JP5891906B2 - Sterilization water generator - Google Patents

Description

  The present invention relates to a sterilizing water generating apparatus that electrolyzes water containing chloride ions to generate chlorine at an anode, and generates sterilizing water containing hypochlorous acid by a reaction between the chlorine and water.

  As an apparatus for generating hypochlorous acid with high efficiency and high concentration, the apparatus described in Patent Document 1 below is known. The apparatus described in the following Patent Document 1 includes chlorination means for killing or sterilizing microorganisms in untreated seawater, and the chlorination means determines the concentration of chloride ions contained in untreated seawater. Concentration means for increasing, and an electrolyzer for electrolyzing seawater with increased chloride ion concentration to generate hypochlorous acid.

JP 2009-274028 A

  In the apparatus described in Patent Document 1, it is described that a concentrator using an electrodialysis method can be applied as a concentrator used for the concentrating means. Since the electrodialysis method concentrates chloride ions using an ion exchange membrane and a pair of electrodes, the ion exchange membrane is clogged, and regular maintenance of the ion exchange membrane is necessary. .

  Therefore, the present inventors collected chloride ions using a pair of electrodes without using an ion exchange membrane, electrolyzed water containing the chloride ions to generate chlorine at the anode, and the chlorine and It was investigated whether a sterilizing water generating device that generates sterilizing water containing hypochlorous acid by reaction with water could be provided. In such a sterilizing water generating apparatus, it is necessary to release chloride ions collected at the anode at an appropriate timing, but even if the voltage application to the pair of electrodes is finished, the residual charges on the electrodes cause chlorination. A new problem to be solved has been found that the detachment of heavy ions is not performed in a short time.

  This invention is made | formed in view of such a subject, The objective is to provide the disinfection water production | generation apparatus which can supply a high concentration hypochlorous acid rapidly.

Sterile water generator according to the present invention in order to solve the above problems, a water supply passage of water through, provided the water supply path has a pair of concentrated electrodes, a voltage is applied between the pair of stacking electrodes This is provided in the concentration region that attracts chloride ions contained in the water passing through the water supply channel, and the water supply channel downstream of the concentration region, and has a pair of electrolysis electrodes, and a voltage is applied between the pair of electrolysis electrodes. Electrolyzing water flowing through the water supply channel to generate chlorine at the anodes of the pair of electrolysis electrodes, and an electrolytic cell region for generating sterilizing water containing hypochlorous acid by reaction of the chlorine and water ; And control means for controlling the way of water in the water supply channel, the voltage applied between the pair of concentrating electrodes, and the voltage applied between the pair of electrolysis electrodes. The control means passes water so that the flow rate of water in the vicinity of the pair of concentration electrodes becomes the first flow rate, and collects chloride ions in water by applying a voltage to the pair of concentration electrodes. And passing water so that the flow rate of water in the vicinity of the pair of concentration electrodes becomes a second flow rate higher than the first flow rate, and collecting chloride ions collected by executing the concentration mode of the pair of concentration electrodes. A supply mode in which water containing chloride ions is separated from the anode and supplied to the electrolytic cell region, and a voltage for electrolysis is applied to the pair of electrolysis electrodes, and the water supplied from the concentration region is electrolyzed by executing the supply mode. And an electrolysis mode in which hypochlorous acid is generated by treatment.

  According to the present invention, in the concentration mode for collecting chloride ions in water, water is passed to achieve the first flow rate, and in the supply mode for removing chloride ions from the anode, water is passed to provide the second flow rate. The second flow rate is faster than the first flow rate. Therefore, by supplying water to the pair of concentrating electrodes at a relatively slow first flow rate, chloride ions in the water are efficiently collected, and after smooth portion ions are collected, at a relatively fast second flow rate. By supplying water to the pair of concentrating electrodes, chloride ions can be reliably separated from the electrodes in a short time. Thus, since the water which raised the chloride ion density | concentration by supply mode can be supplied to an electrolytic cell area | region, a high concentration hypochlorous acid can be obtained.

