200927665 九、發明說明： ^ 【發明所屬之技術領域】 μ# 日f Ϊ有關具備對水進行電解而生成酸性水及驗性水的電 解槽的登水器。 少 【先前技術】 辨水益一般具備可以連續地提取電解水的電解 ^而’有藉由隔膜將電解槽内劃分形成為配設陽 且在極室和配設陰極而生成鹼性水的陰極室，並 室連通連結導水管而使生水流人，並且利 的取水管可以分別提取酸性水、驗性水的整水 構，利用使水通過陽極及陰極之間而能夠連續地 驗ϊ水’提供雜雜财益騎性錢賊用。 =存會在』，多’因』二::望 性水乃不二境值糊1。的驗 ιϊΐ-ίΓΐ，先提出了具備相對配置了陽極和陰極的第 第二電i部，陰極—側所生成的驗性水的溶解氫漢度的 利文獻1 (參照專 θ 【發明内容】 解部文^所公開的整水器做成具備第一電 副電解構’且實際上在整水器内具備主電解槽和 ⑴在本發明中，在具備相對配置了陽極和陰極的電解槽， 5 200927665 並且對流入該電解槽内的生水進行電解，從而可以提取酸性水和 鹼性水的整水器，做成具備飲用最優化裝置的整水器，該飲用最 優化裝置降低由上述電解槽生成的pH值在10以上的強鹼性水的 鹼度而可以提取pH值不到1〇的鹼性水。 、（2)本發明在上述（丨）所記載的整水器中，其特徵為：將 上述電解槽劃分成鹼性水生成室和酸性水生成室，將流入該電解 ，的生水按照規定的比例向上述鹼性水生成室和上述酸性水生成 室分配。 (3)本發明在上述（1)或⑵所記載的整水器中，其特徵 為·上述飲用最優化裝置，具備從使上述生水流入上述電解槽的 生水供給道的巾間部位分支，並與放出生成於上述電解槽的驗性 水的取驗性水流道連通的生水旁通流道，並且將上述生水供給道 中的生水按照規定的比例向上述生水旁通流道和上述電解槽分 配。 (4)本發明在上述（3)所記載的整水器中，其 裝置，具備按照規定的_向上述生水旁通流道和 上述電解槽分配的流道切換閥。 f5)本發明在上述⑴或⑵所記载的整水器中，其 崎優化裝置，具備使生狀上述電觸的酸性水與 生成於上述電解槽的驗性水合流的流道。 /、 本發明在上述（5)所記載的整水器中，其特徵為：t ϊίίί流道城閥從放出生成於電解槽的酸性水的取i性水 ======—強驗性 驗!·生水*道内具備容納了 pH調節劑的阳調節部。 、 (8)本發明在上述（7)所記載的整水器中，其特微兔. 述pH調節部設置在藉由流道切換閥從放出生成於上述電解槽的 200927665 鹼性水的取鹼性水流道的中間部位分支並與該取鹼性水流道合 的分支流道内。 ” (口9)本發明在上述⑷、⑹、（8)中的任意一項所記载的 整水器中，其特徵為：上述流道切換閥具有流量調節功能。 时（ίο)本發明在上述（D〜中的任意一項所記載的整 水器中，其特徵為：在提取的上述pH值不到1〇的鹼性水内至 含有300ppb以上的溶解氫。 ❹ (11)本發明的方法為，使生水流入相對配置了陽極和险極 的電解機行電解而生成pH值在1G社的驗性水後，通 该鹼性水飲用最優化而生成既pH值不到1〇又至少含有3〇 以上的溶解氫的鹼性水的鹼性水生成方法。 根，本發明，雖然是極其簡單的結構，但能夠有效地得到含 有足夠量的溶解氫且適合於飲用的pH值不到1〇的驗性水。 【實施方式】 有關本實施方式的整水器做成可提取適合於飲用的pH值不 到10且含有足夠的溶解氫量的驗性水，在做成具備相對配置了陽 極和陰極㈣賴’賊人魏解制❾生水a行轉而可以提 S酸性水和驗性水的整水器中’做成具備飲用最優化裝置的结 © 構，該飲用最優化裝置降低由上述電解槽生·ΡΗ值在10以上 的強驗性水的驗度而可以提取pH值不到的驗性水。 即，雖然市場希望提供可以提取提高了溶解氫濃度的鹼性水 的整水器，但如圖1的曲線圖所示，已知溶解氫在1)11值超過10 時急劇增加，越是強鹼性水存在得就越多。另一方面，由於容許 飲用的驗性水的pH值不到10,因此由一般的整水器提取的驗性 水中不，含有例如300ppb以上的所期望的程度的溶解氫量。 於是，在本實施方式中，在先生成了大量含有溶解氫的pH值 以上的賴性錢’通過_上述侧最優化裝置降低該強 鹼性水的鹼度，可以生成適合於飲用的pH值不到1〇且至少含有 7 200927665 300ppb以上溶解氫的鹼性水。 :隔電 inr二電極的第^龄的電㈣採==構^ 的久ίϊΐ通電並使-個作為正極、另—個作為負極赌電解样 =:ί水進行電解’可從正極-側制酸性水，“ 此時’可將電解棚分成驗性水生魅和酸性水 水的淨水按照規定的比例向驗性水生Ϊ 室分配。例如，使向驗性水生成室的淨水流入含 :=iS的淨水流入量為4:1。從而，使得生成的酸: 優絲聯賴式®，—邊朗作為具備飲用最 作為飲用最優化裝置，可考濾例如圖2 (a) 電解槽1劃分成驗性水生成室2和酸性水生成ϋ冓是使 ΡΗ值在7程度的中性水即生水流入t解槽i 水以卜4 $ 於淨魅水财水裝置5,使前端分辽別與驗ί 道切換閥，7是使基端與驗性水生成室2連通的取= 以提取鹼性水。8是使基端與水域室3連通“水流 然使酸性核出’但如_L所述，由於雜水的量 水^ ===:成為廢水而從排水流道8=酸性工 配置:極 顛倒的’因此有雛驗性水生成室2和酸性水生成 上述結構雜水最優化裝置的-侧子是騎了藉由流道切 200927665 換閥6從生水供給道4的中間部位分支，並與取鹼性水流道7連 通的生水旁通流道9的結構，其取鹼性水流道7為將生成於電解 槽1的鹼性水放出的取水流道。而且，在本實施方式中，藉由流 道切換閥6將生水供給道4中的生水（淨水）按照一定比例分配 生水旁通流道9和電解槽1。在此，流道切換閥6具備了作為流 量調節閥的功能，通過調節閥體的開閉度，可以適當地進行從關 閉流道而使流量為零的狀態至全開流道而全部向一個方向流出的 狀態的流量調節。 在該例子中，作為流道切換閥6的閥體的開閉度，將流入生 Q 水旁通流道9的流量和流入電解槽1一側的流量的比例設定成4: 1 ° 根據這種結構’在將能夠供於飲用的pH值不到1〇 (例如pH 值為9.5程度）的驗性水用於飲用而提取的場合，通過使淨水（生 水)的全部流量中的1/5供給至電解槽i内，無需大電力就能對水 進行電解並在鹼性水生成室2内容易地生成pH值超過1〇的強鹼 性水》在該強驗性水中含有大量的溶解氫（參照圖i)。 另一方面，淨水（生水）的全部流量的4/5流入生水旁通流道 9内。然而，如上所述，在強鹼性水中含有大量的溶解氫，從而， ^於即便加進淨水進行稀釋也仍然保持充分的溶解氫，驗度只是 ❹ 韻降低，因此可以制既含有充分的溶解氫且pH值又不到1〇 的適合飲用的給性火。 此外，由於供、給至電解槽i的生水中，4/5流入驗性水生成室 性水生成室3内，因此來自排水流道8成為廢水 的酉夂性水僅為机過生水供給道4的水量的1/25，因此，不會白 地增加廢水，從而可以節水。 嫌.有關本實施方式的飲用最優化裝置做成了如下結 I ϊ ΐ ί有流量調節功能的流道切換閥6從使生水流入 内的二k妨山7供給道4的*間部位*支，並與生成於電解槽1 内的驗性水放di的取驗性水流道7連通的生水旁通流道9,並且使 200927665 生水供給道4中的生水按照規定的比例（4: υ向生水旁通流道9 和電解槽1内分配，但作為其變型例能夠做成圖2 所示的結 構。 。 即，做成如下結構：在從使生水流入電解槽丨内的生水供給 道4分支出生水旁通流道9的分支部上，取代流道切換閥6而設 置依規定的比例（4 : 1)將流量向生水旁通流道9和電解槽i内 分配的節流部61，並且在生水旁通流道9的中間部位配設 開關閥62。 即便根據這種結構，也可以通過在含有大量的溶解氫的強鹼 性;^中混合來自生水旁通流道9的淨水而進行稀釋，而得到含有 大量的溶解氫且pH值不到1〇的適合於飲用的驗性水。 作為飲用最優化裝置的其他實施方式，也能做成圖3所示的 結構。此外，在圖3中，在與圖2中所示的主要構成部件相同的 部件上附註相同符號而表示，在此省略說明。 圖3所示的飲用最優化裝置具備使生成於電解槽丨内的酸性 水與生成於電解槽1内的強驗性水合流的酸性水分支流道81。該 酸性水分支流道81藉由具有流量調節功能的流道切換閥6從成= 放出生成於電解槽1的酸性水的取酸性水流道的排水流道8的中 =部位分支，並與放出生成於電解槽丨内的強鹼性水的取鹼性水 k道7連通。 友根據採用這種結構的飲用最優化裝置，在先生成大量含有溶 ，氫且pH值在1〇以上的強驗性水後，在該強驗性水中混合與生 ^強驗性水時同時生成的紐水、至pH值不到1G而能夠飲用最 優化。從而，可以提取既適合於飲用的pH值不到1〇又至少含 3〇〇ppb以上的溶解氫的鹼性水。 這樣，能夠有效利用提取鹼性水時作為廢水的酸性水，還能 生f顯著的節水效果。尤其’通骑#地決定流人驗性水生成室2 生成室3的生水的分配比例或各室2⑴的容積比、向 置在電簡1的各電㈣·量等，使從生成於雜水生成室3 ❹ ❹ 200927665 的排水流道8的排水量树，也可以不作為廢水而全部 用來稀釋強鹼性水，從而可以得到顯著的節水效果。 所-ϋίί用最優化裝置的進—步的其他實财式，也能做成圖4 構。此外’在圖4中，在與圖2或圖3所示的主要構成 藉相同的部件上附注相同符號而表示，在此省略說明。200927665 IX. Description of the invention: ^ [Technical field to which the invention pertains] μ# A water trap that has an electrolytic tank that electrolyzes water to form acidic water and water. Less [Prior Art] The water-saving benefit generally has an electrolysis capable of continuously extracting electrolyzed water. 'There is a cathode which is formed by a diaphragm to divide the inside of the electrolytic cell into a positive electrode and a basic chamber and a cathode to generate alkaline water. The chamber and the chamber are connected to the connecting water pipe to make the raw water flow, and the profitable water collecting pipe can separately extract the whole water structure of the acidic water and the test water, and the water can be continuously tested by using the water between the anode and the cathode. Providing miscellaneous wealth and riding money thieves. = The existence of the deposit in the "," more than the second two:: Looking at the water is not the same value. In the inspection of ιϊΐ-ίΓΐ, the second document of the second electric i-part having the opposite anode and the cathode, and the dissolved hydrogen of the geochemical water generated by the cathode-side is proposed (refer to the content of the invention). The water purifier disclosed in the section is provided with a first electric sub-electrolysis structure and actually has a main electrolysis cell in the water purifier and (1) in the present invention, an electrolysis cell having an anode and a cathode disposed oppositely , 5 200927665 and electrolyzing the raw water flowing into the electrolytic cell to extract a water purifier of acidic water and alkaline water, thereby forming a water purifier having a drinking optimization device, and the drinking optimization device is lowered by the above The alkaline water having a pH of less than 1 Torr can be extracted from the alkalinity of the strong alkaline water having a pH of 10 or more. (2) In the water eliminator described in the above (丨), It is characterized in that the electrolytic cell is divided into an alkaline water generating chamber and an acidic water generating chamber, and raw water flowing into the electrolytic solution is distributed to the alkaline water generating chamber and the acidic water generating chamber at a predetermined ratio. The present invention is in the above (1) or (2) In the water-storing