JP4914338B2 - Water conditioner - Google Patents

Description

  The present invention relates to a water conditioner including an electrolytic cell that electrolyzes water to produce acidic water and alkaline water.

  Conventionally, a water conditioner is generally provided with an electrolytic tank that can continuously take electrolytic water. As an example, the inside of the electrolytic cell is partitioned and formed through a diaphragm into an anode chamber in which a positive electrode is disposed to generate acidic water and a cathode chamber in which a negative electrode is disposed to generate alkaline water. Some water guide pipes were connected to the anode chamber and the cathode chamber to feed raw water, and acid water and alkaline water could be taken from the water intake pipes connected to each chamber. With such a configuration, it is possible to continuously take in acidic water and alkaline water by passing water between the positive electrode and the negative electrode. Alkaline water, which is considered particularly healthy, is used for drinking. Become.

  In addition, if there is a large amount of dissolved hydrogen in drinking water, for example, bone density has been improved, and there are reports that it is good for health.Therefore, a water conditioner that can take in alkaline water with a high concentration of dissolved hydrogen is desired. It is rare. However, since there is more dissolved hydrogen in stronger alkaline water, the pH value becomes higher when it is attempted to secure the desired amount of dissolved hydrogen, and the desired amount of dissolved hydrogen is generated when alkaline water having a pH of less than 10 is suitable for drinking. We were in a dilemma that we could not secure the amount.

Therefore, the present applicant includes a first electrolysis unit in which an anode and a cathode are arranged to face each other, and a second electrolysis unit that increases the concentration of dissolved hydrogen in the alkaline water generated on the cathode side, and increases dissolved hydrogen. In the past, an alkaline water that can be taken in was proposed (see Patent Document 1).
JP 2005-40781 A

  However, the water conditioner disclosed in Patent Document 1 has a configuration including a first electrolysis unit and a second electrolysis unit, and is essentially a main electrolyzer and a sub-electrolyte 2 in the water conditioner. Since the structure has two electrolytic cells, the structure is inevitably complicated. An object of the present invention is to provide a water conditioner that can solve the above-described problems.

(1) In the present invention, an electrolytic cell having an anode and a cathode arranged opposite to each other is provided. The raw water flowing into the electrolytic cell is electrolyzed so that acidic water and alkaline water can be taken. In a water conditioner having a first level alkaline water production mode, a second level alkaline water production mode, and a third level alkaline water production mode as the production mode, the production mode is disposed between the anode and the cathode. A partition wall that divides the electrolytic cell into an alkaline water generation chamber and an acidic water generation chamber, a tip is branched to communicate with the alkaline water generation chamber and the acidic water generation chamber, respectively, and raw water flowing into the electrolytic cell The raw water supply path that distributes the alkaline water generation chamber and the acidic water generation chamber at a predetermined ratio, and the alkaline water generated in the alkaline water generation chamber in communication with the alkaline water generation chamber is discharged. An alkaline water extraction flow path, a drain flow path that communicates with the acidic water generation chamber and discharges acidic water generated in the acidic water generation chamber, and the alkaline water extraction flow branches off from the middle of the raw water supply path A raw water bypass passage communicating with the road is provided, and the raw water in the raw water supply passage is distributed at a predetermined ratio between the raw water bypass passage and the electrolytic cell, and a strong pH of 10 or more generated by the alkaline water generation chamber. Drinking that allows alkaline water having a pH of less than 10 containing at least 300 ppb or more of dissolved hydrogen to be taken in by reducing the alkalinity of the strongly alkaline water having a pH of 10 or more by supplying the raw water to the alkaline water through the raw water bypass channel a optimization unit, in each level alkaline water generating mode is once voltage der applied to generate a strongly alkaline water However, the voltage levels are made different so that a relatively high voltage in the order of the first level alkaline water generation mode, the second level alkaline water generation mode, and the third level alkaline water generation mode is applied to the anode and the A water conditioner was applied to the cathode .

(2) In the water conditioner according to (1), the strong alkaline water is a strongly alkaline water having a pH of 11 containing 1500 ppb of dissolved hydrogen, and the alkaline water having a pH of less than 10 includes a dissolved hydrogen of 300 ppb. It is characterized by being alkaline water having a pH of 9.5.

  According to the present invention, alkaline water having a sufficient amount of dissolved hydrogen and having a pH of less than 10 suitable for drinking can be efficiently obtained with a very simple configuration.

  The water conditioner according to this embodiment is capable of taking alkaline water containing a sufficient amount of dissolved hydrogen while having a pH of less than 10 suitable for drinking, and is an electrolytic cell in which an anode and a cathode are arranged to face each other. In a water conditioner capable of taking acidic water and alkaline water by electrolyzing raw water flowing into the electrolytic cell, reducing the alkalinity of strongly alkaline water having a pH of 10 or more generated by the electrolytic cell. It is set as the structure provided with the drink optimization means which can take in alkaline water less than pH10.