  In the sterilizing water generating device according to the present invention, it is also preferable to include a flow rate reducing means for adjusting the flow rate of water in the vicinity of the pair of electrolysis electrodes to be a third flow rate that is slower than the second flow rate.

  As described above, when the chloride ions are separated from the electrodes in the supply mode, the flow rate of water passing through the water supply channel is preferably a relatively high second flow rate, but water is supplied to the pair of electrolysis electrodes at the same rate. If it does, the water which passes without contributing to the production | generation of hypochlorous acid will increase, and the hypochlorous acid water of high concentration cannot be produced | generated. Therefore, in this preferred embodiment, by providing a flow rate reducing means for adjusting the flow rate of water in the vicinity of the pair of electrolysis electrodes to be a third flow rate that is slower than the second flow rate, a high concentration is provided in the vicinity of the pair of electrolysis electrodes. Thus, a high concentration of hypochlorous acid water can be generated.

  In the sterilizing water generator according to the present invention, it is also preferable that the control means applies a preparatory voltage different from the electrolysis voltage to the pair of electrolysis electrodes in the supply mode.

  In this preferred embodiment, since a preparatory voltage different from the electrolysis voltage is applied to the pair of electrolysis electrodes in the supply mode, the amount of change in the applied voltage when starting the electrolysis mode and shifting to the electrolysis voltage is reduced. can do. Thereby, deterioration of an electrode can be suppressed, shifting an applied voltage to the voltage for electrolysis in a short time.

  Further, in the sterilizing water generator according to the present invention, the control means measures the flow of electricity supplied to the electrolytic cell region by applying a preparatory voltage to the pair of electrolysis electrodes, and the flow of electricity. It is also preferable to shift from the concentration mode to the supply mode based on the transition from the weaker state to the stronger state.

  As described above, when chloride ions are collected on the anode in the concentration mode, the quality of water passing through the electrolytic cell region changes due to fluctuations in chloride ions. More specifically, when chloride ions are collected at the anode, the chloride ion concentration in the water decreases, and the flow of electricity in water becomes weak. Thereafter, when the amount of chloride ions collected at the anode is saturated, the chloride ion concentration in the water rises again, and the flow of electricity in water becomes strong. Therefore, in this preferred embodiment, it is measured by applying a preparatory voltage to the pair of electrodes for electrolysis that the flow of electricity flowing through the water supply channel on the downstream side of the electrolytic cell region has changed from a weak state to a strong state. On the basis of the measurement results, the transition from the concentration mode to the supply mode enables the transition to the supply mode with a sufficient amount of chloride ions collected on the anode. Hypochlorous acid can be obtained reliably.

  Further, in the sterilizing water generator according to the present invention, the flow rate reduction means adjusts the flow rate of water in the vicinity of the pair of electrolysis electrodes by reducing the flow rate of water flowing through the water supply channel. It is also preferable to reduce the flow rate of water flowing through the water supply channel after a predetermined time has elapsed after adjusting the flow rate of water in the vicinity of the concentration electrode to be the second flow rate.

  If the flow rate of water is increased to the second flow rate after collecting chloride ions, it can be estimated how long it will reach the electrolytic cell region. Therefore, in this preferred embodiment, the flow rate of water in the supply mode is adjusted to be the second flow rate, and then the flow rate of water flowing through the water supply channel is reduced after a predetermined time has elapsed, thereby reliably and simply a pair of electrolysis electrodes. The flow rate in the vicinity can be lowered, and highly concentrated hypochlorous acid water can be obtained reliably.

  Further, in the sterilizing water generator according to the present invention, the flow velocity reducing means has a flow channel having a larger channel cross-sectional area in the water supply channel downstream of the pair of concentrating electrodes than in the vicinity of the pair of concentrating electrodes. It is also preferable that it has an enlarged part, and a pair of electrodes for electrolysis are arranged in the channel enlarged part.

  In this preferred embodiment, the flow rate in the vicinity of the pair of electrolysis electrodes is lowered with a simple configuration by arranging the pair of electrolysis electrodes in the flow passage enlarged portion having a widened cross-sectional area of the flow channel, and the next high concentration is surely achieved. Chlorous acid water can be obtained.

