201238911 、發明說明： 【發明所屬之技術領域】 本發明係關於一種能將原水經電氣分解以生成鹼性離 子水及酸性離子水的電解水生成裝置，其特別是關於一種 使得可用來飲用之驗性離子水之pH値不會過度上昇，並可 獲得高溶氫量(Dissolved Hydrogen)之電解水的電解水生成 裝置。 【先前技術】 近年來隨著對於安全的水及健康的關注越來越多，可 將自來水等原水於電解槽内進行電氣分解以生成鹼性離子 水與酸性離子水的電解水生成裝置亦廣泛地普及至一般家 庭中。此種電解水生成裝置之結構係自吐水通路吐出^性 離子水與紐離子水之-者以供使用，並自排水通路排出 另一者’特^是可提供對健康有益的驗性離子水以供飲用。 冲^1，最近有研究報告指出高溶氫量的制水有預防或 =如帕金森氏症或代謝性症候群 (ifestyle-related Diseases)等的效果。因此 一 氫量鹼性離子水的電解水生成裝 b 、/、同溶 氫量係依靠f解槽的魏強度。X 增加。然而’溶 量的驗性離子水，由於會使pH值變’，製=溶氫 之適於飲用的條件，則必須^為滿足阳值小於 因此，提高溶氫量變得較為困難。麵強度至一定程度。 此處，已知一種整水器，复星 極的電解槽，對流人該電解槽向配置有陽極與陰 出酸性水與鹼性水(例如，參‘專利7文:了)電氣分解後可取 4/22 201238911 電解槽 、此專利文獻1所揭露之整水器，其為了讓電解槽所生 成之pH值10以上的強驗性水能最適於飲用，係具備有流 道=換閥，以將原水以狀之比财配至原水旁通流路及 [先前技術文献] [專利文獻1]曰本專利特開第2〇〇9_16〇5〇3號公報 【發明内容】 然而，上述先前技術的結構，係在電解槽外部設置流 道切換閥，經由該流道切換閥，以特定之比例將原水分配 至原水旁通流路及f解槽。為此，需魏外職道切換闕， 而造成初期設置成本高，且有電解水生成系統大型化的問 題。此外，電解槽與流道切換閥之間需以配管連接，於該201238911, the invention relates to: [Technical Field] The present invention relates to an electrolyzed water generating device capable of electrically decomposing raw water to generate alkaline ionized water and acidic ionized water, and more particularly to a test which makes it usable for drinking The pH of the ionized water does not rise excessively, and an electrolyzed water generating device of electrolyzed water having a high dissolved hydrogen amount (Dissolved Hydrogen) can be obtained. [Prior Art] In recent years, with the increasing attention to safe water and health, electrolyzed water generating devices that can electrically decompose raw water such as tap water in an electrolytic cell to generate alkaline ionized water and acidic ionized water are also widely used. The land is popularized in the general family. The structure of the electrolyzed water generating device is such that it is used for spitting out the ionized water and the neon ion water from the spit water passage, and is discharged from the drain passage, and the other is to provide the test ion water which is beneficial to health. For drinking. Chong ^1, a recent research report indicates that high-hydrogen-dissolved water has preventive effects such as Parkinson's disease or ifestyle-related diseases. Therefore, the amount of hydrogen produced by the electrolyzed water of a hydrogen-containing alkaline ionized water is dependent on the Wei strength of the unsinking tank. X increases. However, it is difficult to increase the amount of hydrogen dissolved in the case where the amount of the ionized water of the solution is changed to pH, and the condition for making the hydrogen soluble is suitable for drinking. The surface strength is to a certain extent. Here, there is known a water purifier, a complex star electrolysis cell, which is convectively configured to have an anode and an acidic water and an alkaline water (for example, the reference patent) 4/22 201238911 Electrolyzer, the water separator disclosed in Patent Document 1, which has a flow path = valve replacement in order to make the potent water having a pH value of 10 or more generated by the electrolytic cell most suitable for drinking In the prior art, the above-mentioned prior art is used. The structure is such that a flow path switching valve is provided outside the electrolytic cell, and the raw water is distributed to the raw water bypass flow path and the f solution groove by a specific ratio through the flow path switching valve. For this reason, it is necessary to switch the external service route, which results in a high initial installation cost and a problem of large-scale electrolysis water generation system. In addition, a pipe connection is required between the electrolytic cell and the flow path switching valve.
配管連接部’可能會有從Q型環及封裝部漏水之風險增^ 的情況。 S 本發明係為了解決此一習知問題，目的為提供一種具 單純的結構及低價的配置，吐水之pH値不會過度上昇，可 製出南溶鼠罝之驗性離子水的電解水生成裝置。 為解決前述的問題，本發明係一種電解水生成裝置， 其特徵係具有：由具備陰極之陰極室與具備陽極之陽極室 所構成而能將通入之原水經電氣分解以生成鹼性離子水及 酸性離子水的電解槽、以及控制前述電解槽之電解強度的 控制部；並具備：連接至前述陰極室而可吐出前述陰極室 所生成之前述鹼性離子水的吐水通路、以及連接至前述陽 極室而可排出前述陽極室所生成之前述酸性離子水的排水 通路’其中，前述電解槽内具備有匯流部，讓前述陽極所 生成之前述酸性離子水之一部份匯流至前述陰極所生成之 5/22 201238911 刚述驗性離子水。 、又，前述匯流部較佳係構成為設置於前述電解槽内之 下游側（即，前述排水通路側）。 又’前述匯流部較佳係構成為具備有可調整流量的開 閉閥。 又’前述匯流部較佳係構成為具備有能去除前述酸性 離子水中之殘留氯的除去手段。 又’較佳係構成為至少於前述排水通路設置有可調整 流量的前述開閉閥 [發明的效果] 於本發明中，藉由將匯流部設置於電解槽内部，讓陽 極所生成之酸性離子水之一部份匯流至陰極所生成之鹼性 離子水’以單純的結構及低價的配置’使吐水之pH値不會 過度上昇，可生成高溶氫量的鹼性離子水。 【實施方式】 以下，參照圖式，依序詳細地說明本電解水生成裝置 之實施形態(實施例1)、（實施例2)。 (實施例1) 圖1係本電解水生成裝置之實施例1的結構示意圖。 如圖1所示，自來水等的原水管道I係經由水龍頭2 連接至本體部3的淨水部4。淨水部4具備有能吸附内部原 水中之殘留氣、三鹵曱烷、霉味等的活性炭以及準確地清 除一般細菌或雜質的中空纖維薄膜等。經淨水部4過濾後 的水係自導入通道5 a流炱流量檢測部6。流量檢測部6確 認有通水便會指示控制部25進行控制。淨水部4處所過濾 的水通過流量檢測部ό而分流至導入通道5b、5c。導入通 6/22 201238911 Ί"!置有妈供給部用節流器7與妈供給部8。詞供給部 么# 1器7叮°周整流通於導入通道5c的流量。每供給部8 係將，油魏K乳酸解_子加人原水巾以提高原水 之電氣傳導度。導人通道&會匯流至導人通道％。導入通 、、之下游奋經由導入通道5d而連通至第1電極室用導 2通道9 ’再連通至電解槽12之第i電極室仏内。又， =通道5d分岐形成有第2電極室用導入通道10。第2電 極至用導人通道1G係經由可調整流通於第2電極室用導入 f2b2:極室用節流器11 ’ *連通至電解槽 酸性I:: 12:將過濾水經電氣分解以生成鹼性離子水及 部形財藉由隔膜❿、说而分隔之第 Μ — 與第2電極室⑽。第1電極室l2a内，第！ 私極室用電極板14a、14b呈對向配置 配置有第2電極室用電極板15。 电内 第2電極室12b内之下游側設置有具雜軒水導 月“匯流部16。匯流部16緊鄰地配置 之下游側。匯流部16之功能係趑笙至12a内 之離子她2 4電極室12b内所生成 二子W弟2電極至用電極板15為陽 子水)之一部份導入第1電極室12a肉u生離 連接有將第2電極宮u 匯流部16之下游則 枚^ 電才 孔之水（第2電極室用電極板15 A陷 極之情況係指酸性離子水)排出的排水通路收、晰^ ^通路18a、18b之途中介設有限制 於排 流量的排水通路用節流器19。 、於排水通路l8a之 再者，一併說明排水通路18a、18b 排水通路18。 馆 使统％為 7/22 201238911 ㈣之:：f有吐一，路 為陰極之情況係指驗性離 電極至用電極板14a及Mb 路17之上游處分岐而連接飲用水而吐出。吐水通 路係經由限制流量之吐水吐水旁通流 至㈣部22。阳感·而連接 出至吐水旁通流路20内的=第】電極室⑽ 吐水旁通流路20之下游會匯離^水的阳值進行檢測。 控制部25係由本體述排水通路⑽。 的電解的能量供給至電解作控制用或將電氣分解用 Μ為電源插頭，㈣斤構成。圖中符號 轉換成直流電源的電源部。符電23之交流電源 子水或酸性離子水、淨水 :'τ'讓使用者針對驗性離 擇設定的操作顯示部。 貝或ρΗ值等各種機能進行選 圖3係匯流部16及笛7 α 詳細圖。 t極室12b^分之#施例1的 圖3中’匯流部1 $今番女 用節流器28係在將第2相節流器28。匯流部 電極室用電街i2b所生成之離子水(第2 電極室子水)導入第> 產生施例1的電解水生成裝置，說明 及所期望之水淨水模式等、以 _ 、式興pH值，並開啟水龍頭2 鱼;^、s 7 。從水龍頭2導人之原水係藉由淨水部4將原水中的^ 8/22 201238911 留氯或三鹵曱烷、霉味、一般細菌等雜質去除，經導入通 道5a並通過流量檢測部6。然後，原水之—部份會分岐至 導入通道5c側，並藉由鈣供給部用節流器7而限&於適量 流量。接著，於妈供給部8處溶入甘油磷酸舞或乳酸妈等 以處理成較易進行電氣分解之水，然後，再次與導入通道 5b匯流。匯流後之原水係經由第丨電極室用導^通道=及 第2電極室用導入通道10(各自為電解槽12内之第】電極 室12a及第2電極室12b料用而設置)而導入至各自之電 極室。此處’第2電極室用節流器n係為了調整第i電極 室12a及第2電極室12b之内壓平衡而設置著。即， 於流經第1電極室12a ώ σ側與第2電極室⑶出口側 流量比’可藉由改變流經第i電極室用導入通道9㈣ 電極室用導入通道10的流量比來加以調整。