device, the drinking-optimizing device includes branching from the inter-flank portion of the raw water supply path for allowing the raw water to flow into the electrolytic cell, and releasing the test water generated in the electrolytic cell The raw water bypass passage that communicates with the water passage of the raw water, and the raw water in the raw water supply passage is distributed to the raw water bypass passage and the electrolytic tank at a predetermined ratio. (4) The present invention is as described above (3) In the water separator according to the present invention, the device includes a flow path switching valve that is distributed to the raw water bypass passage and the electrolytic cell in accordance with a predetermined condition. f5) The present invention is described in the above (1) or (2). In the water purifier, the sifting optimization device includes a flow path for causing the acidic water in the above-described electric contact to flow and the hydration flow generated in the electrolytic cell. In the water purifier according to the above (5), the present invention is characterized in that: t ϊ ίίί, the flow channel valve is released from the acidic water generated in the electrolytic cell, ======- Test! The raw water * has a positive adjustment unit that contains a pH adjuster. (8) The water purifier according to the above (7), wherein the pH adjusting unit is provided in the 200927665 alkaline water which is generated from the electrolytic cell by the flow path switching valve. The intermediate portion of the alkaline water flow path branches and branches into the branch flow path where the alkaline water flow path is combined. In the water purifier according to any one of the above aspects (4), (6), or (8), the flow path switching valve has a flow rate adjustment function. In the water purifier according to any one of the above aspects, the extracted water having a pH value of less than 1 Torr is contained in the alkaline water to 300 ppb or more. ❹ (11) In the method of the invention, the raw water is introduced into the electrolysis machine which is disposed opposite to the anode and the dangerous electrode, and the pH is determined by the water of 1G, and the alkaline water is optimally consumed to produce a pH of less than one. The method of producing an alkaline water containing at least 3 or more dissolved hydrogen alkaline water. The present invention has an extremely simple structure, and can effectively obtain a pH containing a sufficient amount of dissolved hydrogen and suitable for drinking. The water-repellent water of the present embodiment is made of an extractable water which is suitable for drinking and has a pH value of less than 10 and which contains a sufficient amount of dissolved hydrogen. With a relatively configured anode and cathode (four) Lai 'thief people Wei Jie system twin water a line It can be made into a water heater with S acidic water and water for verification, which is made into a structure with a drinking optimization device, which reduces the amount of water that is produced by the above-mentioned electrolytic cell and has a devaluation of 10 or more. It is possible to extract an illustrative water having a pH value less than that. That is, although it is desired to provide a water purifier capable of extracting alkaline water having an increased dissolved hydrogen concentration, as shown in the graph of Fig. 1, it is known that dissolved hydrogen is known. When the value of 1) 11 exceeds 10, it increases sharply, and the more alkaline water exists, the more. On the other hand, since the pH of the water for drinking is less than 10, it is extracted by a general water purifier. In the case of the test water, the amount of dissolved hydrogen of a desired degree of, for example, 300 ppb or more is contained. Thus, in the present embodiment, a large amount of pH-dependent money containing dissolved hydrogen is added to the above-mentioned side. The device reduces the alkalinity of the strong alkaline water, and can generate alkaline water suitable for drinking with a pH value of less than 1 〇 and containing at least 7 200927665 300 ppb or more dissolved hydrogen: the electricity of the second electrode of the inr two electrodes (4) Take == constituting ^ for a long time, energizing and making - as a positive electrode Another one as the negative gambling electrolytic sample =: ί water for electrolysis 'can be made from the positive side - side acid water, "At this time, the electrolysis shed can be divided into the water of the aquatic scent and the acidic water in accordance with the prescribed ratio Sexual aquatic sputum distribution. For example, the amount of purified water flowing into the water-producing water generating chamber into the water containing: = iS is 4:1. Thus, the resulting acid: 优丝联赖®, - Bianlang as the most suitable drinking-optimizing device for drinking, can be filtered, for example, Figure 2 (a) Electrolytic cell 1 is divided into anatory water generating chamber 2 and acidic water The formation of ϋ冓 is to make the ΡΗ value at 7 degrees of neutral water, that is, the raw water flows into the t solution tank i water to the 4 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ The base end is connected to the water-producing water generating chamber 2 to extract alkaline water. 