  Moreover, in the sterilizing water generating apparatus according to the present invention, the flow velocity reducing means has a channel bending portion that is configured to bend the channel so that stagnation of the water flow occurs in the water supply channel downstream of the pair of concentrating electrodes. It is also preferable that the pair of electrodes for electrolysis is arranged in the flow path bending portion.

  In this preferred embodiment, the flow rate in the vicinity of the pair of electrolysis electrodes is lowered with a simple configuration by arranging the pair of electrolysis electrodes in the flow path bending portion where the flow path is bent. Chloric acid water can be obtained.

  ADVANTAGE OF THE INVENTION According to this invention, the sterilization water production | generation apparatus which can supply a high concentration hypochlorous acid rapidly can be provided.

It is a perspective view which shows the flush toilet in which the sterilization water production | generation apparatus which is one Embodiment of this invention was installed. It is a flow-path system figure at the time of the sterilization washing | cleaning of the sterilizing water production | generation apparatus shown in FIG. It is a schematic diagram for demonstrating the electrolytic vessel used for the sterilization water production | generation apparatus shown in FIG. It is a flowchart which shows the procedure which determines a 1st voltage. It is a figure which shows the relationship between electrical conductivity and a 1st voltage. It is a flowchart which shows operation | movement of the sterilizing water production | generation apparatus shown in FIG. It is a timing chart which shows operation | movement of the sterilizing water production | generation apparatus shown in FIG. It is a figure which shows typically reaction of the electrode vicinity in concentration mode and electrolysis mode. It is a figure which shows typically a part of sterilization water production | generation apparatus which is a modification of this embodiment. It is a figure which shows typically a part of sterilization water production | generation apparatus which is a modification of this embodiment.

  Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. In order to facilitate the understanding of the description, the same constituent elements in the drawings will be denoted by the same reference numerals as much as possible, and redundant description will be omitted.

  FIG. 1 is a perspective view showing a flush toilet in which a sanitary washing apparatus including a sterilizing water generating apparatus according to an embodiment of the present invention is installed. As shown in the figure, the sanitary washing device 100 is installed and used on a toilet 120 of a water-washing type Western toilet 110. Then, by operating the controller, the cleaning nozzle 14 moves into the toilet 120, and the human body local area can be cleaned by spraying the cleaning water from the tip of the cleaning nozzle 14 toward the human body local area (such as a buttocks). it can.

  FIG. 2 is a flow path system diagram at the time of sterilization cleaning of the sterilizing water generator WD according to the embodiment of the present invention. In the drawing, elements not related to sterilization and cleaning are not shown, but the sanitary cleaning device of this embodiment has a configuration necessary for cleaning a well-known human body part.

  As shown in FIG. 2, the flow path system 10 of the sterilizing water generator WD at the time of sterilization cleaning according to the present embodiment includes a water supply source 12 such as a water pipe and a cleaning nozzle 14, and a flow path 16 (water supply path). They are connected by a path 18, and the concentration tank 6 (concentration region) and the electrolytic cell 1 (electrolysis cell region) are provided in the flow channel 16. A branch part 20 is provided downstream of the electrolytic cell 1 in the flow path 16, a water discharge flow path 18 extending from the branch part 20 to the cleaning nozzle 14, and a drainage flow path 22 extending downward from the branch part 20. It is branched to.

  The water discharge channel 18 is configured such that the cross-sectional area at the water discharge port of the cleaning nozzle 14 (that is, the minimum channel cross-sectional area of the water discharge channel 18) is smaller than the minimum channel cross-sectional area of the drainage channel 22. ing. Thereby, the pressure loss of the drainage channel 22 is smaller than that of the water discharge channel 18. Water is discharged from the nozzle hole of the cleaning nozzle 14 by opening the cleaning valve 28 by the primary pressure from the water supply source 12. The cleaning nozzle 14 is provided with a plurality of nozzle holes for discharging water toward a human body part, and a flow path for supplying water to the nozzle holes. The cleaning nozzle can also clean the outer surface of the cleaning nozzle itself with water discharged from the nozzle hole.