本實施例！ ^ ，先調整成〔（第i電極室12a之出口側流i t%1? 2 口側流量)〉(第1電極室用導入通道9之流 里丨=2電極室用導入通道1〇之流量）〕。此處，第 極至12b之内覆較第^電極室12a之内壓更 電極室12b之7k合亡、*人杜 °幵/成讓第2 0有、*向第1電極室12a之傾向的狀能。 邶w力 從電源插頭23供給AC100V，以產生^ 之=器及控制用直流電源進行電氣分解所= Ϊ ^之第3_25將電氣分解所需能量供給至= 15 μ電極至料極板I Mb及第2電極室用雷 極板15。此時，施加有相對為 至用電 加有負電壓之電極視作陰極，於電解槽〗^ …咮所分隔之陽極室 由隔 水生成模式時，第丨 冉者奴性離子 第電極至用電極板Ha及14b為陰極， 9/22 201238911 第2電極室用電極板15則為陽極。 接著’開始通水後，控制部25會讀取來自流量檢測部 6之輸出喊，當單位時間内流通之流量等級㈣)超過一 定量時，便判斷此狀態為通水中。此時，根據已選擇好之 水質模式及p Η值等的電氣分解條件，控制部2 5係對電解 槽12—供給狀之電解能量。驗性離子水生成模式時，第】 電極室β用電極板14a及14b為陰極，帛2電極室用電極板 為陽極此時，吐水通路i7會吐出驗性離子水且排水通 =、1二會排出酸性離子水。又，此時，藉由第2電極室用 即抓态11來調整成第2電極室12b之内壓使較第丨電極室 仏之内壓更高。讓第2電極冑⑶所生成之酸性離子水之 -部份，過匯流部16所設置之匯流部用節流器28，使與第 1電極室12a所生成之鹼性離子水匯流，藉以抑制驗性離 水之pH值。 再者，只要能滿足此關係式〔（第i電極室12a之出口 側流虿)/(第2電極t 12b之出口侧流量）>(第！電極室用 導入通道9之流量)/(第2電極室用導入通道1〇之流量）〕 的結構時，可自由改變第2電極室用節流器u之位置或個 ^例如’可叹置在第i電極室用導入通道9或吐水通路 7、排水通路18a或i8b之途中’亦可設置於複數個位置 〇 又，匯流部16可設置在電解槽12内之水流上游側， =可設置於下游侧。再者，為了更進一步地抑制第！電極 =12a所生成之鹼性離子水的pH值，將其設置在第2電極 室、12b内酸性最高之電解槽12内下游側者較為有效。又， 匯流部用節流器28之位置可於匯流部16之上部，亦可於 10/22 201238911 側面部。 如此，藉由匯流部用節流器28而 性離子水餘吐水祕17以鮮=抑制之驗 Λβ,/ν. . ,, ^ 乂仏1人用。鹼性離子水之一 礼仏岐至吐水旁通流路2〇，藉由吐 器2i限制於適量流量，導 方通机路用即"比 測定。此處，刪25 t22錢行PH值 轳、“韻夺，于貝取來自PH感測部22之輸出訊 破，逐次電解的能量，以達到操 之PH值般地進行控制。铁後 丨仏所。又疋好 .…、後通過PH感測部22之鹼性 離子水在與排水通路18b匯流後，_ 此時，為了使其能飲用且盡 排出 0^ - ^ υΐΛ 也了此乓加鹼性離子水中的 盡以上之範圍内’應調整電解的能量以 ί ιΓ上值者為佳。此時’匯流部16位在電解 可將酸性度較高之酸性離子水匯流至 电和至12a所生成的驗性離子水。接著 後之驗性離子水的pH值不變，便; 其結果，於第1電極室12a處之氣氣產生 成溶氫量較多之鹼性離子水。 夏《 «加了生 然後，當單位時間内流通之— 便判斷此狀態為止水，停业朝雪_寻級低於一疋置時， 士上 朝電解槽】2供給電解的銥呈。 此時，在止水後之-定時間内，對第 1 及14b施加相對之正電壓 电至用電極板… 負電壓。|έ此，可將咐荃、包極室用電極板15施加 貝电毖糟此了將附者於第丨 的每等的水垢洗淨去除。 i用板14a及14b 如以上般’依據本實施例1， 12内，藉由匯流部16讓由 生成^ ^納於電解槽 份匯流至由陰極所生成之㈣之=離子水之-部 因双Γ生離子水。因此’無需如習知 Π/22 201238911 技術般於電㈣外㈣t道連減道切㈣，可降 本。再者，亦可降低從配管之連接部分處之〇型環或封 部漏水等的驗。其結果，具單純結構及倾配置二 易達到電解水生成系統之小型化。 令 又，由於匯流部16係配置在電解槽12内之下游側（即， 排水通路18a側），可讓酸性度較高之酸性離子水匯流至由 陰極所生狀祕離子水。且，可-邊輕操物示部％ 所顯示之pH值，一邊藉由pH感測部22來調整飲用之浐 性離子水的pH值。其結果，吐水之？^1值不會過度上昇^ 並可有效率地生成溶氫量較多的驗性離子水。 再者，作為匯流部16之一範例，亦可將分隔第2電極 室12b之隔膜i3a、13b之一部份設置穿透孔，並藉由匯流 部用節流器28來調整穿透孔之大小的結構。 机 (實施例2) 本實施例2中，針對與實施例丨具相同結構及作用効 果者係賦予和實施例丨相同之符號，關於其詳細說明請援 用實施例1之說明。 本貫施例2與實施例1之相異部分在於，電解槽I]内 f匯流部16設置有可調整流量之開閉閥與殘留氯除去手 段，且至少於酸性離子水排水通路處設置有可調整流量之 開閉閥。以上述差異點為基礎，使用圖2以及圖4來說明 本實施例2之電解水生成裝置的動作。 圖2係實施例2之電解水朱成裝置的結構示意圖。 圖2中，於排水通路18a之途中具備有開閉閥27，其 可根據來自控制部25之命令，自由調整流通於排水通路18a 之流1。符號33係將來自控制部之控制訊號輸入至開 12/22 201238911 閉閥27的訊號線。 圖4係匯流部16以及第2電極室12b部份之實施例2 的詳細圖。 圖4中，由内筒30a與外筒30b所組成的開閉閥3〇來 構成匯流部16。内筒30a配置於第2電極室12b的正後方。 内筒30a内部收納有殘留氣除去手段29。該殘留氣除去手 & 29係用以將從第2電極室12b(圖2)經匯流部16而導入 第1電極室12a(圖2)的水中之殘留氣或三鹵曱烷等去除。 内筒30a收納於外筒30b内。内筒30a設置有流量調整用 孔31a，外筒30b設置有流量調整用孔31b。内筒3〇a連接 有步進馬達32，其可根據來自控制部25之命令，迴轉•停 止於任意位置。圖2中之符號34係將來自控制部25之^ 制訊號輸入至步進馬達32的訊號線。 工 圖2中，使用者係操控該操作顯示部26之特定按鍵， 藉以選擇驗性離子水生成模式、酸性離子水生成模式或淨 水模式等所期望之水質模式與pH值，並開啟水龍頭2以進 行通水。從水龍頭2導入之原水係藉由淨水部4將原水中 • ㈣留氣或三鹵曱m -般細g轉質去除，且經 - 2=入通道5a並通過流量檢測部ό。然後，原水之一部份 曰刀岐至導入通道5c側，並藉由鈣供給部用節流器7限制 於適量流量，於触給部8處溶入甘油填酸贼乳酸句等 以處理成較易進行電氣分解之水。然後，再次與導入通道 5b匯流。匯流後之原水係經由第丨電極室用導入通道9及 =2电極室用導入通道1〇(各自為電解槽内之第1電極 至^2a及第2電極室12b的專用而設置）而導入至各自之電 極至。此處，第2電極室用節流器^係為了調整第i電極 13/22 201238911 至12a及第2電極室12b之内壓平衡而設置。接 於流經第1電極室12a * 口側與第2電極室12b出口，對 流，，由改變流經第1電極室用導入通道9與第= 極=用V入通道1〇的流量比來加以調整。本施例已 =調整成〔（第i電極室12a之出口側流量= 至2b之出口側流量）〉（第】電極室用導入通道· =第2電極室料-通道1。之流量)〕。此處，第二二) 2b之内壓較第i電極室仏之内壓更高 ^ 極室12b之水會有流向第】電極室i2a之傾向的電 另方面，從電源插頭23供給Aci〇〇v，以 =24内之魏n及控直流電源進行電氣分的= 罝。接著，經由控制部25脾八切 而的月匕 解样12d m _需的能量供給至電 電極板心⑽及第2電極室用 二2 S3之h電極視作陰，’便會於電解槽12内形成由 、 所分隔之陽極室與陰極室。再者，驗性離 = ;第1電極室用電極板A及Mb為陰極， 第2電極至用電極板15則為陽極。 6 :!始通倾’控制部25會讀取來自流量檢測部 兩出减’當早位時間内流通之流量等級超過 時^判斷此狀態為通水中。此時，根據已選擇好之水質 值等的電氣分解條件，控制部25係對電解槽12 ，給特疋之電解能量。驗性離子水生成模式中，第】電極 ^電極板14a及！4b為陰極，第2電極室用電極板15為 =二Γ路17會吐出驗性離子水且排水通路1如會排 性離子水。此時，第2電極室用節流器η係調整成第 14/22 201238911 2電極室12b之内壓較第}電極室12a之内壓更高。讓第2 電極室12b所生成之酸性離子水之一部份通過殘留氣除去 手段29。此時，可將電氣分解前便包含於原水中的殘留氣、 三鹵曱烷等或因陽極所產生之氣氣造成的殘留氯等去除。 然後，通過由匯流部16之内筒30a與外筒3〇b所設置的流 ΐ調整用孔31a與31b之迴轉位置所形成的開口部，匯流 至第1電極室12a所生成之鹼性離子水。藉此，可抑制鹼 性離子水之pH值。 再者，只要能滿足此關係式〔（第丨電極室12a之出口 側流篁)/(第2電極室12b之出口側流量）〉（第i電極室用 導入通道9之流量)/(第2電極室用導入通道1〇之流量）〕 的結構時，可自由改變第2電極室用節流器丨丨之位置或數 目。即’可設置在第1電極錢導人通道9或吐水通路17、 排水通路18a或18b之途中，亦可設置於複數個位置處。 又，匯流部16可設置在電解槽12内之水流上游側， =可設置於下游側。再者，為了更進—步地抑制第i電極 至12a所生成之鹼性離子水的pH值，將其設置在第2 室12b _性最高之電解槽12内的下游側者較為有效。" 又’殘留氣除去手段29之具體結構可使絲性炭 子交換樹脂、臭氧產生裝置等。又，關於匯流部沾雖 係於圓筒狀内筒3〇a及外筒鳩各自設置有流量辦:， 3la及训。該内筒施連接至步進馬達32而可藉 迴轉•停止，各流量調整用孔3Ia、3lb之重聂乂 仃 効孔徑’故可藉由内筒30a之停止位置來達;;^有 3〇之功能。再者，不使用步進馬達32之=開閉間 筒3〇3連接有能讓使用者旋轉用的刻度盤。T ’、可於内 15/22 201238911 如此，pH值受抑制之鹼性離子水係從吐水通路17吐 出以ί、Ι人用。驗性離子水之—部份係分岐至吐水旁通流路 20，由吐水旁通流路用節流器21來限制於適量流量，導入 至pH感測部22以進行ρΗ值測定。此處，控制部25係讀 取來自pH感測部22之輸出訊號，逐次調整電解的能量， 以達到操作顯示部26所設定好之pH值般地進行控制。然 後通過pH感測部22之驗性離子水在與排水通路匯 流後，則以排水之方式排出。 此時為了使其能飲用且盡可能增加驗性離子水中的 /合氫里在未達pHl〇以上之範圍内，應調整電解能量以盡 可能獲得較高pH值者為佳。 、或是’當電解的能量達最大之狀態下，自pH感測部 22進行pH值測定。若此時達pH1〇以上，則慢慢增加匯流 部16之流量調整用孔仏及训的重疊部分，直到達飲用 pH值的乾圍為止。藉此，可讓從第2電極室⑶流入第1 電極室12a之酸性離子水的量維持較多。 又’在設定之pH值範圍内，控制開閉閥π以使來自 排水通路18b之排水量最少化時，可提高節水劾果。再者， 作為控制開閉閥2 7以使來自排水通路18 b之排水量最少化 的其他方法，可控淑增加吐水稱17线水管徑。 然後，當單位時間内流通之流量等級低於-定量時， 便判斷此狀態為止水’停止朝電解槽12供給電解的能量。 此時，在止水後之-料間内，和電極室用電 對之正霞，對第2電極㈣電極板15施加 負電£。糟此，可將附著於第1電極室用電極板】4a及I4b 16/22 201238911 如以上般’依據本實施例2，電解槽η内之匯流部^ :调整流量之開閉閥3〇(内筒遍、外筒勘)所構成。藉 可，據吐水之p H值讓適量之酸性離子水匯流至驗性離 ϋ雜J合飲用之吐水阳值範圍内’生成溶氫量最高的 二::水。再者，匯流部16具備有殘留氣除去手段29， == 電氣分解前便包含於原水中的殘留氯、 ^或因㈣所產生之氨氣造成的殘留氣等去除。如此生 通:：生水係美味且安全。再者’酸性離子水之排水 Γ備討膽流量之開_ 27，可根據吐水之 值讓來自排水通路18a之排水量達最少化。其結果，可 挺向節水効果。 雷^以明般’ ^、圖2所示魏水生絲置係具有 $槽Π與控制部25。電解槽以有陰極室與陽極室。 =室具有陰極。陽極室具有陽極。電解槽12係將通入之 ^水經電氣分解而生錢性離子水及酸性離子水。更料 ^電_丨2剌通人之原錢行蚊分解。藉此，於陰 °至會生成驗性離子水’於陽極室會生成酸性離子水。控 備：25可控制電解槽12之電解強度。電解水生成裝置： j水通路17與排水稱18。吐水觀17連接至陰極 “猎此，可從吐水通路17將陰極室所生成之驗性離子水 出。排水通路18則連接至陽極室，藉此，可經由排水通 is將陽極室所生成之酸性離子水排出。電解槽12之内 =具有匯流部16。匯流部16係用以讓陽極所生成之酸性離 水的一部份與陰極所生成之鹼性離子水匯流。 '衣又’匯流部16設置於電解槽12内之下軸。又，匯 %部16位在電解槽12内且在較陰極更下游之位置處。又， 17/22 201238911 匯流部16位在電解槽⑽且在較陽極更下游之位置處。 又，陽極室與陰極室係藉由隔膜13a、13b而分隔。 又’匯流部16位在吐水通路17與陽極之間。又，匯 机口卩16位在吐水通路17與陰極之間。 之笛1山排水通路18具有第1端與第2端。排水通路18 •^弟1端係與陽極室直接連接。 又’ f解水生成裝置更具有吐树通流路2()。吐水旁 路20係可讓流通於吐水通路17之液體流人般地配置 产拉t吐水旁通流路2G具有第1端與第2端。吐水旁通 之笛1 <帛1 &連肢吐水通路17，使吐料通流路20 端位在較匯流部16更下游之位置處。藉此，可讓流 k ; 土水通路〗7之液體流入至吐水旁通流路。 又’吐水旁通流路20之第2端連接至排水通路18。 又，吐水旁通流路2〇具有pH感測部22。 入， p感測部22係構成為可對流通於吐水旁通流路 20之液體進行氫離子指數測定。 再者，實施例之感測器不限於PH感測部22。