8 is to make the base end and the water chamber 3 connected "the water flows to make the acid out" but as described in _L, due to the amount of miscellaneous water ^ ===: becomes waste water from the drainage channel 8 = acidic configuration: pole The inverted side is therefore the side of the raw water supply chamber 2 and the acidic water generating the above-mentioned structural water optimization device. The structure of the raw water bypass passage 9 that communicates with the alkaline water passage 7 is taken as the water intake passage that discharges the alkaline water generated in the electrolytic tank 1. Further, in the present embodiment In the meantime, the raw water bypass passage 9 and the electrolytic tank 1 are distributed to the raw water (purified water) in the raw water supply path 4 by the flow path switching valve 6. Here, the flow path switching valve 6 is provided as The function of the flow rate adjusting valve can appropriately adjust the flow rate in a state in which the flow rate is zero from the state in which the flow rate is zero to the full-open flow path and all flows out in one direction by adjusting the opening and closing degree of the valve body. As the opening and closing degree of the valve body of the flow path switching valve 6, the flow of the raw Q water bypass flow path 9 will flow. The ratio of the amount and the flow rate to the side of the electrolytic cell 1 is set to 4: 1 ° according to this structure 'in the use of water for testing that can be used for drinking at a pH of less than 1 〇 (for example, a pH of 9.5) In the case where the drinking water is extracted, one-fifth of the total flow rate of the purified water (raw water) is supplied to the electrolytic cell i, and the water can be electrolyzed without generating large electric power and easily generated in the alkaline water generating chamber 2. Strong alkaline water with a pH of more than 1 》 contains a large amount of dissolved hydrogen in the potent water (see Figure i). On the other hand, 4/5 of the total flow of purified water (raw water) flows into the raw water bypass. In the flow channel 9. However, as described above, a large amount of dissolved hydrogen is contained in the strong alkaline water, so that even if the purified water is added for dilution, the dissolved hydrogen is sufficiently maintained, and the degree of measurement is only reduced, so A potable fire that contains sufficient dissolved hydrogen and has a pH of less than 1 。. In addition, 4/5 flows into the effluent water generating room of the test water due to the supply and supply to the raw water of the electrolytic cell i. 3, so the alkaline water from the drainage channel 8 to become waste water is only the machine water supply channel 4 The amount of water is 1/25, so that the wastewater is not whitened, so that water can be saved. The drinking optimization device according to the present embodiment is constructed as follows: 流 ί 流 Flow path switching valve 6 having a flow regulating function The raw water flowing into the inner water is supplied to the raw water bypass passage 9 which is connected to the * between the * and the * of the supply channel 4, and is connected to the flowable water flow path 7 of the test water discharge di which is generated in the electrolytic cell 1. Further, the raw water in the raw water supply passage 4 of 200927665 is distributed to the raw water bypass passage 9 and the electrolytic tank 1 in a predetermined ratio (4: υ), but the configuration shown in Fig. 2 can be obtained as a modification. In other words, the branch portion of the raw water bypass passage 9 is branched from the raw water supply passage 4 that allows raw water to flow into the electrolytic cell, and a predetermined ratio is provided instead of the flow path switching valve 6 ( 4: 1) The flow rate is supplied to the raw water bypass passage 9 and the throttle portion 61 distributed in the electrolytic cell i, and an on-off valve 62 is disposed in the middle portion of the raw water bypass flow passage 9. According to this configuration, it is possible to dilute by mixing the purified water from the raw water bypass passage 9 in a strong alkali containing a large amount of dissolved hydrogen, thereby obtaining a large amount of dissolved hydrogen and having a pH of less than 1 验 suitable for drinking water. As another embodiment of the drinking optimization device, the structure shown in Fig. 3 can also be made. Incidentally, in FIG. 3, the same components as those of the main components shown in FIG. 2 are denoted by the same reference numerals, and the description thereof will be omitted. The drinking optimization device shown in Fig. 3 includes an acidic water branch flow path 81 for causing acidic water generated in the electrolytic cell and a strong hydration flow generated in the electrolytic cell 1. The acidic water branch flow path 81 is branched from the middle portion of the drainage flow path 8 of the acidic water flow path of the acidic water generated in the electrolytic cell 1 by the flow path switching valve 6 having the flow rate adjustment function, and is generated by the discharge path The alkaline water in the electrolytic tank is connected to the alkaline water k-channel 7 . According to the drinking optimization device adopting this structure, after mixing a large amount of potent water containing dissolved hydrogen and having a pH of 1 〇 or more, it is mixed with the strong test water in the test water. The generated new water can be optimally drunk until the pH is less than 1G. Thereby, it is possible to extract alkaline water which is suitable for drinking and has a dissolved hydrogen having a pH of less than 1 Torr and at least 3 ppb or more. In this way, it is possible to effectively utilize the acidic water which is used as the waste water when the alkaline water is extracted, and it is possible to produce a remarkable water-saving effect. In particular, it is determined that the distribution ratio of the raw water in the generation chamber 3 or the volume ratio of each chamber 2 (1) and the amount of electricity (four) that is placed in the electric system 1 are generated in the "passing the ground". The water storage chamber 3 ❹ ❹ 200927665 The drainage tree of the drainage channel 8 can also be used as a waste water to dilute the strong alkaline water, so that a significant water saving effect can be obtained. The - ϋίί can also be made into the structure of Figure 4 with the other real-life formula of the optimization device. In addition, in FIG. 4, the same components as those of the main components shown in FIG. 2 or FIG. 3 are denoted by the same reference numerals, and the description thereof will be omitted.
