効塩素濃度を有す
る電解水の生成を開始できる。この場合、逆止弁、空気
抜き路などが必要ないため、装置の構成も比較的簡単で
ある。
In the embodiment having the above-described structure, while the production of the electrolyzed water is stopped, the diluted salt water downstream of the electrolytic cell 10 flows back to the concentrated salt water tank 50 side with the passage of time and the concentrated salt water supply passage 40 is provided. Even when the salt water is accumulated inside, since a relatively large amount of concentrated salt water is stored in the concentrated salt water supply passage 40 by the concentrated salt water storage portion 43, the concentration of salt water in the concentrated salt water supply passage 40 remains relatively high. To be kept. Therefore, when the production of electrolyzed water is restarted, the production of electrolyzed water having a desired effective chlorine concentration can be promptly started. In this case, since a check valve, an air vent passage, etc. are not required, the structure of the device is relatively simple.

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

【図1】本発明の第1の実施形態に係る塩水処理装置の
全体構成図である。
FIG. 1 is an overall configuration diagram of a salt water treatment device according to a first embodiment of the present invention.

【図2】図1の電気制御回路により実行されるプログラ
ムを示すフローチャートである。
FIG. 2 is a flowchart showing a program executed by the electric control circuit of FIG.

【図3】本発明の第1の実施形態に係る塩水処理装置の
全体構成図である。
FIG. 3 is an overall configuration diagram of a salt water treatment device according to a first embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10…電解槽、14,15…電極、20…直流電源装
置、30…給水路、31…給水バルブ、40…濃塩水供
給路、50…濃塩水タンク、60…電動ポンプ、70…
電気制御回路、71…生成スイッチ、72…タイマ。
10 ... Electrolyzer, 14, 15 ... Electrode, 20 ... DC power supply device, 30 ... Water supply channel, 31 ... Water supply valve, 40 ... Concentrated salt water supply channel, 50 ... Concentrated salt water tank, 60 ... Electric pump, 70 ...
Electric control circuit, 71 ... Generation switch, 72 ... Timer.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉田 恭一郎 愛知県豊明市栄町南館3番の16 ホシザキ 電機株式会社内 (72)発明者 藤田 昌浩 愛知県豊明市栄町南館3番の16 ホシザキ 電機株式会社内 Fターム(参考) 4D061 DA02 DB07 DB09 EA02 EB01 EB04 EB12 EB37 EB39 ED12 GA02 GA12 GC06 GC20    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Kyoichiro Yoshida             16 Hoshizaki, 3rd South Building, Sakaemachi, Toyoake City, Aichi Prefecture             Electric Co., Ltd. (72) Inventor Masahiro Fujita             16 Hoshizaki, 3rd South Building, Sakaemachi, Toyoake City, Aichi Prefecture             Electric Co., Ltd. F-term (reference) 4D061 DA02 DB07 DB09 EA02 EB01                       EB04 EB12 EB37 EB39 ED12                       GA02 GA12 GC06 GC20