即，感 ::，罐吐水旁通流路20之液體進行氫離子指 、夜’制11只要是料通於吐水旁通流路20之 ，針對能顯示氫離子指數之f訊進行測定者即可。換+ 只要是對流通於吐水旁通流路2G之液體針對i ‘離子指數相當之資訊進行測定者即可。 又，排水通路18更具備有排水通路用節流器19。 再者，排水通路18之第2端定義為排水口。 又’吐水旁通流路20之第2端連接至排水通路18，且 18/22 201238911 位在排水触㈣流心與排水口之間。 :通流路2〇具有吐水旁通流路用節流器1 6構二^ 置更具有流量檢測部6。流量檢測部 6構成為可針對流人電解槽12之液體流量進行檢測。 又，陽極室構成為可經由導入通道而接收水。導入通 道具有陽極室用節流器。 更詳細地，陽極室構成為可經由陽極室用導入通道而 接收液體。陰極室構成為可經由陰極室用導入通道而接收 液體。陽極室用導入通道與陰極室用導入通道係獨立配 置。陽極室用導入通道具有陽極室用節流器。 又’電解水生成裝置具有導入通道。導入通道具有陽 極室用導入通道與陰極室用導入通道。 又，陽極室之内壓設定為較陰極室内壓更高。 又，陽極室與前述陰極室與前述陽極室用導入通道與 前述陰極室用導入通道之間，係設定為能滿足下述關係式。 (第1電極室l2a之出口側流量)/(第2電極室12b之 出口側流量）>(第1電極室用導入通道9之流量)/(第2電 極室用導入通道1〇之流量） 又，如圖2及圖4所示’匯流部16具備可調整流量之 開閉閥30。 又，排水通路18具備可調整流量之開閉閥27 ° 藉由採用前述構成，可提供一種構造單純，可生成驗 性離子水的電解水生成裝置。 【圖式簡單說明】 圖1係本發明之—實施形態中的電解水生成裝置之結 構示意圖。 19/22 201238911 圖2係本發明之另一實施形態中的電解水生成裝置之 結構示意圖。 圖3係同上之電解槽内之陽極室的外部透視圖。 圖4係同上之電解槽内之陽極室的另一例的外部透視 圖。 【主要元件符號說明】 1 原水管道 2 水龍頭 3 本體部 4 淨水部 5a 導入通道 5b 導入通道 5c 導入通道 5d 導入通道 6 流量檢測部 7 鈣供給部用節流器 8 鈣供給部 9 第1電極室用導入通道 10 第2電極室用導入通道 11 第2電極室用節流器 12 電解槽 12a 第1電極室 12b 第2電極室 13a 隔膜 13b 隔膜 14a 第1電極室用電極板 20/22 201238911 14b 第1電極室用電極板 15 第2電極室用電極板 16 匯流部 17 吐水通路 18 排水通路 18a 排水通路 18b 排水通路 19 排水通路用節流器 20 吐水分流通路 21 吐水分流通路用節流器 22 pH感測部 23 電源插頭 24 電源部 25 控制部 26 操作顯示部 27 開閉閥 28 匯流部用節流器 29 殘留氯除去手段 30 開閉閥 30a 内筒 30b 外筒 31a 流量調整用孔 31b 流量調整用孔 32 步進馬達 33 訊號線 訊號線 21/22 34The piping connection portion may have a risk of leaking water from the Q-ring and the package. In order to solve this conventional problem, the present invention aims to provide a simple structure and a low-cost configuration, and the pH of the spouting water does not rise excessively, and the electrolyzed water of the experimental ionized water of the southern squirrel can be produced. Generate a device. In order to solve the above problems, the present invention is an electrolyzed water generating apparatus characterized by comprising: a cathode chamber having a cathode and an anode chamber having an anode, which can electrically decompose the raw water to generate alkaline ionized water. And an electrolysis cell for acidic ionized water; and a control unit for controlling the electrolysis intensity of the electrolysis cell; and a water discharge passage connected to the cathode chamber to discharge the alkaline ionized water generated by the cathode chamber, and connected to the foregoing a drain passage for discharging the acidic ionized water generated by the anode chamber in the anode chamber, wherein the electrolytic cell is provided with a confluent portion, and a part of the acidic ion water generated by the anode is flown to the cathode 5/22 201238911 Just described the ionized water. Further, the busbar portion is preferably configured to be disposed on the downstream side of the electrolytic cell (that is, on the drain passage side). Further, the header portion is preferably configured to include an opening and closing valve having an adjustable flow rate. Further, the header portion is preferably configured to include means for removing residual chlorine in the acidic ion water. Further, it is preferable that the opening and closing valve is provided with an adjustable flow rate at least in the drain passage. [Effect of the Invention] In the present invention, the acid ionized water generated by the anode is formed by providing the bus bar in the inside of the electrolytic cell. One part of the alkaline ionized water generated by the cathode is formed in a simple structure and a low-cost configuration, so that the pH of the spouting water does not rise excessively, and an alkaline ionized water having a high dissolved hydrogen amount can be produced. [Embodiment] Hereinafter, embodiments (Example 1) and (Example 2) of the present electrolyzed water generating apparatus will be described in detail with reference to the drawings. (First Embodiment) Fig. 1 is a schematic view showing the configuration of a first embodiment of the present electrolyzed water generating apparatus. As shown in FIG. 1, the raw water pipe I such as tap water is connected to the water purification part 4 of the main body part 3 via the faucet 2. The water purification unit 4 is provided with an activated carbon capable of adsorbing residual gas in the internal raw water, trihalothane, musty, and the like, and a hollow fiber membrane which can accurately remove general bacteria or impurities. The water filtered by the water purification unit 4 flows from the introduction passage 5 a to the flow rate detecting unit 6 . The flow rate detecting unit 6 confirms that there is a water flow, and instructs the control unit 25 to perform control. The water filtered at the water purification unit 4 is branched into the introduction channels 5b and 5c by the flow rate detecting unit. Imported 6/22 201238911 Ί"! There is a throttle unit 7 and a mother supply unit 8 for the mother supply unit. Word Supply Department #1 7 叮 ° week rectified the flow through the introduction channel 5c. Each supply unit 8 will add oil to the original water towel to improve the electrical conductivity of the raw water. The guide channel & will merge to the guide channel %. The downstream passage of the introduction passage is connected to the first electrode chamber guide passage 9' and reconnected to the i-th electrode chamber of the electrolytic cell 12 via the introduction passage 5d. Further, the second channel chamber introduction passage 10 is formed in the =channel 5d branch. The second electrode to the guide channel 1G is configured to flow through the second electrode chamber to be introduced into the f2b2: the chamber restrictor 11'* to communicate with the electrolytic cell acid I:: 12: the filtered water is electrically decomposed to generate Alkaline ionized water and the second section are separated from the second electrode chamber (10) by a diaphragm. In the first electrode chamber l2a, the first! The electrode plates 15 for the second electrode chamber are disposed in the opposite direction to the electrode plates 14a and 14b for the