赚示驗用最航裝置做成如下結構：在放出生成於電 驗性水的取驗性水流道7内具備容納了 pH調節劑的pH ϊϊΐ 在t，p„72設置在分支流道71内，該分支支 二由具有流I調節功能的流道切_ 6從取驗性水流道7 的中間部位分支並與該取鹼性水流道7合流。 ㈣結構，錢生献量含有溶解氫的PH值為10以上 接取Ϊίΐί ’將PH調節劑溶解並混入該強鹼性水中，從而能夠 PH值不到1G為止的紐水。也就是說，可以 氫於侧的PH值师G又”含有綱响以上的溶解 尤古j ’作為阳調節劑’可考濾、例如檸檬酸、轉檬酸三納等。 用；以使轉檬等酸性食品。總之，只要適合用於飲 用jc且犯夠使強鹼性水飲用最優化即可。 的禮5〜圖7對有關上述實施方式的整水11的更具體 構的概略=月Ξ °圖5是包含有關第一實施例的整水器的内部結 ，圖6是包含有關第二實施例的整水器的内部結 構的概略^Ξ ’圖7是包含有關第三實施例的整水器的内部結 主要構成部件上使=同==7。中’在與圖2〜圖4相同的 11 200927665 -tSn! : 一電 i〇的底部近旁的功能部自配設於箱體 〇 ίΓϊ的相同極的電極板，另-方面，第二電極二’ ΐΐίί極 =板12和第三電極板η的極性相反的極性。ϊ此1帶4與二第^ ，板12和第二電極板13作為陰極板，而作 成至對應’第—電解室16和第三電解室n 對應:相反，在第二電極板12和第三電極板13成^^ 合，第一電極板11成為陰極板，第一電解室i ^ ^ 與酸性水生成室3對應，第電4 電解室18 水生成室2_。 電解至16和第二電解室17與驗性 〇 在各電解室15、16、17、18上設有水的流入口和流出口與 第-電解室15和第四電解室18的各流出口連通的 流 而形成取雜水流道7,從樣夠從該取紐賴道7提;" 的pH值的鹼性水。另一方面，與第二電解室16和第三電解室口 的各流出口連通的流道彼此合流而形成排水流道8，從而藉由設置 在排出口近旁的電磁閥42可以排出酸性水。如上所述，若對調各 電極板11、12、13的極性，則理所當然能夠從作為取鹼性水^道 7的流道提取酸性水，從排水流道8排出鹼性水。 雖然在第一電解室15、第二電解室16、第三電解室17、第四 電解室18的流入口上分別分支連接有生水供給道4，但在本實施 方式中，將從生水供給道4流入第一電解室15及第四電解室18 的流量和流入第二電解室16及第三電解室17的流量設定成4 : 12 200927665 • 1。另外，生水供給道4的分支上游側和排水流道8藉由止回閥41 進行連接。該止回閥41平時阻止水從排水流道8向生水供給道4 方向的流動，並且在通水時的存在水壓的場合，不僅阻止水向生 水供給道4方向的流動’還阻止水從該生水供給道4向排水流 方向的流動。 如圖所示，這種電解槽1接受從水管20通過水龍頭21供給 ❾水，在水龍頭21上配設有分支栓22，在這種分支栓22上連接 了水軟g 23的一端，而同一給水軟管23的另一端連接在内置於 it·裝ΐ 淨水濾筒51驗人口上。此外，在下淨水濾、筒 0 51内主要填充有活性炭。 下淨水濾筒51的流出口連接在上淨水濾筒52的流入口上。 ΐίΐΪΐ 52做成除了使用金屬網或布質材料、濾、紙等的比較稀 以外，還使用如中空絲膜（membranethrcad)那樣的 =菌轉可以除去的猶裝置，樣，使得從水管2()供給的生 水即淨水通過淨水裝置5而淨化。 π t另1卜二上淨水濾筒52的流出σ連接在流量感測器53的流入 ％構成為可以測定流水量，例如在流量感測器 蚤设有螺旋樂，通過這種螺旋躺旋轉次數來測定流 ο 53的流出σ連接在水道切換閥54的流入口上。 水、首、^垃二表4略對於一個流入口具有兩個流出口’一個流出口通過 力f f添加筒55上，另-嫩㈣通過水道連接在鈣添 添丄θ π ^ Ξ，通過水道切換使淨水流入食鹽添加筒55或詞 添加筒56的任意一個中。 酸性55内容納有用於使水在電解槽1内呈強 劑，张在加筒56内容納有用於在淨水裏添加鈣 在辦，連接在食鹽添加筒55的流出口上的水道和連接 在人1‘=入&上的水道合流而形成生水供給道4。圖中57是設置 口 =别的艮孤添加筒55和合流部之間的水道上的止回閥。 述力月b。卩19具備有對有關本實施方式的整水器的功能進 13 200927665 行各種控制的控制電路19a，並電連接在流量感測器53、第一電 極板11、第二電極板12、第三電極板13上。流量感測器53將檢 測的電信號輸出至控制電路19a上，控制電路19a利用來自流量 感測器53的電信號計算通水量。由於第一電極板^、第二電極板 12第一電極板13間接地連接在控制電路上，因此控制電路 19a基於通過用戶的面板操作而輸入的控制信號，在電極板^、 12、13土施加電壓。此外，用戶進行的面板操作是指對配設在整 水器的箱體10表面的操作面板（未圖示）的操作，在這種面板上 設有例如電源按鈕、ORP (高氧化還原電位〇xidati〇n reducti〇n potential)顯示按知、通水量顯示按知、強鹼性水供給按鈕、設置 在弱鹼至強鹼的每個級別的鹼性水供給按鈕、淨水供給按鈕、酸 性f供給按紐、衛生水（強酸性水）供給按鈕等。另外，還設有 顯示pH值、ORP值、通水量等資訊的七段LED等的顯示部^ ，源按紐是用於啟動本整水器的按紐，是無論在何種狀態下 按紐。在即便按下電源按紐’正在進行排水處理等處 ^的汉備也不停止的場合，祕做成在這些處雜束後斷電。0即 ，不於在上述七段LED上顯示當前的水的0RP值的按 ΐ 顯ΐ按紐是用於在上述七段卿上顯示當前的水的通 水供給触是胁指示本整水器生成強驗性 味、煮蔬菜ί驗性水ΡΗ值例如為10·5 ’能夠使用在煮食、去除澀 水的本邮蝴一級驗性 欠：楚丄=f 例如為9.5，能夠使用在做菜、泡 3的是崎㈣轉水11域第二級驗 的按鈕。第三級鹼性水pH值例如為85 “生成第二級鹼性水 ，火由^為8·5’能夠用作可飲用的水等。 來水水器不生成離子水而使來自自 來水的水健雜地直接通。.賴給餘是用於指 200927665 成fr紐。酸性㈣μ，並且能 ^^衛生摘生絲柄燈。齡水 同，區別僅在於針對下淨水诘饩丨丨^ 用可命叹疋上按鈕相 直累計到當前的通t零按蝴於對一 Ο 水量進行歸零。該歸零触在按 時才有效’從而可以防止因弄錯而按下 ::4 歸零按鈕在更換上淨水濾筒52或 '芮 $ 零。该 上述強鹼性水#认；^4#楚&淨夂濾旖5〗的％合使用。就 供給it第===性=給按紐、第二級驗性水 此外，在操作面板地己置= 度^^;^可= 見覺辨認。 燈用於在電解槽i内發生溫度上升的“告^厂度上升指不 ❹ 種生按ί所進行的綱’在本整水財，大體分為以下四 ^供、..酸性水的酸性水生成模式、供給衛±水的衛生水生= 成模成2ΓΓ強弱順序’祕 丨米級驗生水生成模式、第二級鹼性水生成模式、第： 的狀Ιΐ生ΐΐί糾ί驗性水生成模式中，在打開上述電磁閥L 過控制電路19a的控制，使第二電極板12及第三電 和板3成為陰極板，使第一電極板u成為陽極板。 k 至？三級的驗性水生成模式中生成能夠飲用的驗性 + ί不，通常溶解氫量僅是UGppb以下級別的水，但若 採用根據本實施方式的整水器，在先生獻量含有溶解氫的pH值 15 200927665 在10以上，最好pH值為10.5以上的強鹼 最優化裝置使該髓性讀崎優化 "300ppb 雷極板1 卜1 中’在已關閉電磁閥42的狀態下，在任何 電極板1卜12、13上也不施加電壓，即，不進行電解此 ^關^電_ 42，無狀讀排出σ Μ翻。在酸性水生成模式 ΐ 莫式相反，通_制電路19a的控制，使 US 板13成為陽極板，使第-電極板11成 〇 晉，的特徵在於具備了飲用最優化裝 蕤Α-士2包方式中’作為飲用最優化裝置，做成如下結構： ，由即以61使生水旁通流道9從生水供給道4的中間部位分 電刺關62使該生水旁通鱗9的前端與取驗性水 、曾Q if m中，使流量按照大約4:丨的比例向生水旁通流 例如第一級驗性水(pH9.5 ) 拍二„電中，使電磁開關閥62處於打開狀態， 性;^二ϊΐ板11〜13施加的電壓提高至與操作強驗 時其以上後’制㈣流部61錢量節流至 ❹ 電解*先域ΡΗ^ 11程度且雜麟1500PPb 水，並通過湘相#於從生水旁通流道9供給的全 ittti的4/5的淨水對該強驗性水進行稀釋，能約供給既是 Lil的第一級驗性水又是含有九約300ppb之多的溶解氫的 佐沾^卜’在控制電路伽的記憶部内貯存有所選取之期望的PH ^=級鹼性水生成模式和與施加電壓的之預錄優化的圖 k /t 士、^制電路19& 一邊參照這種圖表，一邊按照第一級驗性 板式、第二級驗性水生成模式、第三_性水生成模式的 順序施加相對較高的電壓。理所當然，由於施加電壓越高驗性越 16 200927665 強，因此溶解氫量也增多。 此外，如圖2 (a)所示’也可以取消節流部61，藉由具有流 量調節功能的流道切換閥6使生水旁通流道9從生水供給道4分 支。 其次’使用圖6對飲用最優化裝置的第二實施例進行說明。 此外，作為整水器’除了飲用最優化裝置的構成以外與第一實施 例大致相同，僅說明不同點，省略其他說明。不同點在於，在先 前的實施例中’將從生水供給道4流入鹼性水生成室2 (第一電解 至15及第四電解室18)的流量和流入酸性水生成室3 (第二電解 ❹ 室16及第三電解室17)的流量設定成4 :卜但在此為2 : 1。 如圖所示，在此的飲用最優化裝置具備使生成於電解槽i内 的酸性水與生成於電解槽1内的強鹼性水合流的酸性水分支流道 趴。該酸性水分支流道81藉由具有流量調節功能的流道切換閥6 從排水流道8的中間部位分支，並與放出生成於電解槽丨的強驗 性水的取鹼性水流道7連通，其中，排水流道8為放出生成於電 解槽1的酸性水生成室3 (第二電解室16及第三電解室17)的酸 性水的取酸性水流道。 根據採用這種結構的飲用最優化裝置，在控制電路19a中， 將向第一至第三電極板11〜13的施加電壓提高至與操作強鹼性水 Ο 供給按紐時相同的級別，先生成例如在驗性水生成室2 (第一電解 室15及第四電解室18)的pH值為10.7〜11.0的程度，且溶解氫 為900〜1500ppb程度的強鹼性水，並能夠從酸性水分支流道81 使例如流入量被節流到1/3的生成於酸性水生成室3 (第二電解室 16及第二電解室π)的強酸性水與該強鹼性水僅合流必要量，從 ，降低驗度。為了製成能夠供於飲用的驗性水而需要的強酸性水 量，可以根據通過生水供給道4的生水的總流量並經實驗獲知。 即’可以獲知強驗性水和強酸性水的混合比例。從而，控制電路 19a根據生水的總水量能夠得到所需量的強酸性水地控制流道切 換閥6的閥開閉度。而且’不供混合的強酸性水從排水流道8排 17 200927665 出。 此外’生成於電解槽1内的酸性水中存在三鹵甲烧，該三鹵 甲烷具有由在淨水裝置5中未能除淨的生水中的結合氯或游離氯 引起的致癌性。於是，能夠在從電解槽丨的取酸性水流道（排水 流道f)至酸性水分支流道81之間配設具有除去上述三自甲烷功 能的二=曱烷除去功能部83。作為三鹵曱烷除去功能部83的具體 構成，旎夠應用使用了粉末狀、顆粒狀或纖維狀的活性炭的活性 炭處理裝置，或者是臭氧發生裝置等。 ❹ 在表1中表示了利用有關本實施例的飲用最優化裝置提取的 PH值及溶解氫量的測定結果。此外，表丨的大節流量和 2 ΐ區分是根據相對於從取水流道7 (噴嘴）提取的流量的 (流量比）的大小而大體劃分的。另外，劃分在大 ϋ給ίΪ、ϋ(2)和劃分在中節流量中的（5)、（6)使從生 内ί场性水生成室2(第—電駭15及細電解室18)The profit-seeking most-flight device is configured to have a pH 容纳 containing a pH adjuster in the aspirating water flow path 7 generated in the electrophoretic water, and is disposed in the branch flow path 71 at t, p„72 The branch branch 2 is branched from the middle portion of the flowable water channel 7 by the flow path cut_6 having the flow I regulating function and merges with the taken alkaline water flow path 7. (4) Structure, the money contribution contains dissolved hydrogen PH value is 10 or more. Ϊίΐί 'The pH adjuster is dissolved and mixed into the strong alkaline water, so that the pH can be less than 1G. That is to say, the hydrogen can be hydrogen on the side of the pH teacher G" The dissolution of the above-mentioned Eugene j 'as a positive regulator' can be filtered, such as citric acid, trisodium citrate and the like. Use; to make lemon food and other acidic foods. In short, as long as it is suitable for drinking jc and is enough to optimize the drinking of strong alkaline water. 