  That is, the market demands a water conditioner that can take in alkaline water with a high concentration of dissolved hydrogen, but as shown in the graph of FIG. 1, dissolved hydrogen increases rapidly when the pH exceeds 10. It is known that more strongly alkaline water exists. On the other hand, since the alkaline water permitted to be drunk is set to a pH of less than 10, the alkaline water taken with a general water conditioner does not contain a desired amount of dissolved hydrogen such as 300 ppb or more.

  Therefore, in the present embodiment, after once producing strong alkaline water having a pH of 10 or more containing a large amount of dissolved hydrogen, the alkalinity of the strong alkaline water is lowered by the drinking optimization means, so that the pH is less than 10 suitable for drinking. However, alkaline water containing at least 300 ppb or more of dissolved hydrogen is generated.

  The electrolytic cell may have a conventionally known configuration. For example, the electrolytic cell is divided into a first electrode chamber in which the first electrode is disposed and a second electrode chamber in which the second electrode is disposed, with a diaphragm interposed therebetween. The formed one can be suitably used. With such a configuration, each electrode is energized to electrolyze raw water in each electrode chamber of the electrolytic cell with one as a positive electrode and the other as a negative electrode. Alkaline water can be obtained from the side.

  At this time, the electrolytic cell is divided into an alkaline water generation chamber and an acidic water generation chamber, and purified water as raw water flowing into the electrolytic cell is distributed to the alkaline water generation chamber and the acidic water generation chamber at a predetermined ratio. Can do. For example, the amount of purified water inflow into the alkaline water generation chamber and the amount of purified water inflow into the acidic water generation chamber are set to 4: 1. Therefore, the amount of acidic water produced is less than that of alkaline water.

  An outline as a water conditioner provided with drinking optimization means will be described with reference to schematic diagrams shown in FIGS.

  As a drinking optimization means, the structure shown to Fig.2 (a) can be considered, for example. That is, the electrolytic cell 1 is divided into an alkaline water generation chamber 2 and an acidic water generation chamber 3. Reference numeral 4 denotes a raw water supply passage for supplying raw water, which is neutral water having a pH of about 7, to the electrolytic cell 1, and a water purifier 5 for purifying the raw water is provided in the middle, and the tip is branched to generate alkaline water. The chamber 2 and the acidic water generation chamber 3 are communicated with each other. Reference numeral 6 denotes a flow path switching valve provided in the raw water supply path, and reference numeral 7 denotes a water intake flow path whose base end communicates with the alkaline water generation chamber 2 so that alkaline water can be taken. 8 is a drainage channel having a base end communicating with the acidic water generation chamber 3, and the acidic water flows out. As described above, since the amount of acidic water is smaller than that of alkaline water, alkaline water is used. When water is taken, there is little acidic water flowing out from the drainage flow path 8 as waste water, and water can be saved.

  In this example, the first electrode disposed in the alkaline water generation chamber 2 is a positive electrode, and the second electrode disposed in the acidic water generation chamber 3 is a cathode. However, since the polarity of the electrode can be reversed, the alkaline water generation chamber 2 and the acidic water generation chamber 3 may be interchanged.

  An example of the drinking optimization means in the above configuration is an alkaline water extraction flow that is a water intake flow channel that branches off from the middle of the raw water supply channel 4 via the flow switching valve 6 and discharges the alkaline water generated in the electrolytic cell 1. The raw water bypass passage 9 communicated with the passage 7 is provided. In this embodiment, the raw water (purified water) in the raw water supply path 4 is distributed to the raw water bypass flow path 9 and the electrolytic cell 1 through the flow path switching valve 6 at a predetermined ratio. Here, the flow path switching valve 6 has a function as a flow rate adjustment valve, and by adjusting the opening of the valve body, the flow path is closed from the state where the flow path is closed and the flow rate is zero. The flow rate can be adjusted as appropriate until the valve is fully opened and all flows out in one direction.

  In this example, the opening degree of the valve body of the flow path switching valve 6 is set so that the ratio of the flow rate to the raw water bypass flow path 9 and the flow rate to the electrolytic cell 1 side is 4: 1.

  With this configuration, when alkaline water having a pH of less than 10 (for example, about pH 9.5) that can be used for drinking is taken for drinking, 1/5 of the total flow rate of purified water (raw water) is supplied to the electrolytic cell 1. Thus, strong alkaline water exceeding pH 10 can be easily generated in the alkaline water generation chamber 2 by electrolyzing water without requiring large electric power. This strong alkaline water contains a large amount of dissolved hydrogen (see FIG. 1).

  On the other hand, 4/5 of the total flow rate of purified water (raw water) flows to the raw water bypass channel 9. However, as described above, strong alkaline water contains a large amount of dissolved hydrogen. Therefore, even when purified water is mixed and diluted, the degree of alkalinity decreases slightly while still retaining sufficient dissolved hydrogen. Alkaline water suitable for drinking having a pH of less than 10 can be obtained.