  The water discharge channel 18 is provided with a cleaning valve 28 that is communicably connected to the control unit 24. The cleaning valve 28 opens and closes based on a command from the control unit 24 and controls the inflow of water into the flow path 18 that is a water discharge flow path. The cleaning valve 28 is configured not only to open and close the flow path 18 but also to adjust the opening. The larger the opening degree of the cleaning valve 28, the larger the flow rate and flow velocity. By adjusting the opening degree of the cleaning valve 28, the flow rate in the electrolytic cell 1 arranged on the upstream side can be adjusted.

  A discharge valve 30 connected to the control unit 24 so as to be communicable is provided on the downstream side of the branch part 20 of the drainage flow path 22. The discharge valve 30 opens and closes based on a command from the control unit 24 and controls the inflow of water into the drain passage 22. The drainage channel 22 and the discharge valve 30 constitute a discharge mechanism 32. In this embodiment, the flow path 16 is branched and the drain flow path 22 is provided. However, the present invention is not limited to this, and an opening may be provided only on the lower surface of the flow path 16. In the present embodiment, the drain valve 30 is provided in the drain channel 22 to control the water flow through the drain channel 22, but the present invention is not limited to this, and the drain channel 22 is used by using a pump or the like. It is also possible to control the flow of water flowing through.

  The discharge valve 30 is opened when a concentration mode (details will be described later) in the electrolytic cell 1 is executed or when the electrical conductivity of water is measured. The water discharged from the discharge valve 30 is discharged to the bowl portion of the toilet 120.

  The control unit 24 (control unit) can control the water supply valve provided in the water supply source 12 to adjust the amount of water flowing through the flow path 16. The control unit 24 is configured to control the timing of applying a voltage to the pair of concentrating electrodes arranged in the concentrating tank 6 and to change the voltage. Similarly, the control unit 24 is configured to control the timing of applying a voltage to the pair of electrolytic cell electrodes arranged in the electrolytic cell 1 and to change the voltage. The control unit 24 controls the voltage applied between the pair of electrodes of the concentration tank 6 to be a first voltage that attracts chloride ions to the anode (concentration mode). The control unit 24 includes a preparation / measurement mode (supply mode) for controlling the voltage applied between the pair of electrodes of the electrolytic cell 1 to be a preparation voltage or a measurement voltage, and a voltage applied between the pair of electrodes. However, it is comprised so that execution of the electrolysis mode controlled so that it may become an electrolysis voltage higher than a 1st voltage is possible. The second voltage is defined as the voltage that generates hypochlorous acid or hypochlorite ions.

  FIG. 3 is a schematic diagram for explaining the electrolytic cell 1 and the concentration vessel 6. As shown in the figure, the concentration tank 6 has a pair of electrode plates 2a and 4a, and is configured so that a voltage can be applied between the electrode plates 2a and 4a. The concentration tank 6 only collects chloride ions. Moreover, the electrolytic cell 1 has a pair of electrode plates 2b and 4b, and electrolyzes water by applying a voltage between these electrode plates 2b and 4b.

When tap water is electrolyzed, reactions of formulas (1) and (2) occur, and oxygen is generated from the anode and hydrogen is generated from the cathode.
Anode: 2H ₂ O → 4H ⁺ + O ₂ + 4e ⁻ (1)
Cathode: 4H ₂ O + 4e ⁻ → 2H ₂ + 4OH ⁻ (2)

Here, by using an electrode coated with platinum / iridium (Pt · IrO ₂ ) as an electrode catalyst, chlorine is generated at the anode as shown in Formula (3).
Anode: 2Cl ⁻ → Cl ₂ + 2e ⁻ (3)

Chlorine becomes chlorine, hypochlorous acid (HClO), and hypochlorite ion (ClO ⁻ ) depending on pH (see Formulas 4 and 5). Hypochlorous acid (HClO) and hypochlorite ion (ClO ⁻ ) have bactericidal power.
Anode: Cl ₂ + H ₂ O → HClO + H ₂ + Cl ⁻ (4)
Anode: HClO → ClO ⁻ + H ⁺ (5)

  Since chloride ions in tap water are attracted to the anode before reaching the reaction of formula (3), chloride ions are applied to the anode surface by applying a voltage that does not cause the reaction of formula (3). It can be collected unreacted.