5 to FIG. 7 is a more detailed configuration of the water refining 11 relating to the above embodiment. FIG. 5 is an internal junction including the water purifier relating to the first embodiment, and FIG. 6 is a second embodiment. [Overview of the internal structure of the water purifier of the example] Fig. 7 is a main constituent member of the internal knot including the water purifier according to the third embodiment, and ===7. In the same 11th as in Fig. 2 to Fig. 4, 200927665 -tSn!: The function part near the bottom of the electric 〇 is self-disposed to the same electrode plate of the case ,ίΓϊ, and the other side, the second electrode ' ΐΐ ί 极 = polarity of the opposite polarity of the plate 12 and the third electrode plate η. 11, 4 and 2, the plate 12 and the second electrode plate 13 are used as cathode plates, and are formed corresponding to the corresponding 'electro-electrolysis chamber 16 and the third electrolysis chamber n: oppositely, on the second electrode plate 12 and The three-electrode plate 13 is formed, the first electrode plate 11 serves as a cathode plate, the first electrolysis chamber i ^ ^ corresponds to the acidic water generating chamber 3, and the first electrolysis chamber 18 forms a water generating chamber 2_. The electrolysis to 16 and the second electrolysis chamber 17 and the annulus are provided with inlets and outlets for water on the respective electrolysis chambers 15, 16, 17, 18, and respective outlets of the first and third electrolysis chambers 15 and 18. The connected flow forms a water-storing flow path 7, which is sufficient from the sample to take the water; the pH of the alkaline water. On the other hand, the flow paths communicating with the respective outlets of the second electrolysis chamber 16 and the third electrolysis chamber port merge with each other to form the drainage flow path 8, so that the acidic water can be discharged by the electromagnetic valve 42 provided near the discharge port. As described above, if the polarities of the electrode plates 11, 12, and 13 are adjusted, it is a matter of course that acidic water can be extracted from the flow path as the alkaline water channel 7, and the alkaline water can be discharged from the drain flow path 8. Although the raw water supply path 4 is branched and connected to the inflow ports of the first electrolysis chamber 15, the second electrolysis chamber 16, the third electrolysis chamber 17, and the fourth electrolysis chamber 18, in the present embodiment, the raw water will be produced. The flow rate of the supply passage 4 flowing into the first electrolysis chamber 15 and the fourth electrolysis chamber 18 and the flow rate into the second electrolysis chamber 16 and the third electrolysis chamber 17 are set to 4: 12 200927665 • 1. Further, the branch upstream side of the raw water supply path 4 and the drain flow path 8 are connected by a check valve 41. The check valve 41 normally prevents the flow of water from the drain flow path 8 toward the raw water supply path 4, and in the case where water pressure is present when the water is passed, not only prevents the flow of water toward the raw water supply path 4 but also blocks The flow of water from the raw water supply passage 4 to the direction of the drainage flow. As shown in the figure, the electrolytic cell 1 receives the water supply from the water pipe 20 through the faucet 21, and the branch faucet 22 is disposed on the faucet 21, and one end of the water soft g 23 is connected to the branch pin 22, and the same The other end of the water supply hose 23 is connected to the inside of the IT/water purification filter cartridge 51. In addition, in the lower water purification filter, the cylinder 0 51 is mainly filled with activated carbon. The outflow port of the lower water purification cartridge 51 is connected to the inflow port of the upper water purification cartridge 52. ΐίΐΪΐ 52 is made of a metal mesh or cloth material, filter, paper, etc., and is also used as a hollow fiber membrane (membranethrcad) = bacteria can be removed to remove the device, so that the water pipe 2 () The raw water supplied, that is, the purified water, is purified by the water purifying device 5. The inflow σ of the water purification cartridge 52 connected to the flow sensor 535 is configured to measure the amount of water flowing, for example, a spiral music is provided in the flow sensor, and the spiral is rotated by the spiral lie. The flow rate σ of the flow rate ο 53 is connected to the inflow port of the water passage switching valve 54. Water, first, and second table 4 have two flow outlets for one inflow port. One flow outlet is added to the cylinder 55 by force ff, and the other is tender (four) is connected to the calcium through the water channel to add 丄 θ π ^ Ξ through the water channel. The switching causes the purified water to flow into any one of the salt adding cylinder 55 or the word adding cylinder 56. The acid 55 content is used to make the water strong in the electrolytic cell 1, and the column is filled with the calcium in the refreshing water 56 for the addition of calcium in the purified water, and the water channel connected to the outflow port of the salt adding cylinder 55 is connected and connected. The water channel on the person 1'=in& merges to form the raw water supply channel 4. In the figure, 57 is a check valve on the water channel between the set port and the other 艮 添加 adder cylinder 55 and the merging portion. Describe the month b. The cymbal 19 is provided with a control circuit 19a having various functions for controlling the water eliminator of the present embodiment, and is electrically connected to the flow sensor 53, the first electrode plate 11, the second electrode plate 12, and the third. On the electrode plate 13. The flow sensor 53 outputs the detected electric signal to the control circuit 19a, and the control circuit 19a calculates the water flow amount using the electric signal from the flow sensor 53. Since the first electrode plate 2 and the second electrode plate 12 are indirectly connected to the control circuit, the control circuit 19a is based on the control signal input through the panel operation of the user, on the electrode plates ^, 12, 13 Apply voltage. Further, the panel operation performed by the user refers to an operation of an operation panel (not shown) provided on the surface of the cabinet 10 of the water purifier, and such a panel is provided with, for example, a power button, ORP (High Oxidation Reduction Potential 〇 The xidati〇n reducti〇n potential) displays the basic water supply button, the clean water supply button, and the acid f at each level of the weak alkali to strong alkali according to the knowledge and water volume. Supply button, sanitary water (strongly acidic water) supply button, etc. In addition, a display unit such as a seven-segment LED that displays information such as pH value, ORP value, and