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】直流電圧が印加される一対の電極を収容し
てなり、供給された希塩水を電気分解して電解水を生成
する電解槽と、 電気的に開閉制御可能な電磁バルブを介装してなり該電
磁バルブの開状態にて前記電解槽に連続的に水を供給す
る給水路と、 電気的に作動制御可能な電動ポンプを介装してなり該電
動ポンプの作動により前記電解槽の下方に配設した濃塩
水タンク内に貯えた濃塩水を前記給水路に供給する濃塩
水供給路と、 電解水の生成を指示するための生成指示手段と、 前記生成指示手段により電解水の生成が指示されている
とき前記電解槽に所定濃度の希塩水を供給するように前
記電磁バルブを開状態に保つとともに前記電動ポンプを
作動制御する電気制御回路とを備えた電解水生成装置に
おいて、 前記電気制御回路が、前記電解水の生成の停止中、所定
時間毎に前記電動ポンプを作動させて前記濃塩水タンク
内の濃塩水を所定量だけ前記濃塩水供給路中にて前記給
水路及び電解槽側に送ることを特徴とする電解水生成装
置。
1. An electrolytic cell that accommodates a pair of electrodes to which a DC voltage is applied and that electrolyzes the supplied diluted salt water to generate electrolyzed water, and an electromagnetic valve that can be electrically controlled to open and close. The electrolysis tank is equipped with a water supply path for continuously supplying water to the electrolysis tank when the electromagnetic valve is open, and an electric pump whose operation can be electrically controlled. A concentrated salt water supply path for supplying the concentrated salt water stored in a concentrated salt water tank disposed below the tank to the water supply path, a generation instruction means for instructing generation of electrolytic water, and an electrolytic water generated by the generation instruction means. In the electrolyzed water production apparatus, the electrolysis water is provided with an electric control circuit for keeping the electromagnetic valve open so as to supply dilute salt water having a predetermined concentration to the electrolysis tank when the production of , The electrical control circuit While the generation of electrolytic water is stopped, the electric pump is operated at predetermined time intervals to send a predetermined amount of concentrated salt water in the concentrated salt water tank to the water supply passage and the electrolytic cell side in the concentrated salt water supply passage. Characterized electrolyzed water generator.
【請求項2】前記請求項1に記載の電解水生成装置にお
いて、 前記電気制御回路が、前記電解水の生成の停止中におけ
る電動ポンプの作動が完了する毎に、前記電磁バルブを
開いて前記電解槽内を水で満たすことを特徴とする電解
水生成装置。
2. The electrolyzed water producing apparatus according to claim 1, wherein the electric control circuit opens the electromagnetic valve every time the operation of the electric pump is completed while the production of the electrolyzed water is stopped. An electrolyzed water generator characterized in that the inside of an electrolyzer is filled with water.
【請求項3】直流電圧が印加される一対の電極を収容し
てなり、供給された希塩水を電気分解して電解水を生成
する電解槽と、 電気的に開閉制御可能な電磁バルブを介装してなり該電
磁バルブの開状態にて前記電解槽に連続的に水を供給す
る給水路と、 電気的に作動制御可能な電動ポンプを介装してなり該電
動ポンプの作動により前記電解槽の下方に配設した濃塩
水タンク内に貯えた濃塩水を前記給水路に供給する濃塩
水供給路と、 電解水の生成を指示するための生成指示手段と、 前記生成指示手段により電解水の生成が指示されている
とき前記電解槽に所定濃度の希塩水を供給するように前
記電磁バルブを開状態に保つとともに前記電動ポンプを
作動制御する電気制御回路とを備えた電解水生成装置に
おいて、 前記濃塩水供給路に、前記濃塩水タンクから給水路に供
給される濃塩水を一時的に貯える濃塩水貯留部を介装し
たことを特徴とする電解水生成装置。
3. An electrolytic cell that accommodates a pair of electrodes to which a DC voltage is applied and that electrolyzes the supplied diluted salt water to generate electrolyzed water, and an electromagnetic valve that can be electrically controlled to open and close. The electrolysis tank is equipped with a water supply path for continuously supplying water to the electrolysis tank when the electromagnetic valve is open, and an electric pump whose operation can be electrically controlled. A concentrated salt water supply path for supplying the concentrated salt water stored in a concentrated salt water tank disposed below the tank to the water supply path, a generation instruction means for instructing generation of electrolytic water, and an electrolytic water generated by the generation instruction means. In the electrolyzed water production apparatus, the electrolysis water is provided with an electric control circuit for keeping the electromagnetic valve open so as to supply dilute salt water having a predetermined concentration to the electrolysis tank when the production of , In the concentrated salt water supply passage, Electrolytic water generation apparatus for it, characterized in that interposed concentrated salt water reservoir to store the concentrated brine supplied temporarily to the water supply passage from dark brine tank.
JP2001196527A 2001-06-28 2001-06-28 Electrolytic water making apparatus Pending JP2003010850A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001196527A JP2003010850A (en) 2001-06-28 2001-06-28 Electrolytic water making apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001196527A JP2003010850A (en) 2001-06-28 2001-06-28 Electrolytic water making apparatus

Publications (1)

Publication Number Publication Date
JP2003010850A true JP2003010850A (en) 2003-01-14

Family

ID=19034319

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001196527A Pending JP2003010850A (en) 2001-06-28 2001-06-28 Electrolytic water making apparatus

Country Status (1)

Country Link
JP (1) JP2003010850A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009160533A (en) * 2008-01-08 2009-07-23 Hoshizaki Electric Co Ltd Electrolytic water generator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009160533A (en) * 2008-01-08 2009-07-23 Hoshizaki Electric Co Ltd Electrolytic water generator

Similar Documents

Publication Publication Date Title
US8419926B2 (en) Electrolyzed water producing method and apparatus
JP3957476B2 (en) Water treatment equipment
JP4874104B2 (en) Electrolyzed water generation / dilution supply equipment
JP6098919B2 (en) Sterilization water generator
JP2003010850A (en) Electrolytic water making apparatus
JP4804655B2 (en) Electrolyzed water generator
JP3571258B2 (en) Electrolyzed water generator
JP3575726B2 (en) Method for producing weakly acidic water
JP2010207668A (en) Electrolytic water generator
JP2001219169A (en) Electrolytic apparatus
JP3411094B2 (en) Salt water supply device
JP3767983B2 (en) Electrolyzed water generator
JPH10469A (en) Electrolytic water producing apparatus
JP2001009454A (en) Electrolytic water maker
JP3383757B2 (en) Electrolyzed water generator
JP4689817B2 (en) Electrolyzed water generator
JP3579498B2 (en) Electrolyzed water generator
JPH11114565A (en) Electrolyzed water producing device
JP3767976B2 (en) Electrolyzed water generator
JP3548637B2 (en) Electrolyzed water generator
IE85467B1 (en) Electrolyzed water producing method and apparatus
JP2005279519A (en) Apparatus for producing electrolytic water
JP3575714B2 (en) Electrolyzed water generator
JP4881581B2 (en) Electrolyzed water generator
JP2000005752A (en) Electrolytc water producing device