  Of the raw water supplied to the electrolytic cell 1, 4/5 flows into the alkaline water generation chamber 2 and 1/5 flows into the acidic water generation chamber 3. Thus, 1/25 of the amount of water flowing through the raw water supply channel 4 is sufficient, and water can be saved without unnecessarily increasing the amount of discarded water.

  As described above, the drinking optimization means according to the present embodiment branches from the middle of the raw water supply path 4 through which the raw water flows into the electrolytic cell 1 via the flow path switching valve 6 having a flow rate adjusting function. The raw water bypass flow passage 9 communicated with the alkaline water extraction flow passage 7 for discharging the alkaline water generated in step 1 is provided, and the raw water in the raw water supply passage 4 is supplied to the raw water bypass flow passage 9 and the electrolytic cell 1 in a predetermined manner. However, as a modification thereof, the configuration shown in FIG. 2B can be adopted.

  That is, the flow rate is changed to a raw water bypass flow path at a predetermined ratio (4: 1) instead of the flow path switching valve 6 to the branch portion where the raw water bypass flow path 9 branches from the raw water supply path 4 through which the raw water flows into the electrolytic cell 1. 9 and the electrolytic cell 1 are provided with a throttle 61, and an electromagnetic on-off valve 62 is provided in the middle of the raw water bypass passage 9.

  Even with such a configuration, alkaline water suitable for drinking containing a large amount of dissolved hydrogen and having a pH of less than 10 can be obtained by mixing and diluting the purified water from the raw water bypass passage 9 with strong alkaline water containing a large amount of dissolved hydrogen. Can be obtained.

  As another embodiment of the drinking optimization means, the configuration shown in FIG. 3 may be adopted. In FIG. 3, the same components as those shown in FIG. 2 are denoted by the same reference numerals, and description thereof is omitted here.

  The drinking optimization means shown in FIG. 3 includes an acidic water branch channel 81 that joins acidic water generated in the electrolytic cell 1 with strongly alkaline water generated in the electrolytic cell 1. The acidic water branch flow path 81 branches from the middle of the drainage flow path 8 serving as the acidic water extraction flow path for discharging the acidic water generated in the electrolytic cell 1 via the flow path switching valve 6 having a flow rate adjusting function. The alkaline water extraction flow path 7 for discharging the strong alkaline water generated in the electrolytic cell 1 communicates with the alkaline water extraction flow path 7.

  According to the drinking optimization means having such a configuration, after strongly alkaline water having a pH of 10 or more containing a large amount of dissolved hydrogen is once generated, the strongly alkaline water is mixed with acidic water generated at the same time when the strongly alkaline water is produced. Drinking optimization can be achieved by below pH 10. Therefore, it is possible to take alkaline water containing at least 300 ppb or more of dissolved hydrogen while the pH is less than 10 suitable for drinking.

  In this way, it is possible to effectively use the acidic water that has been discarded when alkaline water is taken, resulting in a significant water-saving effect. In particular, the distribution ratio of the raw water to the alkaline water generation chamber 2 and the acidic water generation chamber 3, the volume ratio of each chamber 2 (3), the energization amount to each electrode disposed in the electrolytic cell 1, and the like are appropriately determined. Accordingly, the amount of drainage from the drainage flow path 8 of the acidic water produced in the acidic water production chamber 3 can be set to zero, and can be used for diluting all strongly alkaline water without using it as waste water. An effect can be obtained.

  As still another embodiment of the drinking optimization means, the configuration shown in FIG. 4 may be adopted. In FIG. 4, the same components as those shown in FIG. 2 and FIG. 3 are denoted by the same reference numerals, and description thereof is omitted here.

  The drinking optimization means shown in FIG. 4 is configured to include a pH adjuster 72 containing a pH adjuster in the alkaline water extraction channel 7 for discharging alkaline water generated in the electrolytic cell 1. Here, the pH adjusting unit 72 is branched from the middle of the alkaline water extraction flow path 7 via the flow path switching valve 6 having a flow rate adjusting function, and merges with the alkaline water extraction flow path 7. Is provided.

  With such a configuration, after generating strong alkaline water having a pH of 10 or more containing a large amount of dissolved hydrogen, the pH adjuster is dissolved and mixed in the strong alkaline water, and the drinking-optimized alkaline water is taken to a pH of less than 10. Can do. That is, it is possible to take alkaline water containing at least 300 ppb or more of dissolved hydrogen while having a pH less than 10 suitable for drinking.

  Examples of the pH adjuster include citric acid and trisodium citrate. Of course, you may use acidic foods, such as lemon. In any case, any material that is not inconvenient for use in drinking water and that can optimize drinking of strongly alkaline water can be used.

  Hereinafter, a more specific configuration of the water adjuster according to the above-described embodiment will be described with reference to FIGS. FIG. 5 is a schematic explanatory diagram including the internal configuration of the water adjuster according to the first embodiment, FIG. 6 is a schematic explanatory diagram including the internal configuration of the water adjuster according to the second embodiment, and FIG. It is a schematic explanatory drawing containing the internal structure of the water adjuster which concerns on an Example. 5 to 7, the same constituent elements as those in FIGS. 2 to 4 are denoted by the same reference numerals.