water flow amount is provided, and the source button is a button for starting the water purifier, which is a button in any state. . In the case where the Hanbok is not stopped even if the power button is pressed, the door is shut down. 0, that is, the button that does not display the current water 0RP value on the above seven segments of LEDs is used to display the current water supply on the above seven segments. Produce a strong taste, boiled vegetables, such as the value of ΡΗ 为 例如 10 10 10 10 10 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够 能够It is button of the second-level examination of the 11th grade of the 11th. The third-stage alkaline water has a pH of, for example, 85 "generates a second-stage alkaline water, and a fire of 8.5" can be used as potable water, etc. The water water does not generate ionized water to make water from tap water. The water is mixed with the ground. The Lai Yuyu is used to refer to 200927665 as fr. New acid. (4) μ, and can be used to clean the silk handle light. The difference is only for the next clean water. The button on the sigh can be directly accumulated to the current pass, and the zero is pressed to zero. The zero return is valid on time. This prevents the error from being pressed::4 The button is replaced with the water purification cartridge 52 or '芮$ zero. The above-mentioned strong alkaline water # recognize; ^4# Chu & net filter 5% of the total use. Supply it ==== In addition to the button, the second level of water, in addition, in the operation panel has been set = degree ^ ^; ^ can = see the recognition. The lamp is used in the electrolytic cell i temperature rise "gue ^ plant degree rise refers not ❹ ❹ ❹ 按 按 按 按 按 按 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在 在The weak sequence 'secret meter level test water generation mode, the second level alkaline water generation mode, the first: the Ιΐ Ιΐ Ιΐ 纠 纠 纠 纠 纠 纠 纠 纠 纠 纠 纠 纠 纠 验 验 验 验 验 验 验 验 电磁 电磁 电磁 电磁 电磁 电磁 电磁 电磁 电磁 电磁 电磁 电磁The second electrode plate 12 and the third electric plate 3 are made into a cathode plate, and the first electrode plate u is an anode plate. k to? In the three-stage water-producing water generation mode, the potable testability is generated. The amount of dissolved hydrogen is usually only UGppb or less. However, if the water purifier according to the embodiment is used, the amount of dissolved hydrogen is contained in the Mr. The pH value of 15 200927665 is above 10, preferably the strong base optimization device with a pH value of 10.5 or higher makes the myeloid Nasaki optimization "300ppb lightning plate 1 Bu 1 'with the solenoid valve 42 closed No voltage is applied to any of the electrode plates 1 and 12, i.e., no electrolysis is performed, and no readout σ is turned over. In the acidic water generation mode, the control of the pass-through circuit 19a causes the US plate 13 to become an anode plate, and the first electrode plate 11 is formed into a spurt, which is characterized by having an optimal drinking device-study 2 In the package mode, as the drinking optimization device, the following structure is made: by the 61, the raw water bypass passage 9 is branched from the middle portion of the raw water supply passage 4 to make the raw water bypassing the scale 9 The front end of the water and the test water, the current Q if m, so that the flow rate to the raw water bypass flow, such as the first level of water (pH 9.5) in the ratio of about 4: 拍, in the electricity, so that the electromagnetic switch The valve 62 is in an open state, and the voltage applied by the two jaws 11 to 13 is increased to the extent that the operation is strong, and the above-mentioned (four) flow portion 61 is throttled to ❹ electrolysis * first domain ΡΗ ^ 11 degree and miscellaneous Lin 1500PPb water, and dilute the strong water by the Xiangshui # 4% pure water of the whole itti supplied from the raw water bypass passage 9, and can supply the first-grade water that is both Lil It is also a mixture of nine and about 300 ppb of dissolved hydrogen, which is selected from the memory of the control circuit. The water generation mode and the pre-recorded optimization of the applied voltage are shown in the figure k/t, the circuit 19& while referring to this chart, according to the first-level verification plate type, the second-stage inspection water generation mode, and the third _ Sexual water generation mode is applied in a relatively high voltage. Of course, the higher the applied voltage, the stronger the testability is, the higher the dissolved hydrogen is. Therefore, as shown in Figure 2 (a), the section can also be cancelled. The flow unit 61 branches the raw water bypass flow path 9 from the raw water supply path 4 by the flow path switching valve 6 having the flow rate adjustment function. Next, a second embodiment of the drinking optimization device will be described using FIG. In addition, the water purifier' is substantially the same as the first embodiment except for the configuration of the drinking water optimization device, and only the differences will be described, and the other description will be omitted. The difference is that in the previous embodiment, the water supply channel 4 will be supplied. The flow rate into the alkaline water generating chamber 2 (the first electrolysis to the 15th and the fourth electrolysis chamber 18) and the flow rate into the acidic water generating chamber 3 (the second electrolysis chamber 16 and the third electrolysis chamber 17) are set to 4: But here is 2: 1. As shown in the figure. Here, the drinking optimization device includes an acidic water branching channel that causes the acidic water generated in the electrolytic cell i to merge with the strongly alkaline water generated in the electrolytic cell 1. The acidic water branching channel 81 has a flow rate. The flow path switching valve 6 of the regulating function branches from the intermediate portion of the drain flow path 8 and communicates with the alkaline water flow path 7 that discharges the potent water generated in the electrolytic cell, wherein the drainage flow path 8 is generated by the discharge flow path 8 The acidic water flow path of the acidic water in the acidic water