  Next, the procedure for determining the first voltage by the control unit 24 will be described with reference to FIG. FIG. 4 is a flowchart showing a procedure for determining the first voltage. The flow shown in FIG. 4 is performed at the first energization after the installation of the apparatus or periodically.

  In step S <b> 11, the discharge valve 30 is opened to form a flow in the flow path 16. In step S12, the electrical conductivity of water is measured using the pair of electrodes 2b and 4b provided in the electrolytic cell 1.

  In step S13, the first voltage is determined based on the measured electrical conductivity. FIG. 5 shows an example of the relationship between the electrical conductivity and the first voltage. Such a correspondence relationship is set in advance and stored in the memory of the control unit 24. As illustrated in FIG. 5, it is assumed that the lower the electrical conductivity of water, the lower the chloride ion concentration contained in the supplied water.

  In step S14, the first voltage V1 determined in step S13 is stored in the memory. In step S15, the discharge valve 30 is closed.

  Next, the operation of the control unit 24 when performing sterilization cleaning will be described with reference to FIGS. 6 and 7. FIG. 6 is a flowchart showing the operation of the sterilizing water generator WD shown in FIG. FIG. 7 is a graph showing the movement of each valve, the chloride ion concentration, and the like when the sterilizing water generator WD is operated in the flowchart shown in FIG. 7A shows the open / close state of the discharge valve 30 and the cleaning valve 28, FIG. 7B shows the flow velocity in the vicinity of the electrodes, FIG. 7C shows the voltage applied to each electrode, FIG. 7D shows the chloride ion concentration, FIG. 7E shows the change in electrical conductivity, and FIG. 7F shows the change in hydrogen ion concentration.

  In step S21, the discharge valve 30 is opened to form a flow in the flow path 16 (time t0). In step S22, the first voltage V1 is applied to the pair of electrodes 2a, 4a of the concentration tank 6 (time t1). At the same timing, in step S23, the measurement voltage Vm is applied to the pair of electrodes 2b and 4b of the electrolytic cell 1. In step S24, it is determined whether time T1 has elapsed from the start of application of the first voltage V1, and when time T1 has elapsed, the process proceeds to step S25.

  In step S25, based on the detection result in the electrolytic cell 1, it is determined whether the electrical conductivity σ exceeds the threshold value σ1. If the electrical conductivity σ of the flowing water exceeds the threshold σ1, the process proceeds to step S27, and if not, the process proceeds to step S26. At this stage, as shown in FIG. 8A, collection of chloride ions is in progress.

  In step S26, it is determined whether time T2 (T2> T1) has elapsed since the start of application of the first voltage V1. If the time T2 has not elapsed since the application of the first voltage V1, the process returns to step S25. If the time T2 has elapsed since the application of the first voltage V1, the process proceeds to step S27.

  In step S27, the discharge valve is closed (time t3). In step S28, voltage application to the pair of electrodes 2a and 4a of the concentration tank 6 is stopped. In step S29, an electrolytic voltage Ve (Ve> Vm) is applied to the pair of electrodes 2b and 4b of the electrolytic cell 1. In step S30, the cleaning valve 28 is opened at the opening S2, and sterilizing water is discharged from the cleaning nozzle 14 (time t4). At this stage, as shown in FIG. 8B, chloride ions collected by the pair of electrodes 2a and 4a for concentration move toward the pair of electrodes 2b and 4b for electrolysis. In step S31, it is determined whether time T3 has elapsed since the cleaning valve 28 was opened. If the time T3 has not elapsed, the determination is continued, and if the time T3 has elapsed, the process proceeds to step S32.