  As shown in FIG. 5, the configuration of the water conditioner is large, an electrolysis unit including an electrolysis tank 1 that electrolyzes raw water, and a water purification unit including a water purification device 5 that purifies raw water supplied to the electrolysis tank 1 in advance. And an addition section for adding a predetermined additive to the purified raw water (purified water), and these are housed and disposed in a substantially box-shaped casing 10.

  The electrolytic cell 1 is made of a metal plate such as titanium, and includes a first electrode plate 11 located at the center, a second electrode plate 12 and a third electrode located so as to sandwich the first electrode plate 11. And a plate 13. Then, partition walls 14 are disposed between the first electrode plate 11 and the second electrode plate 12 and between the first electrode plate 11 and the third electrode plate 13, respectively. The first electrolysis chamber 15, the second electrolysis chamber 16, the third electrolysis chamber 17, and the fourth electrolysis chamber 18 are partitioned by the 11, 12 and 13 and the partition wall 14.

  The second electrode plate 12 and the third electrode plate 13 are supplied from a power source (not shown) provided in a functional unit 19 disposed in the vicinity of the bottom of the casing 10, and have the same polarity as the cathode or the anode. On the other hand, the first electrode plate 11 has a polarity opposite to that of the second electrode plate 12 and the third electrode plate 13. Here, the second electrode plate 12 and the third electrode plate 13 are cathode plates, the first electrode plate 11 is an anode plate, and the first electrolysis chamber 15 and the fourth electrolysis chamber 18 are illustrated in FIG. The second electrolysis chamber 16 and the third electrolysis chamber 17 correspond to the acidic water generation chamber 3 corresponding to the alkaline water generation chamber 2 shown in FIGS. On the other hand, when the second electrode plate 12 and the third electrode plate 13 are anode plates, the first electrode plate 11 is a cathode plate, and the first electrolysis chamber 15 and the fourth electrode plate are connected. The electrolysis chamber 18 corresponds to the acidic water generation chamber 3, and the second electrolysis chamber 16 and the third electrolysis chamber 17 correspond to the alkaline water generation chamber 2.

  Each electrolysis chamber 15, 16, 17, 18 is provided with an inlet and an outlet for water, and the flow paths communicating with the respective outlets of the first electrolysis chamber 15 and the fourth electrolysis chamber 18 merge with each other. Thus, the alkaline water extraction flow path 7 is formed, and alkaline water having a desired pH can be taken from the alkaline water extraction flow path 7. On the other hand, the flow paths communicating with the outlets of the second electrolysis chamber 16 and the third electrolysis chamber 17 merge with each other to form the drainage flow path 8 and are acidified via an electromagnetic valve 42 provided near the discharge port. Water can be drained. As described above, if the polarities of the electrode plates 11, 12, 13 are reversed, naturally, acidic water is taken from the flow path as the alkaline water take-out flow path 7, and alkaline water is taken from the drain flow path 8. Will be drained.

  The raw water supply path 4 is branched and connected to the inlets of the first electrolysis chamber 15, the second electrolysis chamber 16, the third electrolysis chamber 17, and the fourth electrolysis chamber 18. In the embodiment, the flow rate flowing into the first electrolysis chamber 15 and the fourth electrolysis chamber 18 from the raw water supply path 4 and the flow rate flowing into the second electrolysis chamber 16 and the third electrolysis chamber 17 are 4: 1. It is set to be. Further, the branch upstream side of the raw water supply channel 4 and the drainage channel 8 are connected via a check valve 41. This check valve 41 always stops the flow of water from the drainage flow path 8 toward the raw water supply path 4, and when there is water pressure during water flow, the flow of water toward the raw water supply path 4 In addition, the flow of water in the direction from the raw water supply path 4 to the drainage flow path 8 is stopped.

  As shown in the figure, the electrolytic cell 1 is supplied with water from a water pipe 20 via a water tap 21. A branch tap 22 is disposed on the water tap 21, and a water supply hose is connected to the branch tap 22. One end of the water supply hose 23 is connected to the inflow port of the lower water purification cartridge 51 built in the water purifier 5. The lower water purification cartridge 51 is mainly filled with activated carbon.

  The outlet of the lower water purification cartridge 51 is connected to the inlet of the upper water purification cartridge 52. The upper water purification cartridge 52 is a filtering means capable of removing germs such as a hollow fiber membrane in addition to a relatively coarse filter such as a metal mesh, a cloth material, and filter paper. Thus, the purified water that is the raw water supplied from the water pipe 20 passes through the water purification device 5 and is purified.