private cells. On the downstream side of the second electrode chamber 12b in the electric chamber, there is a manifold portion 16 in which the manifold portion 16 is disposed. The downstream portion of the busbar portion 16 is disposed immediately adjacent to each other. The function of the busbar portion 16 is to the ion in the 12a. A part of the second sub-electrode 2 electrode generated in the electrode chamber 12b to the electrode plate 15 is introduced into the first electrode chamber 12a, and the second electrode is connected to the downstream side of the confluent portion 16 of the second electrode. The water of the electric hole (the second electrode chamber electrode plate 15 A is trapped in the case of acidic ionized water) is discharged from the drain passage, and the passages 18a and 18b are provided with a drain passage restricted to the discharge flow. The throttle device 19 is used in the drain passage 18a. The drain passages 18a and 18b are also explained. The pavilion is 7/22 201238911 (4):: f has spit and the road is cathode. It refers to the detection of the electrode to the upstream of the electrode plate 14a and the Mb path 17, and the drinking water is connected and discharged. The water discharge path is connected to the (four) portion 22 via the spout water discharge flow restricting the flow rate. The first electrode chamber (10) in the spouting bypass passage 20 is downstream of the spout bypass passage 20 The positive value of the water is detected. The control unit 25 supplies the energy of the electrolysis to the electrolysis control or the electric decomposing device to the power supply plug, and the electric power is plugged into the power supply plug, and the symbol is converted into a DC power supply. The power supply unit. The AC power supply water or acidic ionized water of the electric power 23, the clean water: 'τ' allows the user to set the operation display part for the experimental selection. The various functions such as the Bay or the ρΗ value are selected. Part 16 and flute 7 α detailed view. t pole chamber 12b ^ # Example 1 in Fig. 3 'confluence unit 1 $ I am a female throttle 28 in the second phase throttle 28. Confluence Ionized water (second electrode chamber water) generated by the electrode chamber electric street i2b is introduced into the > The electrolyzed water generating device of the first embodiment is produced, and the desired water purification mode, etc. Value, and open the tap 2 fish; ^, s 7. The raw water from the tap 2 guides the water in the raw water by the water purification unit 4 8/22 201238911 leaving chlorine or trihalodecane, musty, general bacteria, etc. The impurities are removed and introduced into the channel 5a and passed through the flow detecting portion 6. Then, the portion of the raw water is branched to the inlet. On the side of the 5c side, the amount of flow is limited by the throttle unit 7 of the calcium supply unit. Then, the glycerin phosphate dance or the lactic acid mother is dissolved in the mother supply unit 8 to process the water which is more easily electrically decomposed. Then, it merges with the introduction channel 5b again. The raw water after the flow is passed through the second electrode chamber guide channel = and the second electrode chamber introduction channel 10 (each is the first electrode chamber 12a and the second electrode in the electrolytic cell 12) The chamber 12b is introduced into each of the electrode chambers. Here, the second electrode chamber restrictor n is provided to adjust the internal pressure balance of the i-th electrode chamber 12a and the second electrode chamber 12b. In other words, the flow rate ratio of the flow direction through the first electrode chamber 12a ώ σ and the outlet of the second electrode chamber (3) can be adjusted by changing the flow ratio of the introduction passage 9 through the electrode passage for the i-th electrode chamber (4). . This embodiment! ^, first adjusted to [(the outlet flow side of the i-electrode chamber 12a is it%1? 2 port side flow rate)> (the flow rate of the first electrode chamber introduction passage 9 is 丨 = 2 electrode chamber introduction passage 1 )]. Here, the tendency of the inner electrode of the first electrode chamber 12a to the end of the electrode chamber 12a is greater than that of the fourth electrode chamber 12a, and the tendency of the second electrode chamber 12a to the first electrode chamber 12a. The shape of energy.邶w force is supplied from the power plug 23 to AC100V to generate electrical decomposition of the ^ and the control DC power supply = 第 ^3_25 supplies the energy required for electrical decomposition to the = 15 μ electrode to the plate I Mb and The second electrode chamber uses a lightning plate 15. At this time, the electrode to which the negative voltage is applied to the negative electrode is regarded as the cathode, and when the anode chamber separated by the electrolytic cell is formed by the water-blocking mode, the electrode of the first electrode is used as the electrode to the electrode. The plates Ha and 14b are cathodes, and the electrode plate 15 for the second electrode chamber of 9/22 201238911 is an anode. Then, after the water supply is started, the control unit 25 reads the output call from the flow rate detecting unit 6, and when the flow rate level (four) flowing per unit time exceeds a certain amount, it is judged that the state is the water passing. At this time, based on the selected electric decomposition conditions such as the water quality mode and the p-value, the control unit 25 supplies the electrolytic energy to the electrolytic cell 12. In the experimental ion water generation mode, the first electrode chamber β electrode plates 14a and 14b are cathodes, and the 电极2 electrode chamber electrode plates are anodes. At this time, the spouting water passage i7 exudes the test ion water and the drain water is passed, and