  In step S32, the opening degree of the cleaning valve 28 is changed from S2 to S1 (S2> S1). The timing at time t5 is a stage where chloride ions reach the pair of electrodes 2b and 4b and hypochlorous acid is generated as shown in FIG. 8C.

  In step S33, it is determined whether time T4 has elapsed since the opening of the cleaning valve 28 was changed. If the time T4 has not elapsed, the determination is continued, and if the time T4 has elapsed, the process proceeds to step S34.

  In step S34, the cleaning valve 28 is closed. In step S35, the application of voltage to the pair of electrodes 2b and 4b of the electrolytic cell 1 is stopped.

  As described above, the sterilizing water generator WD in the present embodiment electrolyzes water containing chloride ions to generate chlorine at the anode, and generates sterilizing water containing hypochlorous acid by reaction of this chlorine and water. A channel 16 as a water supply channel through which water passes, and a pair of concentrating electrodes 2a and 4a provided in the channel 16 and applying a voltage between the pair of concentrating electrodes 2a and 4a Thus, a concentration tank 6 as a concentration region that attracts chloride ions contained in water passing through the flow path 16 and a flow path 16 on the downstream side of the concentration tank 6 are provided, and a pair of electrolysis electrodes 2b and 4b are provided. The electrolytic cell 1 as an electrolytic cell region for electrolyzing the water flowing through the flow channel 16 by applying a voltage between the pair of electrolysis electrodes 2b and 4b, A voltage applied between the concentration electrodes 2a and 4a and a pair Comprising electrode for electrolysis 2b, the control unit 24 as control means for controlling the voltage applied between 4b, and.

  The control unit 24 passes water so that the flow rate of water in the vicinity of the pair of concentrating electrodes 2a and 4a becomes the first flow rate v1, and applies a voltage to the pair of concentrating electrodes 2a and 4a. The concentration mode (steps S21 to S28 in FIG. 6) for collecting product ions and the flow rate of water in the vicinity of the pair of concentration electrodes 2a and 4a are set to a second flow rate v2 that is faster than the first flow rate v1. Through, the supply mode (steps S30 to S31) in which chloride ions collected by the execution of the concentration mode are separated from the anode and water containing the chloride ions is supplied to the electrolytic cell 1, and a pair of electrodes 2b for electrolysis , 4b is applied with an electrolysis voltage Ve, and an electrolysis mode (steps S29 to S35) in which water supplied from the concentration tank 6 is electrolyzed by execution of the supply mode to generate hypochlorous acid can be executed. It is configured.

  According to the present embodiment, in the concentration mode for collecting chloride ions in water, water is passed so as to have the first flow rate v1, and in the supply mode in which chloride ions are released from the anode, the second flow rate is set to v2. Water is passed, and the second flow velocity v2 is faster than the first flow velocity v1. Accordingly, by supplying water to the pair of concentrating electrodes 2a and 4a at a relatively slow first flow velocity v1, chloride ions in the water are efficiently collected, and relatively fast after the chloride ions are collected. By supplying water to the pair of concentration electrodes 2a and 4a at the second flow velocity v2, chloride ions can be reliably separated from the electrodes in a short time. Thus, since the water which raised the chloride ion density | concentration by supply mode can be supplied to the electrolytic cell 1, a high concentration hypochlorous acid can be obtained.

  In the present embodiment, the control unit 24 preferably applies a preparatory voltage different from the electrolysis voltage Ve to the pair of electrolysis electrodes 2b and 4b. Thus, by applying a preparatory voltage different from the electrolysis voltage Ve to the pair of electrolysis electrodes 2b and 4b, the amount of change in the applied voltage when starting the electrolysis mode and shifting to the electrolysis voltage Ve Can be reduced. Thereby, deterioration of the electrode can be suppressed while the applied voltage is shifted to the electrolysis voltage Ve in a short time.

  In particular, in the present embodiment, the control unit 24 measures the flow of electricity supplied to the electrolytic cell 1 by applying a measurement voltage Vm as a preparation voltage to the pair of electrolysis electrodes 2b and 4b. It is also preferable to shift from the concentration mode to the supply mode based on the transition from a weak state to a strong state of electricity flow.