  Further, the outlet of the upper water purification cartridge 52 is connected to the inlet of the flow sensor 53. The flow sensor 53 is configured to be able to measure the amount of flowing water. For example, a propeller is provided at the center of the flow sensor 53 and the amount of flowing water is measured based on the number of rotations of the propeller. The outlet of the flow sensor 53 is connected to the inlet of the water channel switching valve 54. The water channel switching valve 54 has two outflow ports for one inflow port, one outflow port is connected to the salt addition tube 55 through the water channel, and the other outflow port is connected to the calcium addition tube 56 through the water channel. Connected. Therefore, the purified water flows into either the salt-added tube 55 or the calcium-added tube 56 by switching the water channel.

  The salt addition tube 55 contains salt for making water strongly acidic in the electrolytic cell 1, and the calcium addition tube 56 contains a calcium agent for adding calcium to the purified water. However, as shown in the figure, the water channel connected to the outlet of the salt addition tube 55 and the water channel connected to the calcium addition tube 56 merge to form the raw water supply channel 4. In the figure, 57 is a check valve provided in the water channel between the salt addition cylinder 55 before joining and the joining part.

  The function unit 19 includes a control circuit 19a that controls various functions of the water conditioner according to the present embodiment. The flow rate sensor 53, the first electrode plate 11, the second electrode plate 12, and the third The electrode plate 13 is electrically connected. The flow sensor 53 outputs the detected electrical signal to the control circuit 19a, and the control circuit 19a calculates the water flow rate from the flow sensor 53 using the electrical signal. The first electrode plate 11, the second electrode plate 12, and the third electrode plate 13 are indirectly connected to the control circuit 19a, and the control signal given by the user through the panel operation of the control circuit 19a. Is applied to the electrode plates 11, 12, and 13. The panel operation performed by the user refers to an operation of an operation panel (not shown) disposed on the surface of the casing 10 of the water adjuster. The operation panel includes, for example, a power button, ORP display button, water flow rate display button, strong alkaline water supply button, alkaline water supply button, purified water supply button, acid water supply button, sanitary water (strong acid water) supply provided for each level from weak alkali to strong alkali Buttons are provided. In addition, a display unit such as a 7-segment LED that displays information such as a pH value, an ORP value, and a water flow rate is also provided.

  The power button is a button for activating the water conditioner, and is an effective button in any state. Even if the power button is pressed, if the process such as the drainage process is not completed, it is preferable that these processes are completed and the power is turned off. The ORP display button is a button for displaying the current water ORP on the 7-segment LED. The water flow amount display button is a button for displaying the current water flow amount on the 7-segment LED. The strong alkaline water supply button is a button for instructing the water adjuster to generate strong alkaline water. Strong alkaline water, for example, has a pH of 10.5, and can be used for boiled food, acupuncture, boiled vegetables and the like.

  The first level alkaline water supply button is a button for instructing the water regulating apparatus to generate the first level alkaline water. The first level alkaline water has a pH of 9.5, for example, and can be used for cooking, tea and the like. The second level alkaline water supply button is a button for instructing the water regulating apparatus to generate the second level alkaline water. The second level alkaline water has a pH of 9.0, for example, and can be used for cooking rice or the like. The third level alkaline water supply button is a button for instructing the water regulating apparatus to generate the third level alkaline water. The third level alkaline water has a pH of 8.5, for example, and can be used as water for starting drinking.

  The purified water supply button is a button for instructing the water purifier to pass water from tap water as it is without generating ionic water. The acidic water supply button is a button for instructing the water adjuster to generate acidic water. Acidic water has a pH of 5.5, for example, and can be used for face washing, boiled noodles, tea astringents, and the like. The sanitary water supply lamp indicates that the present water conditioner is in the sanitary water generation mode. Sanitized water has a pH of 2.5, for example. Since the life setting upper button also has a different life depending on the type of the upper water purification cartridge 52, the life setting of the upper water purification cartridge 52 is set. Normally, this button is used up to now when the cartridge is replaced. This is performed once when a cartridge different from the used cartridge is set and used. The life setting lower button is the same as the life setting upper button except that it is for the lower water purification cartridge 51. The reset button resets the accumulated water flow amount that has been accumulated until now, and actually clears the accumulated water flow amount counter present in the control circuit 19a. This reset button is enabled by long-pressing for 2 seconds, and prevents the integrated water flow rate from being reset by being erroneously pressed. This reset button is performed when the upper water purification cartridge 52 or the lower water purification cartridge 51 is replaced. The strong alkaline water supply button, the first level alkaline water supply button, the second level alkaline water supply button, the third level alkaline water supply button, the purified water supply button, and the acidic water supply button are currently enabled. The button is lit and visible to the user. In addition, a temperature increase lamp for informing the user when a temperature increase in the electrolytic cell 1 occurs is also provided on the operation panel.

  As explained with each button, in this water purifier, an alkaline water generation mode for supplying alkaline water, a purified water mode for supplying purified water, an acidic water generation mode for supplying acidic water, and sanitary water are supplied. There are four generation modes, sanitary water generation mode.

  The alkaline water generation mode includes a strong alkaline water generation mode, a first level alkaline water generation mode, a second level alkaline water generation mode, and a third level alkaline water generation mode in the order of strong alkalinity. In the alkaline water generation mode, with the electromagnetic valve 42 opened, the second electrode plate 12 and the third electrode plate 13 are used as cathode plates and the first electrode plate 11 is used as an anode plate under the control of the control circuit 19a. To do.