generating chamber 3 (the second electrolytic chamber 16 and the third electrolytic chamber 17) of the electrolytic cell 1. According to the drinking optimization device having such a configuration, in the control circuit 19a, the direction is The applied voltages of the first to third electrode plates 11 to 13 are increased to the same level as when the strong alkaline water is supplied to the button, for example, in the pseudo water generating chamber 2 (the first electrolysis chamber 15 and the fourth electrolysis) The chamber 18) has a pH of 10.7 to 11.0 and a strong alkaline water having a dissolved hydrogen of about 900 to 1500 ppb, and can be throttled from the acidic water branching passage 81 so that, for example, the inflow amount is throttled to 1/3. Water generation chamber 3 (second electrolysis chamber 16 and second electrolysis) [pi]) of the strongly acidic water and strongly alkaline water merging only a necessary amount from the test of the reduction. The amount of strongly acidic water required to produce the water for quenching can be determined based on the total flow rate of raw water passing through the raw water supply passage 4 and experimentally. That is, the mixing ratio of the potent water and the strongly acidic water can be known. Therefore, the control circuit 19a can control the valve opening and closing degree of the flow path switching valve 6 by obtaining the required amount of strongly acidic water based on the total amount of raw water. Moreover, the strong acidic water that is not mixed is discharged from the drainage channel 8 17 200927665. Further, in the acidic water formed in the electrolytic cell 1, there is a trihalomethane which has carcinogenicity caused by bound chlorine or free chlorine in raw water which has not been removed in the water purifying device 5. Then, a di-decane removal function portion 83 having the function of removing the above-mentioned three-methane can be disposed between the acidic water channel (drain channel f) from the electrolytic cell 至 and the acidic water branch channel 81. As a specific configuration of the trihalodecane removal function unit 83, an activated carbon treatment apparatus using activated carbon in the form of powder, granules or fibers, or an ozone generator or the like is used. ❹ The measurement results of the pH value and the dissolved hydrogen amount extracted by the drinking optimization device according to the present embodiment are shown in Table 1. Further, the large-section flow rate and the 2 ΐ discrimination of the surface are roughly divided according to the magnitude of the flow rate (flow ratio) with respect to the flow rate extracted from the water intake runner 7 (nozzle). In addition, it is divided into (5) and (6) which are divided into ϋ, ϋ (2) and divided into the middle flow, so that the field water generating chamber 2 (the first electric 骇 15 and the fine electrolysis chamber 18) )
1818
200927665 表1 ml/ 煺 憲 _ 躪 駐 m e 五 s m 关 s 基 m m 运 屋 < h <Π m 溶解氫 1 CL 660. 000 564. 〇〇〇 457.000 398. 000 710. 000 565. 000 469. 000 400.000 趙裁串 1& 2. 600 2. 670 2.690 2.740 2.620 2.610 , 2.710 2.700 9. 570 9. 580 9.680 9.160 9.780 9.570 9.470 9. 350 | #1S苎柳 S 1.688 2.055 2.252 g g CO 2. 051 2.246 关窜S 坦 Κ·3Φ 趙哥哉插 (升/分） 1_ 0. 921 V015 1.038 1.123 0.875 0.982 1.016 CO _ 胜®es^_：H 5； 1 寸 s 2.014 1.439 1.789 !n σ> 電齧驟口 =& j 2.600 2.670 2.690 2. 740 2. 620 Π 2. 610 2.710 2.700 I (升/分) 〇 CM T— in (O to CM 0. 965 s 1.283 電解槽出口鹼性水 1 10. 800 I_ \ 10. 700 10. 600 10. 400 10.850 I 10.650 10. 600 10. 400 溶解氫 1_ 1102. 402 898.186 679.394 574. 732 1157.264 878.109 697. 649 578. 096 S (升/分） 1_ η 1.713 2.133 2. 529 〇> CO CO 1 1.772 2. 084 2.511 胜駟£辉 2.374 2.825 3. 290 3.785 2.354 I 2. 875 3. 249 3.794 流量比 j 29. 051 i_ I I 28.124 26. 647 27. 459 25.156 1 22. 760 20. 805 21.994 S (升/分） 0.079 0. 097 0.119 0.133 0. 090 1 0.121 0.149 0.165 噴嘴 (升/分） 2. 295 I_ 2. 728 3.171 3.652 2.264 I 2. 754 3.100 3.629 總流量 (升/分） 2. 374 2. 825 3. 290 3.785 I 2. 354 2. 875 3.249 3. 794 s s g w 5 g Sfe剩丑· 19 200927665 9·16-9·78 ^ 氫。 又3有超過充分量的398〜710PPb的溶解 成室2的流量場ϋ於流入驗性水生 2 1374 (^}' 〇 2^izzti^ (^(ίί/)3從^的酸性水中_升/分）量。 提取的2295 = 排出。這樣，對於從取驗性水流道7 SS1 (^} ^ ' 660ppb 成於^水從表1的排水實測值也可知，雖然生 L t ί、" 比例或向各電極板11〜13的施加電壓的 成在雜水生成室3的全部雜水用作 〇 零，從而=顯=效r來自排水流道8的排水量為 此外其7對飲用最優化裝置的第三實施例進行說明。 你丨由於除了飲騎優化裝置的結構以外與第-化裝署二二因此在此省略說明。如圖所示’該例子的飲用、最優 水流道7内具備容納檸檬酸等的PH調節劑的 的PH 1°L丨ίτί ’並在分支流道71内設有作為ΡΗ調節部72 的ρΗ 5周即劑添加缚73，該分支流道71藉由具有流 = ===#_性水_ 7財卿位 20 200927665 即便採用這樣的結構，在驗性水生成室2 (第一電解室】 第四電解至18)中，在先生成大量含有溶解氣的阳值在1〇以上 =強=性水彳H過齡歧切綱6碰駭量賴強驗性水 流^分支流道71内並通過ρΗ調節劑添加筒73，使檸檬酸等的 調_溶解並混合放入到該強鹼性水中，而降低鹼度。而且，降 低了鹼度的鹼性水和從鹼性水生成室2直接流出至取鹼性水流道 7内的強驗性水合流而兩者混合，從而能狗提取飲用最 值不到10的鹼性水。 iprt f該實施例的整水器中，在控制電路19a的記憶部貯存有預 〇 ，對，終的ph值、生水量、應流人分支流道71 量的關係進 行了最優化的圖表，從而在控制電路19a巾，可以一邊參照該圖 表一邊進行利用流道切換閥6的流量調節。 但是，在本實施方式的各級別的驗性水生成模式中，即便是 為了先生成強驗性水而有施加電壓，也使其電壓的大小不同，按 ，，驗性賴式、第—㈣性水生祕式、第二級驗性水生 成模式、第三級鹼性水生成模式的順序施加相對高的電壓。可是， 在各模式都為相同大小的施加電壓的情況下，也可以在先生成相 同級別的，鹼性水後，使用飲用最優化裝置適當地調節與強鹼性 水混合的淨水量、酸性水量、pH調節劑的添加量等而得到規定的 v pH 值》 、，外，士申請發明通過在先生成pH值在1〇以上的強鹼性水 後進行飲用最優化而能夠得到含有超過3〇〇ppb的溶解氫且pH值 不到10的鹼性水，若能夠實現這些，則能夠適當地設定從生水供 給道4向鹼性水生成室2和酸性水生成室3分配的流量的比例， 或者鹼性水生成室2和酸性水生成室3的容積，或者向各電極板 11〜13的施加電壓的大小等具體數值的組合。 21 200927665 【圖式簡單說明】 圖1是表示溶解氫濃度和pH值之間的關係的曲線圖； 圖2 U)、（b)是表示整水器的飲用最優化裝置的一個例子的模式 說明圖； 圖3是表示整水器的飲用最優化裝置的一個例子的模式說明圖· 表示整水_飲躲優化裝置的-個例子的模式說明圖:， 圖5疋表示飲用最優化裝置的第一實施例的說明圖； 圖6是表示飲用最優化裝置的第二實施例的說明圖； 圖7是表示飲用最優化裝置的第三實施例的說明圖。 【主要元件符號說明】 〇 1 電解槽 2 鹼性水生成室 3 酸性水生成室 4 生水供給道 5 淨水裝置 6 流道切換閥 7 取鹼性水流道 8 排水流道 9 生水旁通流道 10 箱體 11 第一電極板 12 第二電極板 13 第三電極板 14 隔開壁 15 第一電節室 16 第二電節室 17 第三電節室 18 第四電節室 22 200927665200927665 Table 1 ml/ 煺宪 _ 躏 in me five sm off s base mm transport house < h < Π m dissolved hydrogen 1 CL 660. 000 564. 〇〇〇457.000 398. 000 710. 000 565. 000 469. 000 400.000 赵裁串1& 2. 600 2. 670 2.690 2.740 2.620 2.610 , 2.710 2.700 9. 570 9. 580 9.680 9.160 9.780 9.570 9.470 9.350 | #1S苎柳 S 1.688 2.055 2.252 gg CO 2. 051 2.246 Off窜S 坦Κ·3Φ Zhao Ge 哉 (L/min) 1_ 0. 921 V015 1.038 1.123 0.875 0.982 1.016 CO _ 胜®es^_:H 5; 1 inch s 2.014 1.439 1.789 !n σ> Electric bite mouth =& ; j 2.600 2.670 2.690 2. 740 2. 620 Π 2. 610 2.710 2.700 I (L/min) 〇CM T— in (O to CM 0. 965 s 1.283 Electrolytic tank outlet alkaline water 1 10. 800 I_ \ 10 700 10. 600 10. 400 10.850 I 10.650 10. 600 10. 400 Dissolved hydrogen 1_ 1102. 