Acidic ionized water will be discharged. Further, at this time, the internal pressure of the second electrode chamber 12b is adjusted by the second electrode chamber, i.e., the gripping state 11, so that the internal pressure is higher than that of the second electrode chamber. The portion of the acidic ion water generated by the second electrode (3) passes through the restrictor 28 of the confluence portion provided in the confluence portion 16 to converge the alkaline ion water generated by the first electrode chamber 12a, thereby suppressing Verify the pH of the water. In addition, as long as the relationship ([the outlet side flow of the i-electrode chamber 12a]/(the outlet side flow rate of the second electrode t12b)> (the flow rate of the lead-in electrode chamber introduction passage 9)/( When the second electrode chamber is configured to have a flow rate of the introduction passage 1), the position of the second electrode chamber restrictor u can be freely changed, for example, it can be slid in the ith electrode chamber introduction passage 9 or spouted. The passage 7 and the passage of the drain passage 18a or i8b may be disposed at a plurality of positions, and the confluence portion 16 may be disposed on the upstream side of the water flow in the electrolytic cell 12, and may be disposed on the downstream side. Furthermore, in order to further suppress the first! The pH of the alkaline ionized water generated by the electrode = 12a is preferably set in the second electrode chamber and the downstream side of the electrolytic cell 12 having the highest acidity in the 12b. Further, the position of the throttle portion restrictor 28 may be at the upper portion of the bus portion 16 or at the side portion of 10/22 201238911. In this way, by the throttle unit 28, the ionic ion water spit water secret 17 is used as a fresh = suppression test Λβ, /ν. . , , ^ 乂仏1 person. One of the alkaline ionized waters is 2 仏岐 仏岐 吐 吐 旁 旁 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 〇 限制 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 Here, the PH value of the 25 t22 money line is deleted, and the rhyme is captured. The output signal from the PH sensing unit 22 is broken, and the energy of the electrolysis is successively controlled to achieve the PH value of the operation. After that, the alkaline ionized water passing through the pH sensing portion 22 is merged with the drainage passage 18b, _ at this time, in order to make it drinkable and discharge 0^ - ^ υΐΛ In the range above the ionized water, it is better to adjust the energy of the electrolysis to the value of ί ιΓ. At this time, the 16th position of the confluence unit can concentrate the acidic ionized water with higher acidity to the electricity and to 12a. The generated ionized water is formed, and then the pH of the test ionized water is unchanged, and as a result, the gas in the first electrode chamber 12a generates alkaline ionized water having a large amount of dissolved hydrogen. «Additional life, then, when it is circulated in a unit of time, it will judge the state of the water, shut down the business to the snow _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ After the water, within a fixed time, apply a positive voltage to the first and 14b to the electrode plate... Negative voltage έ , 施加 施加 包 包 包 包 包 包 包 包 包 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加 施加In the first and second embodiments, the confluence portion 16 is caused to flow from the electrolysis trough to the portion of the (tetra)-ion water generated by the cathode due to the double-producing ionized water. Therefore, it is not necessary to be known. Π/22 201238911 Technology-like electricity (4) Outside (4) t-channel continuous reduction (4), can reduce the cost. In addition, it can also reduce the leakage of the 〇-type ring or seal from the connection part of the piping. The simple structure and the tilting arrangement 2 are easy to achieve miniaturization of the electrolyzed water generating system. Further, since the confluent portion 16 is disposed on the downstream side of the electrolytic cell 12 (that is, on the side of the drainage path 18a), the acidity with higher acidity can be obtained. The ionized water merges into the secret ion water produced by the cathode, and the pH value of the drinking hydrophobic ion water is adjusted by the pH sensing unit 22 while the pH value displayed by the object portion is lightly displayed. As a result, the value of the water spouting does not rise excessively ^ and the amount of dissolved hydrogen is more efficiently generated. Further, as an example of the confluence portion 16, a portion of the diaphragms i3a, 13b partitioning the second electrode chamber 12b may be provided with a penetration hole, and the throttle portion 28 may be used to adjust the penetration. The structure of the size of the hole is the same as that of the embodiment, and the same reference numerals are given to the embodiment. The difference between the present embodiment 2 and the first embodiment is that the electrolytic cell I] is provided with an open-close valve and a residual chlorine removal means for adjusting the flow rate, and is provided at least at the acidic ion water drainage path. There is an on-off valve with adjustable flow. Based on the above difference, the operation of the electrolyzed water generating apparatus of the second embodiment will be described with reference to Figs. 2 and 4 . 