  In the first to third level alkaline water generation modes, alkaline water that can be consumed is generated. However, as shown in FIG. 1, in the present embodiment, the amount of dissolved hydrogen is usually at a level of 110 ppb or less. According to the water conditioner according to the present invention, once strongly alkaline water having a pH of 10 or more, preferably 10.5 or more containing a large amount of dissolved hydrogen is generated, and then drinking is optimized by drinking optimization means. Alkaline water containing at least 300 ppb or more of dissolved hydrogen can be produced while the pH is less than 10 suitable for drinking.

  Further, in the water purification mode, no voltage is applied to any of the electrode plates 11, 12, 13 with the electromagnetic valve 42 closed, that is, no electrolysis is performed. Here, by closing the electromagnetic valve 42, useless water is not discharged from the discharge port 63. In the acidic water generation mode, the second electrode plate 12 and the third electrode plate 13 are used as an anode plate and the first electrode plate 11 is used as a cathode plate under the control of the control circuit 19a, contrary to the alkaline water generation mode. To do.

  In the above configuration, the feature of the present embodiment is that it includes drinking optimization means. In this embodiment, raw drinking water is fed from the middle of the raw water supply path 4 through the throttle unit 61 as drinking optimization means. The bypass flow path 9 is branched, and the leading end of the raw water bypass flow path 9 is communicated with the alkaline water extraction flow path 7 via an electromagnetic open / close valve 62.

  In the throttle unit 61, the flow rate is distributed approximately 4: 1 between the raw water bypass flow path 9 and the electrolytic cell 1. Therefore, for example, when the first level alkaline water (pH 9.5) supply button is operated, the control circuit 19a opens the electromagnetic on-off valve 62 and moves to the first to third electrode plates 11-13. The applied voltage is raised to the same level as or higher than when the strong alkaline water supply button is operated, and the purified water whose flow rate is reduced to 1/5 by the throttle unit 61 is electrolyzed, and dissolved hydrogen is 1500 ppb at about pH 11 The first level alkaline water having a pH of 9.5 is obtained by once generating strong alkaline water of a certain level and diluting the strong alkaline water with purified water corresponding to 4/5 of the total supply purified water supplied from the raw water bypass passage 9. However, alkaline water containing about 300 ppb of dissolved hydrogen can be supplied.

  The storage unit of the control circuit 19a stores a table in which the relationship between the alkaline water generation mode at each level that takes a desired pH value and the applied voltage is optimized in advance, and the control circuit 19a stores such a table. With reference to the first level alkaline water generation mode, the second level alkaline water generation mode, and the third level alkaline water generation mode, a relatively high voltage is applied in this order. Of course, the higher the applied voltage, the stronger the alkali, so the amount of dissolved hydrogen also increases.

  In addition, as shown in FIG. 2A, the throttle unit 61 can be eliminated and the raw water bypass flow path 9 can be branched from the raw water supply path 4 via the flow path switching valve 6 having a flow rate adjusting function. .

  Next, a second embodiment of the drinking optimization means will be described with reference to FIG. The water conditioner is substantially the same as that of the first embodiment except for the configuration of the drinking optimization means, and only different points will be described, and other descriptions will be omitted. The difference is that in the previous embodiment, the flow rate of flowing from the raw water supply channel 4 into the alkaline water generation chamber 2 (the first electrolysis chamber 15 and the fourth electrolysis chamber 18) and the acidic water generation chamber 3 (second electrolysis chamber 2). Although the flow rate flowing into the electrolysis chamber 16 and the third electrolysis chamber 17) was set to be 4: 1, it is set to 2: 1 here.

  As shown in the figure, the drinking optimization means here includes an acidic water branch channel 81 that joins the acidic water generated in the electrolytic cell 1 with the strong alkaline water generated in the electrolytic cell 1. The acidic water branch flow path 81 is a drainage that becomes an acidic water extraction flow path for discharging the acidic water generated in the acidic water generation chamber 3 (second electrolytic chamber 16 and third electrolytic chamber 17) of the electrolytic cell 1. The flow is branched from the middle of the flow path 8 via a flow path switching valve 6 having a flow rate adjusting function, and communicates with an alkaline water extraction flow path 7 for discharging strong alkaline water generated in the electrolytic cell 1.