  As described above, when chloride ions are collected on the anode in the concentration mode, the water quality of the water passing through the electrolytic cell 1 changes due to fluctuations in the chloride ions. More specifically, when chloride ions are collected at the anode, the chloride ion concentration in the water decreases, and the flow of electricity in water becomes weak. Thereafter, when the amount of chloride ions collected at the anode is saturated, the chloride ion concentration in water rises to the maximum, and the flow of electricity in water becomes strong. Therefore, in this preferred embodiment, a measurement that is a preparatory voltage for the pair of electrolysis electrodes 2b and 4b indicates that the flow of electricity flowing through the water supply channel on the downstream side of the electrolytic cell 1 has changed from a weak state to a strong state. Measured by applying the operating voltage Vm, and based on the measurement result, the mode is switched from the concentration mode to the supply mode, and then the mode is switched to the supply mode with a sufficient amount of chloride ions collected at the anode. This makes it possible to reliably obtain a high concentration of hypochlorous acid.

  Moreover, in this embodiment, the flow rate reduction means which adjusts so that the flow rate of the water in the vicinity of a pair of electrodes 2b and 4b for electrolysis may turn into the 3rd flow rate slower than the 2nd flow rate v2.

  As described above, in supplying the chloride ion from the electrode and supplying it to the electrolytic cell 1 in the supply mode, the flow rate of water passing through the flow channel 16 is preferably the relatively high second flow rate v2, but it is as fast as it is. When water is supplied to the pair of electrolysis electrodes 2b and 4b, the amount of water that passes without contributing to the generation of hypochlorous acid increases, and high concentration hypochlorous acid water cannot be generated. Therefore, by providing a flow rate reducing means for adjusting the flow rate of water near the pair of electrolysis electrodes 2b and 4b to be a third flow rate slower than the second flow rate v2, the vicinity of the pair of electrolysis electrodes 2b and 4b is provided. Can be supplied with a high concentration of chloride ions, and can generate a high concentration of hypochlorous acid water.

  In the present embodiment, as one of the flow rate reducing means, the flow rate of water flowing in the flow path 16 is reduced to adjust the flow rate of water in the vicinity of the pair of electrolysis electrodes 2b and 4b. After adjusting the flow rate of water in the vicinity of the pair of concentrating electrodes 2a and 4a to be the second flow rate v2, the flow rate of water flowing through the water supply channel is reduced after a predetermined time has elapsed.

  If the flow rate of water is increased to the second flow rate v2 after collecting chloride ions, it can be estimated how long it will reach the electrolytic cell 1. Therefore, after adjusting the flow rate of water to be the second flow rate v2 in the supply mode, the flow rate of water flowing through the flow path 16 is reduced after a predetermined time has elapsed, so that the pair of electrolysis electrodes 2b, The flow rate in the vicinity of 4b can be lowered, and highly concentrated hypochlorous acid water can be obtained reliably.

  As the flow velocity reducing means, as shown in FIG. 9, the flow path 16 downstream of the pair of concentrating electrodes 2a, 4a has a flow path larger than the flow path cross-sectional area in the vicinity of the pair of concentrating electrodes 2a, 4a. It is also preferable that the flow path expanding portion 16a has a large cross-sectional area, and the pair of electrodes for electrolysis 2b and 4b are arranged in the flow path expanded portion 16a.

  In this preferred embodiment, the flow rate in the vicinity of the pair of electrolysis electrodes 2b and 4b can be reduced with a simple configuration by disposing the pair of electrolysis electrodes 2b and 4b in the flow channel enlargement portion 16a having a wide channel cross-sectional area. It is possible to reliably obtain a high concentration hypochlorous acid water.

  Further, as the flow velocity reducing means, as shown in FIG. 10, the flow path 16 is bent so that stagnation of water flow occurs in the flow path 16 downstream of the pair of concentration electrodes 2a and 4a. It is preferable that the bent portion 16b is provided, and the pair of electrolysis electrodes 2b and 4b is arranged in the flow path bent portion 16b.