2 is a schematic view showing the structure of the electrolyzed water Zhucheng apparatus of Embodiment 2. In Fig. 2, an opening and closing valve 27 is provided in the middle of the drain passage 18a, and the flow 1 flowing through the drain passage 18a can be freely adjusted in accordance with an instruction from the control unit 25. Symbol 33 is to input the control signal from the control unit to the signal line of the closed valve 27 of 12/22 201238911. Fig. 4 is a detailed view of the second embodiment of the bus portion 16 and the second electrode chamber 12b. In Fig. 4, the opening and closing valve 3 is composed of an inner cylinder 30a and an outer cylinder 30b to constitute a confluence portion 16. The inner cylinder 30a is disposed directly behind the second electrode chamber 12b. The residual gas removing means 29 is accommodated in the inner cylinder 30a. The residual gas removal hand & 29 is for removing residual gas or trihalodecane in the water introduced into the first electrode chamber 12a (Fig. 2) from the second electrode chamber 12b (Fig. 2) via the bus portion 16. The inner cylinder 30a is housed in the outer cylinder 30b. The inner cylinder 30a is provided with a flow rate adjustment hole 31a, and the outer cylinder 30b is provided with a flow rate adjustment hole 31b. The inner cylinder 3A is connected to a stepping motor 32 which is rotatable and stopped at an arbitrary position in accordance with an instruction from the control unit 25. Reference numeral 34 in Fig. 2 is a signal line for inputting a control signal from the control unit 25 to the stepping motor 32. In FIG. 2, the user controls a specific button of the operation display unit 26 to select a desired water quality mode and pH value such as an ionized ion water generation mode, an acidic ion water generation mode, or a water purification mode, and opens the faucet 2 To pass water. The raw water introduced from the faucet 2 is removed by the water purification unit 4 (4) air retention or trihalogenation m-like fine g, and passes through the channel 5a and passes through the flow rate detecting unit. Then, one part of the raw water is smashed to the side of the introduction channel 5c, and is restricted to an appropriate amount of flow by the throttle portion 7 of the calcium supply portion, and the glycerin-filled thief lactic acid sentence is dissolved at the contact portion 8 to be processed. Water that is easier to electrically decompose. Then, it merges with the introduction channel 5b again. The raw water after the confluence is provided through the second electrode chamber introduction channel 9 and the =2 electrode chamber introduction channel 1 (each of which is provided for the first electrode to the 2a and the second electrode chamber 12b in the electrolytic cell) Import to the respective electrodes to. Here, the second electrode chamber restrictor is provided to adjust the internal pressure balance of the i-th electrodes 13/22 201238911 to 12a and the second electrode chamber 12b. After flowing through the first electrode chamber 12a* port side and the second electrode chamber 12b outlet, the convection is changed by the flow ratio of the first electrode chamber introduction passage 9 and the third electrode = V inlet channel 1〇. Adjust it. This embodiment has been adjusted to [(the outlet flow rate of the i-electrode chamber 12a = the outlet side flow rate of 2b)] (the first electrode chamber introduction passage · the second electrode chamber material - the flow rate of the passage 1)] . Here, the internal pressure of the second ii) 2b is higher than the internal pressure of the ith electrode chamber ^. The water of the polar chamber 12b has a tendency to flow toward the first electrode chamber i2a, and the Aci〇 is supplied from the power plug 23. 〇v, with the =24 within the Wei and the control DC power supply for the electrical points = 罝. Next, the energy required by the spleen of the control unit 25 is 12d m _ is supplied to the electrode wall (10) and the second electrode is used to treat the h electrode of the 2 2 S3 as an yin. The anode chamber and the cathode chamber separated by and are formed in 12. Further, the test polarity is =; the first electrode chamber electrode plates A and Mb are cathodes, and the second electrode to electrode plate 15 is an anode. 6 :! The initial tilting & controlling unit 25 reads the two from the flow detecting unit. When the flow rate of the flow in the early time exceeds, it is judged that the state is the water passing. At this time, the control unit 25 supplies the electrolysis energy to the electrolytic cell 12 based on the electric decomposition conditions such as the selected water quality value. In the experimental ion water generation mode, the first electrode ^ electrode plate 14a and ! 4b is a cathode, and the electrode plate 15 for the second electrode chamber is = the second circuit 17 will discharge the ionizing water and the drainage channel 1 will discharge the ionized water. At this time, the second electrode chamber throttle η is adjusted to be 14/22 201238911. The internal pressure of the electrode chamber 12b is higher than the internal pressure of the first electrode chamber 12a. A part of the acidic ionized water generated by the second electrode chamber 12b is passed through the residual gas removing means 29. In this case, residual gas contained in the raw water, trihalodecane, or the like, or residual chlorine caused by the gas generated by the anode, may be removed before the electric decomposition. Then, the opening formed by the rotation positions of the flow regulating holes 31a and 31b provided in the inner tube 30a and the outer tube 3'b of the confluent portion 16 merges with the alkaline ions generated in the first electrode chamber 12a. water. Thereby, the pH of the alkaline ionized water can be suppressed. In addition, as long as the relationship [(the outlet side flow of the second electrode chamber 12a) / (the outlet side flow rate of the second electrode chamber 12b)] (the flow rate of the i-electrode chamber introduction passage 9) / (the In the case of the structure in which the flow rate of the introduction passage 1 is 2), the position or the number of the second electrode chamber restrictor 可 can be freely changed. That is, it may be provided in the middle of the first electrode money guide passage 9, the water discharge