  According to the drinking optimization means having such a configuration, the control circuit 19a raises the voltage applied to the first to third electrode plates 11 to 13 to the same level as when the strong alkaline water supply button is operated, for example, alkaline In the water generation chamber 2 (the first electrolysis chamber 15 and the fourth electrolysis chamber 18), strong alkaline water having a pH of about 10, 7 to 11.0 and a dissolved hydrogen of about 900 to 1500 ppb is once generated. For example, strong acidic water generated in the acidic water generation chamber 3 (the second electrolysis chamber 16 and the third electrolysis chamber 17) whose inflow rate is reduced to 1/3 is converted into alkaline water by the acidic water branch flow path 81. Therefore, it is possible to reduce the alkalinity by joining only a necessary amount. The amount of strongly acidic water necessary to make alkaline water that can be used for drinking is experimentally known according to the total flow rate of raw water passing through the raw water supply path 4. That is, the mixing ratio of strongly alkaline water and strongly acidic water is known. Therefore, the control circuit 19a controls the valve opening degree of the flow path switching valve 6 so that a required amount of strongly acidic water is obtained according to the total amount of raw water. Then, strongly acidic water that is not used for mixing is discharged from the drainage flow path 8.

  In addition, in the acidic water produced | generated in the electrolytic cell 1, the trihalomethane which has carcinogenicity resulting from the combined chlorine and free chlorine in raw | natural water which could not be removed with the water purifier 5 may exist. Therefore, a trihalomethane removal function part 83 having a function of removing the trihalomethane can be disposed between the acidic water extraction channel (drainage channel 8) of the electrolytic cell 1 and the acidic water branch channel 81. As a specific configuration of the trihalomethane removal function unit 83, an activated carbon treatment apparatus using powdered, granular, or fibrous activated carbon, an ozone generator, or the like can be applied.

  Table 1 shows the measurement results of the pH value and the amount of dissolved hydrogen in alkaline water taken by the drinking optimization means according to this example. In Table 1, the large throttle amount and the middle throttle amount are largely classified according to the ratio of the drainage flow rate to the flow rate taken from the intake channel 7 (nozzle) (flow rate ratio). Further, (1) and (2) in which the amount of restriction is divided and (5) and (6) in which the amount of restriction is divided are the alkaline water generation chamber 2 (first electrolysis chamber) from the raw water supply path 4. The ratio of the flow rate flowing into the chamber 15 and the fourth electrolysis chamber 18) and the flow rate flowing into the acidic water generation chamber 3 (the second electrolysis chamber 16 and the third electrolysis chamber 17) is 5: 2. (3) and (4) in the large amount and (7) and (8) in the narrowed amount are the flow rate flowing into the alkaline water generation chamber 2 from the raw water supply path 4 and the acidic water. The ratio of the flow rate flowing into the generation chamber 3 is 2: 1.

  As shown in Table 1, the alkaline water taken up contains 398-710 ppb of dissolved hydrogen in excess of a sufficient amount while being drinkable with a pH value in the range of 9.16-9.78. I understood.

  If it demonstrates in the example of (1) in Table 1, when the total flow rate as a water conditioner, ie, the amount of water which flows into the electrolytic cell 1, is 2.374 (liter / min), it will flow into the alkaline water production | generation chamber 2 Since the ratio of the flow rate to the acidic water generation chamber 3 is about 5: 2, the flow rate to the alkaline water generation chamber 2 is 1.374 (liters / minute) and the acidic water generation chamber 3 is 1.000 (liters / liter). Minutes).

  Then, strong alkaline water having a pH of about 10.8 and having dissolved hydrogen of about 1100 ppb is once generated in the alkaline water generation chamber 2, and then the pH 2.6 generated in the acidic water generation chamber 3 in this strong alkaline water. Of the strongly acidic water of the degree, an amount of 0.921 (liter / minute) is mixed. 0.079 (liter / min) is drained from the drainage channel 8. Thus, the 2.295 (liter / min) alkaline water taken from the alkaline water take-out flow path 7 had a pH value of 9.570, and 660 ppb of dissolved hydrogen was measured.

Moreover, in this example, as can be seen from the wastewater measurement values in Table 1, a part of the acidic water generated in the acidic water generation chamber 3 is drained, but if it is a drinking optimization means of such a configuration, For example, it is generated in the acidic water generation chamber 3 by appropriately setting the flow rate distribution ratio to the alkaline water generation chamber 2 and the acidic water generation chamber 3, the magnitude of the applied voltage to the electrode plates 11 to 13, and the like. It is also possible to use all of the acidic water for diluting strong alkaline water. In such a case, the amount of drainage from the drainage channel 8 becomes zero, so that a significant water saving effect can be obtained.


Next, a third embodiment of the drinking optimization means will be described with reference to FIG. In addition, since it is the same as that of the 1st Example as a water conditioner except the structure of a drink optimization means, description here is abbreviate | omitted. As shown in the figure, the drinking optimization means in this example is configured to include a pH adjusting unit 72 containing a pH adjusting agent such as citric acid in the alkaline water extraction flow path 7, and the alkaline water extraction Addition of a pH adjuster as a pH adjuster 72 into the branch channel 71 that branches from the middle of the channel 7 through the channel switching valve 6 having a flow rate adjusting function and merges with the alkaline water extraction channel 7 A cylinder 73 is provided.