402 898.186 679.394 574. 732 1157.264 878.109 697. 649 578. 096 S (liters per minute) 1_ η 1.713 2.133 2. 529 〇 > CO CO 1 1.772 2. 084 2.511 Victory £2.374 2.825 3. 290 3.785 2.354 I 2. 875 3. 249 3.794 Flow ratio j 29. 051 i_ II 28.124 26. 6 47 27. 459 25.156 1 22. 760 20. 805 21.994 S (L/min) 0.079 0. 097 0.119 0.133 0. 090 1 0.121 0.149 0.165 Nozzle (L/min) 2. 295 I_ 2. 728 3.171 3.652 2.264 I 2 754 3.100 3.629 Total flow (liters per minute) 2. 374 2. 825 3. 290 3.785 I 2. 354 2. 875 3.249 3. 794 ssgw 5 g Sfe ugly · 19 200927665 9·16-9·78 ^ Hydrogen . 3 more than a sufficient amount of 398 ~ 710PPb dissolved into the chamber 2 flow field 流入 inflow into the experimental aquatic 2 1374 (^}' 〇 2 ^ izzti ^ (^ (ίί /) 3 from ^ acidic water _ liter / The amount of extraction 2295 = discharge. Thus, for the measured value of the drainage from Table 1 from the water flow of the SS 7 (1) ^ ' 660 ppb from the water flow channel, although the L t ί, " ratio Or the application of a voltage to each of the electrode plates 11 to 13 is used as the enthalpy of all the water in the waste water generating chamber 3, so that the amount of water discharged from the drain channel 8 is in addition to the seven pairs of drinking optimization devices. The third embodiment will be described. In addition to the structure of the drinking and riding optimization device, the description will be omitted here. As shown in the figure, the drinking and optimal water flow path 7 of the example is accommodated. PH 1°L丨ίτί ' of the pH adjuster such as citric acid is provided in the branch flow path 71 as a 添加5-week agent addition 73 as the ΡΗ adjusting portion 72, the branch flow path 71 having a flow = ===#_性水_ 7财庆位20 200927665 Even with such a structure, in the water-producing chamber 2 (first electrolysis chamber) In 18), the positive value of a large amount of dissolved gas in Mr. is above 1〇=strong=sexual water 彳H overage 歧6 骇 赖 赖 强 强 强 强 强 强 强 强 强 强 强 强 Η Η Η Η Η Η Η Η Η Η Η Η Η Η The addition tank 73 is prepared by dissolving and mixing citric acid or the like into the strong alkaline water to lower the alkalinity. Further, the alkaline water having a reduced alkalinity flows directly from the alkaline water generating chamber 2 to The strong hydration flow in the alkaline water flow channel 7 is taken and the two are mixed, so that the dog can extract the alkaline water having a maximum value of less than 10. iprt f The memory of the control circuit 19a in the water purifier of this embodiment The department stores the pre-existing data, and optimizes the relationship between the final ph value, the raw water amount, and the flow-receiving branch flow path 71. Thus, the control circuit 19a can use the flow path while referring to the chart. The flow rate of the switching valve 6 is adjusted. However, in the water-producing water generation mode of each level of the present embodiment, even if a voltage is applied for the purpose of making a strong water, the magnitude of the voltage is different, and the test is performed. Sexual Lai, the first (four) aquatic secret, the second level of water production The order of the third-stage alkaline water generation mode is relatively high. However, in the case where each mode is the same magnitude of applied voltage, it can also be used after drinking the same level of alkaline water. The optimization device appropriately adjusts the amount of purified water mixed with the strong alkaline water, the amount of acidic water, the amount of the pH adjuster, etc. to obtain a predetermined pH value, and the application of the invention is at a pH of 1〇. After the above-mentioned strong alkaline water is optimized for drinking, alkaline water containing more than 3 ppb of dissolved hydrogen and having a pH of less than 10 can be obtained. If this is achieved, the raw water supply channel 4 can be appropriately set. The ratio of the flow rate to the alkaline water generating chamber 2 and the acidic water generating chamber 3, or the volume of the alkaline water generating chamber 2 and the acidic water generating chamber 3, or the magnitude of the applied voltage to each of the electrode plates 11 to 13 A combination of values. 21 200927665 [Simple description of the drawing] Fig. 1 is a graph showing the relationship between dissolved hydrogen concentration and pH value; Fig. 2 U) and (b) are mode descriptions showing an example of the drinking water optimization device of the water purifier Fig. 3 is a schematic explanatory view showing an example of a drinking water optimization device of a water purifier. Fig. 5 is a schematic explanatory view showing an example of a water purification_drinking optimization device: Fig. 5A shows a drinking optimization device. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 6 is an explanatory view showing a second embodiment of the drinking optimization device. Fig. 7 is an explanatory view showing a third embodiment of the drinking optimization device. [Description of main components] 〇1 Electrolyzer 2 Alkaline water generation chamber 3 Acid water generation chamber 4 Raw water supply channel 5 Water purification device 6 Flow path switching valve 7 Alkaline water flow path 8 Drainage flow path 9 Raw water bypass Flow path 10 Case 11 First electrode plate 12 Second electrode plate 13 Third electrode plate 14 Partition wall 15 First electric junction chamber 16 Second electric junction chamber 17 Third electric junction chamber 18 Fourth electric chamber 22 200927665
19 功能部 19a 控制電路 20 水管 21 水龍頭 22 分支栓 23 給水軟管 41 ' 57 止回閥 42 電磁閥 51 下淨水濾筒 52 上淨水濾筒 53 流量感測器 54 水道切換閥 55 食鹽添加筒 56 崔弓添加筒 61 節流部 62 電磁開關閥 63 排出口 71 分支流道 72 pH調節部 73 pH調節劑添加筒 81 酸性水分支流道 83 功能部 2319 Function part 19a Control circuit 20 Water pipe 21 Water tap 22 Branch pin 23 Water supply hose 41 ' 57 Check valve 42 Solenoid valve 51 Lower water filter cartridge 52 Upper water filter cartridge 53 Flow sensor 54 Waterway switching valve 55 Salt addition Cylinder 56 Cui bow adding cylinder 61 Throttle portion 62 Electromagnetic opening and closing valve 63 Discharge port 71 Branching flow path 72 pH adjusting portion 73 pH adjusting agent adding cylinder 81 Acid water branching flow passage 83 Function portion 23