passage 17, and the drain passage 18a or 18b, or may be provided at a plurality of positions. Further, the confluence portion 16 may be disposed on the upstream side of the water flow in the electrolytic cell 12, and may be disposed on the downstream side. Further, in order to further suppress the pH of the alkaline ionized water generated by the i-th electrode to 12a, it is effective to provide it in the downstream side of the electrolytic cell 12 having the highest temperature in the second chamber 12b. " Further, the specific structure of the residual gas removing means 29 can be a filamentous carbon exchange resin, an ozone generating apparatus or the like. In addition, the flow-receiving portion is provided in the cylindrical inner cylinder 3〇a and the outer cylinder, and the flow rate is provided: 3la and training. The inner cylinder is connected to the stepping motor 32 and can be rotated and stopped. The weight of each of the flow regulating holes 3Ia, 3lb can be reached by the stop position of the inner cylinder 30a; The function of 〇. Further, the dial for the rotation of the user is not connected to the opening/closing cylinder 3〇3 of the stepping motor 32. T ’ can be used in the inner 15/22 201238911, and the alkaline ionized water whose pH is suppressed is discharged from the spouting passage 17 for use. The portion of the test ion water is branched to the jet water bypass passage 20, and is restricted by an appropriate amount of flow rate by the spout bypass passage restrictor 21, and introduced into the pH sensing portion 22 to measure the pH value. Here, the control unit 25 reads the output signal from the pH sensing unit 22, and sequentially adjusts the energy of the electrolysis to control the pH value set by the operation display unit 26. Then, the inspecting ionized water passing through the pH sensing unit 22 is discharged to the drain passage after being merged with the drain passage. In this case, in order to make it drinkable and to increase the amount of hydrogen in the ionic water in the range of less than pH l〇, it is preferable to adjust the electrolysis energy to obtain a higher pH as much as possible. Or, the pH is measured from the pH sensing unit 22 when the energy of the electrolysis is maximized. When the pH is equal to or higher than pH 1 at this time, the overlapping portion of the flow rate adjusting hole and the training portion of the flow portion 16 is gradually increased until the dry limit of the pH value is reached. Thereby, the amount of acidic ionized water flowing into the first electrode chamber 12a from the second electrode chamber (3) can be kept large. Further, when the opening and closing valve π is controlled within the set pH range to minimize the amount of water discharged from the drain passage 18b, the water saving effect can be improved. Further, as another method of controlling the opening and closing valve 27 to minimize the amount of drainage from the drain passage 18b, it is possible to control the water discharge to be referred to as the 17-line water pipe diameter. Then, when the flow rate level per unit time is lower than - the amount is determined, the water is judged to stop supplying energy for electrolysis to the electrolytic cell 12. At this time, in the inter-material after the water stop, the electric current is applied to the electrode chamber to apply a negative electric charge to the second electrode (four) electrode plate 15. In this case, the electrode plate for the first electrode chamber 4a and I4b 16/22 201238911 can be used as described above. According to the second embodiment, the confluence portion in the electrolytic cell n: the opening and closing valve 3 of the flow rate is adjusted (inside) It consists of a tube and an outer tube. By the way, according to the p H value of the spit water, an appropriate amount of acidic ionized water is converged to the range of the positive value of the spit water of the mixed drinking. Further, the bus portion 16 is provided with a residual gas removing means 29, == residual chlorine contained in the raw water before the electrical decomposition, or residual gas due to the ammonia gas generated in (d) is removed. So live:: Raw water is delicious and safe. Furthermore, the drainage of the acidic ionized water is required to minimize the amount of drainage from the drainage passage 18a according to the value of the spouting water. As a result, the water saving effect can be achieved. Lei ^ is as good as ^ ^, as shown in Figure 2, the Weishui raw silk system has a slot and control unit 25. The electrolytic cell has a cathode chamber and an anode chamber. = The chamber has a cathode. The anode chamber has an anode. The electrolytic cell 12 electrically decomposes the water into the ionized ionized water and the acidic ionized water. More material ^ electric _ 丨 2 剌 pass the original money to kill mosquitoes. Thereby, the ionized water will be generated in the anode to produce acidic ionized water in the anode chamber. Control: 25 controls the electrolytic strength of the electrolytic cell 12. Electrolyzed water generating device: j water passage 17 and drainage scale 18. The spouting water 17 is connected to the cathode. Here, the accumulating ion water generated by the cathode chamber can be discharged from the spouting passage 17. The drain passage 18 is connected to the anode chamber, whereby the anode chamber can be generated via the drain passage is The acidic ionized water is discharged. The inside of the electrolytic cell 12 has a confluent portion 16. The confluent portion 16 is configured to allow a portion of the acidic water generated by the anode to merge with the alkaline ionized water generated by the cathode. 