  Even with such a configuration, in the alkaline water generation chamber 2 (the first electrolysis chamber 15 and the fourth electrolysis chamber 18), strong alkaline water having a pH of 10 or more containing a large amount of dissolved hydrogen is once generated. A predetermined amount is introduced into the branch flow path 71 via the flow path switching valve 6 and passed through the pH adjusting agent addition cylinder 73, so that a pH adjusting agent such as citric acid is dissolved and mixed in the strongly alkaline water. Reduce alkalinity. The alkaline water having a reduced alkalinity and the strong alkaline water that has flowed directly from the alkaline water generation chamber 2 into the alkaline water extraction flow path 7 are mixed together to mix the alkaline water that has been optimized for drinking to a pH of less than 10. Can take water.

  In the water conditioner according to this embodiment, the storage unit of the control circuit 19a stores a table in which the relationship between the final pH value, the raw water amount, and the flow rate that should flow into the branch channel 71 is optimized in advance. The control circuit 19a adjusts the flow rate by the flow path switching valve 6 while referring to this table.

  By the way, in the alkaline water generation mode of each level in the present embodiment, even if the voltage is once applied to generate strong alkaline water, the height of the voltage is varied, and the strong alkaline water generation mode, the first A relatively high voltage is applied in the order of level alkaline water generation mode, second level alkaline water generation mode, and third level alkaline water generation mode. However, in each mode, the same level of strong alkaline water is once generated under the same applied voltage, and then the amount of purified water, acidic water, and pH adjustment mixed with strong alkaline water using drinking optimization means. A predetermined pH value may be obtained by appropriately adjusting the addition amount of the agent.

  The invention of the present application is such that alkaline water having a pH of less than 10 containing dissolved hydrogen exceeding 300 ppb can be obtained by optimizing drinking after once producing strong alkaline water having a pH of 10 or more. Can be realized, the ratio of distributing the flow rate from the raw water supply channel 4 to the alkaline water generation chamber 2 and the acidic water generation chamber 3, the volume of the alkaline water generation chamber 2 and the acidic water generation chamber 3, Specific combinations of numerical values such as the height of the voltage applied to the plates 11 to 13 can be set as appropriate.

It is a graph which shows the relationship between dissolved hydrogen concentration and pH value. It is typical explanatory drawing which shows an example of the drinking optimization means of a water adjuster. It is typical explanatory drawing which shows an example of the drinking optimization means of a water adjuster. It is typical explanatory drawing which shows an example of the drinking optimization means of a water adjuster. It is explanatory drawing which shows the 1st Example of a drink optimization means. It is explanatory drawing which shows the 2nd Example of a drink optimization means. It is explanatory drawing which shows the 3rd Example of a drink optimization means.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Electrolyzer 2 Alkaline water production | generation room 3 Acidic water production | generation room 4 Raw water supply path 6 Channel switching valve 7 Alkaline water extraction channel 8 Drain channel 9 Raw water bypass channel
71 Branching channel 72 pH adjusting unit 81 Acidic water branching channel

Claims (2)

Including the electrolytic bath placed opposite the anode and the cathode, as this raw water to flow into the electrolyzer and electrolyzed to allow intake of the acidic water and alkaline water, generation mode of the alkaline water is water intake, the first level In the water conditioner having the alkaline water production mode, the second level alkaline water production mode, and the third level alkaline water production mode ,
A partition wall disposed between the anode and the cathode to partition the electrolytic cell into an alkaline water generation chamber and an acidic water generation chamber;
A raw water that branches into a tip and communicates with the alkaline water generation chamber and the acidic water generation chamber, respectively, and distributes the raw water flowing into the electrolytic cell to the alkaline water generation chamber and the acidic water generation chamber at a predetermined ratio. A supply channel;
An alkaline water extraction flow path for discharging alkaline water generated in the alkaline water generation chamber in communication with the alkaline water generation chamber;
A drainage channel that communicates with the acidic water generation chamber and discharges acidic water generated in the acidic water generation chamber;
A raw water bypass passage branched from the middle of the raw water supply passage and communicating with the alkaline water extraction passage is provided, and the raw water in the raw water supply passage is distributed to the raw water bypass passage and the electrolytic cell at a predetermined ratio. Then, by supplying the raw water to the strong alkaline water having a pH of 10 or higher generated by the alkaline water generation chamber through the raw water bypass flow path, the alkalinity of the strong alkaline water having a pH of 10 or higher is lowered and dissolved at least 300 ppb or higher. A drinking optimization means that makes it possible to take alkaline water containing hydrogen and having a pH of less than 10 ;
In the alkaline water generation mode of each level, even if the voltage is once applied to generate strong alkaline water, the height of the voltage is varied to change the first level alkaline water generation mode and the second level. A water conditioner, wherein a relatively high voltage is applied to the anode and the cathode in the order of an alkaline water generation mode and a third level alkaline water generation mode . The strong alkaline water is a strong alkaline water having a pH of 11 containing 1500 ppb dissolved hydrogen,
2. The water conditioner according to claim 1, wherein the alkaline water having a pH of less than 10 is alkaline water having a pH of 9.5 containing 300 ppb of dissolved hydrogen.

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