  In this preferred embodiment, the flow rate in the vicinity of the pair of electrolysis electrodes 2b and 4b can be reduced with a simple configuration by disposing the pair of electrolysis electrodes 2b and 4b in the flow path bending portion 16b where the flow path is bent. A highly concentrated hypochlorous acid water can be obtained with certainty.

DESCRIPTION OF SYMBOLS 1 Electrolysis tank 2, 4 Electrode plate 6 Concentration tank 10 Channel system 12 Water supply source 14 Washing nozzle 16 Channel 18 Channel 20 Channel 20 Branching portion 22 Drainage channel 24 Control unit 26 Water quality detection unit 28 Cleaning valve 30 Drain valve 32 Drain mechanism 100 Sanitary washing device 110 Western-style toilet 120 Toilet bowl WD Bactericidal water generator

Claims (7)

A waterway through which water passes,
A concentration region provided in the water supply channel, having a pair of concentration electrodes, and attracting chloride ions contained in water passing through the water supply channel by applying a voltage between the pair of concentration electrodes;
Wherein provided on the water supply passage downstream of the enrichment region, a pair of electrode for electrolysis, said electrolysis of water flowing through the water supply passage by applying a voltage between the pair of the electrode for electrolysis pair An electrolytic cell region that generates chlorine at the anode of the electrode for electrolysis and generates sterilizing water containing hypochlorous acid by the reaction of this chlorine and water ;
Control means for controlling the way of water in the water supply channel, the voltage applied between the pair of concentrating electrodes, and the voltage applied between the pair of electrolysis electrodes,
The control means includes
Concentration mode for collecting chloride ions in water by passing water so that the flow rate of water in the vicinity of the pair of concentration electrodes becomes a first flow rate, and applying a voltage to the pair of concentration electrodes;
Water is passed so that the flow rate of water in the vicinity of the pair of concentration electrodes is a second flow rate higher than the first flow rate, and chloride ions collected by the execution of the concentration mode are collected into the pair of concentration electrodes. A supply mode for separating water from the anode and supplying water containing chloride ions to the electrolytic cell region;
An electrolysis mode in which a voltage for electrolysis is applied to the pair of electrolysis electrodes and water supplied from the concentrated region is electrolyzed by execution of the supply mode to generate hypochlorous acid is configured to be executable. A sterilizing water generator characterized by being made.   2. The sterilizing water generating device according to claim 1, further comprising a flow rate reducing unit that adjusts a flow rate of water near the pair of electrolysis electrodes to be a third flow rate that is slower than the second flow rate. The control means includes
The sterilizing water generating device according to claim 2, wherein a preparation voltage different from the electrolysis voltage is applied to the pair of electrolysis electrodes in the supply mode. The control means includes
Measuring the electricity flow of water supplied to the electrolytic cell region by applying a preparatory voltage to the pair of electrolysis electrodes, based on the transition from a weak state to a strong state The sterilizing water generating device according to claim 3, wherein the sterilizing water generating device shifts from the concentration mode to the supply mode. The flow rate reduction means adjusts the flow rate of water in the vicinity of the pair of electrolysis electrodes by reducing the flow rate of water flowing through the water supply channel,
The flow rate of water flowing through the water supply channel is reduced after a predetermined time has elapsed after adjusting the flow rate of water in the vicinity of the pair of concentrating electrodes to be the second flow rate in the supply mode. The sterilizing water generator according to 2. The flow velocity reducing means has a flow channel enlargement portion having a flow channel cross-sectional area larger than a flow channel cross-sectional area in the vicinity of the pair of concentration electrodes in the water supply channel downstream of the pair of concentration electrodes. And
The sterilizing water generation device according to claim 2, wherein the pair of electrolysis electrodes are arranged in the flow path enlarged portion. The flow rate reducing means has a channel bending portion that has a channel bent so that stagnation of the flow of water occurs in the water supply channel downstream of the pair of concentrating electrodes,
The sterilizing water generating device according to claim 2, wherein the pair of electrodes for electrolysis are arranged in the flow path bending portion.

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