16 is disposed in the lower axis of the electrolytic cell 12. Further, the sinking portion 16 is located in the electrolytic cell 12 and at a position further downstream than the cathode. Further, 17/22 201238911 the confluent portion 16 is located in the electrolytic cell (10) and is Further, the anode is further downstream. Further, the anode chamber and the cathode chamber are separated by the separators 13a and 13b. The 'flow portion 16 is located between the jetting passage 17 and the anode. Further, the outlet port 16 is at the spouting passage. 17 between the cathode and the cathode. The flute 1 mountain drainage passage 18 has a first end and a second end. The drain passage 18 is connected directly to the anode chamber. The 'f water-supplied device has a spit-tree flow. Road 2 (). The spouting bypass 20 system allows the liquid to flow through the spouting passage 17 The ground distribution bypass water flow path 2G has a first end and a second end. The spit water bypass flute 1 < 帛 1 & limb limb spouting passage 17 makes the end of the spout passage 20 at the confluence The portion 16 is further downstream. Thereby, the liquid of the stream k; the soil water passage 7 flows into the jet water bypass passage. Further, the second end of the spout bypass passage 20 is connected to the drain passage 18. The water spouting passage 2 has a pH sensing unit 22. The p sensing unit 22 is configured to perform hydrogen ion index measurement on the liquid flowing through the jet bypass passage 20. Further, the sense of the embodiment The detector is not limited to the pH sensing unit 22. That is, the sense:: the liquid in the canister spouting flow path 20 is subjected to hydrogen ion fingering, and the nighttime system 11 is intended to be displayed through the spouting bypass flow path 20 for display. The measurement of the hydrogen ion index can be performed as long as it is a measurement of the information corresponding to the i 'ion index of the liquid flowing through the spout bypass flow path 2G. Further, the drainage passage 18 is provided with drainage. The passage restrictor 19. Further, the second end of the drain passage 18 is defined as a drain port, and the second portion of the spout bypass passage 20 The end is connected to the drain passage 18, and 18/22 201238911 is located between the drain contact (four) flow center and the drain port. : The through-flow passage 2 has a spouting bypass passage for the throttle device. The detecting unit 6. The flow rate detecting unit 6 is configured to detect the flow rate of the liquid in the flow cell 12. The anode chamber is configured to receive water through the introduction passage. The introduction passage has a throttle for the anode chamber. The anode chamber is configured to receive the liquid through the anode chamber introduction passage. The cathode chamber is configured to receive the liquid through the cathode chamber introduction passage. The anode chamber introduction passage and the cathode chamber introduction passage are disposed independently of each other. The introduction passage for the anode chamber has a restrictor for the anode chamber. Further, the electrolyzed water generating device has an introduction passage. The introduction passage has an introduction passage for the anode chamber and an introduction passage for the cathode chamber. Further, the internal pressure of the anode chamber is set to be higher than the cathode chamber pressure. Further, the anode chamber and the cathode chamber and the anode chamber introduction passage and the cathode chamber introduction passage are set to satisfy the following relationship. (flow rate at the outlet side of the first electrode chamber 12a) / (flow rate at the outlet side of the second electrode chamber 12b) > (flow rate of the introduction passage 9 for the first electrode chamber) / (flow rate of the introduction passage 1 for the second electrode chamber) Further, as shown in FIGS. 2 and 4, the "flow portion 16" is provided with an on-off valve 30 that can adjust the flow rate. Further, the drain passage 18 is provided with an opening and closing valve 27 that can adjust the flow rate. By adopting the above configuration, it is possible to provide an electrolyzed water generating apparatus which is simple in structure and capable of generating the test ionized water. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the structure of an electrolyzed water generating apparatus in an embodiment of the present invention. 19/22 201238911 Fig. 2 is a schematic view showing the structure of an electrolyzed water generating apparatus in another embodiment of the present invention. Figure 3 is an external perspective view of the anode chamber in the same electrolytic cell. Figure 4 is an external perspective view of another example of the anode chamber in the same electrolytic cell. [Description of main component symbols] 1 Raw water pipe 2 Faucet 3 Main body part 4 Purification water part 5a Introduction channel 5b Introduction channel 5c Introduction channel 5d Introduction channel 6 Flow rate detection unit 7 Throttler for calcium supply unit 8 Calcium supply unit 9 First electrode Chamber introduction channel 10 Second electrode chamber introduction channel 11 Second electrode chamber throttle 12 Electrolysis cell 12a First electrode chamber 12b Second electrode chamber 13a Diaphragm 13b Diaphragm 14a Electrode plate for the first electrode chamber 20/22 201238911 14b Electrode plate for the first electrode chamber 15 Electrode plate for the second electrode chamber 16 Confluence portion 17 Discharge passage 18 Drainage passage 18a Drainage passage 18b Drainage passage 19 Throttle passage restrictor 20 Sewage flow passage 21 Throttle flow passage section Flow device 22 pH sensing unit 23 Power plug 24 Power supply unit 25 Control unit 26 Operation display unit 27 Opening and closing valve 28 Confluence unit throttle unit 29 Residual chlorine removal means 30 Opening and closing valve 30a Inner tube 30b Outer tube 31a Flow rate adjustment hole 31b Flow adjustment hole 32 Stepping motor 33 Signal line signal line 21/22 34