TW201033133A - Electrolytic water purifier - Google Patents

Electrolytic water purifier Download PDF

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Publication number
TW201033133A
TW201033133A TW098113286A TW98113286A TW201033133A TW 201033133 A TW201033133 A TW 201033133A TW 098113286 A TW098113286 A TW 098113286A TW 98113286 A TW98113286 A TW 98113286A TW 201033133 A TW201033133 A TW 201033133A
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TW
Taiwan
Prior art keywords
water
oxygen
hydrogen
storage tank
control device
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TW098113286A
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Chinese (zh)
Inventor
Toshiaki Omote
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Arega Corp Co Ltd
Toshiaki Omote
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Application filed by Arega Corp Co Ltd, Toshiaki Omote filed Critical Arega Corp Co Ltd
Publication of TW201033133A publication Critical patent/TW201033133A/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/68Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply
    • C02F2103/04Non-contaminated water, e.g. for industrial water supply for obtaining ultra-pure water
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Water Treatment By Sorption (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

A novel electrolytic water purifier is provided by which the amount of hydrogen dissolved in drinking water can be kept in a certain range without decreasing. The water purifier includes a carbon filter (13), etc. for purifying water, a cold-water tank (22) in which the water having passed through the reverse osmosis membrane filter (16), etc. is stored, and a cold-water discharge opening (3) through which the water stored in the cold-water tank (22) is discharged. The water purifier further includes a reverse osmosis membrane filter (16) with which pure water is produced from the water having passed through the carbon filter (13), etc., a supply route through which the pure water produced is supplied from the reverse osmosis membrane filter (16) to the cold-water tank (22), an electrolytic device (32) in which part of the pure water produced with the reverse osmosis membrane filter (16) is electrolyzed to generate hydrogen gas, a circulation route through which the treated water taken out of the cold-water tank (22) is returned to the cold-water tank (22), and a circulation pump (62) which is disposed in the circulation route and through which the treated water taken out of the cold-water tank (22) and the hydrogen gas are returned together to the cold-water tank (22).

Description

201033133 六、發明說明: 【發明所屬之技術領域】 本發明,係關於一種用以將自來水等加以淨化,而供 給一般家庭、營業所等所飲用之水之電解式淨水装置。' 【先前技街】 ❹ 近年來,因健康意志的高漲,用以對供給自上水道之 自來水進行淨化之淨水裝置廣泛普及。尤其是家庭所使用 之淨水裝置,係具有藉由從上方將水倒入,利用水本身的 重量,使其通過含有活性碳、礦石等之過遽器的類型;或 在使其通過連接於自來水管之過㈣後,藉由將附水㈣ 或旋塞)打開,利用水管的水壓使水流出的類型;或者是先 將以過渡器等過濾自來水管所供給之自來水所得之水儲存 在儲槽’然後適當使水流出加以飲用的類型。 ◎ 又目前為止提出有—種於上述淨水裝置附加有電 能者。亦即’係-種具備有藉由對供給自上水道之自 來水進二電解’生成氫氣’然後使此氫氣溶解於上述自來 二水:置。此淨水裝置,主要目的係提升處理 質成對:康有益之:(氧二還專原電位’藉由增加溶氫’可改 M參照專利文獻1、2)。 (專利文獻υ日本特開2005_261999號公報 (專利文獻2)日本特許第26〇5642號公報 【發明内容】 4 201033133 然而’上述各專利文獻所揭示之淨水裝置,水之溶氣 量,會隨著時間之經過而慢慢地降低,大部分在飲用時之 溶氫罝會變得極為微量,上述水之改質的效果亦隨著時間 之經過而逐漸減半。 因此,本發明係為了解決上述以往之電解式淨水裝置 所具有之課題而提出者,其目的在於提供—種不降低所飲 參 用之水的溶氫量而可一直保持在一定範圍之新賴電解式淨 水裝置。 本發明係為解決上述之課題而提出者,第1發明(請求 項1所記載之發明)之電解式淨水裝置,具備有用以將:加 以淨化之淨水處理部、儲存經由此淨水處理部之水的處理 水儲槽、及用以供應储存在此處理水儲槽之水的出水部, 其特徵在於,係具備有自經由該淨水處理部 i 的純水生成部、用以將自此純水生成部所生成之純= 至該處理水儲槽的供給通路、用以對該純水生成部所生成 之純水的一部分進行電解,藉此生成氫氣的氫氣生成部、 用以自該處理水儲槽内取出處理水,再一次使其回到 理水储槽的循環通路、及設置在此循環通路之中途部y用 以使自該處理水儲槽所取出之處理水與該氫氣—起回到該 處理水儲槽的循環泵。 x 淨化此二1發:,會先以淨水處理部將自來水等之水加以 β化H藉由純水生成部使其變成純水, 於處理水儲槽。另一部分,則送至氨氣:存 電解。藉由此電解,生成翁畜.^ 籍此違仃 解成氫乳。此所生成之氫氣,藉由循 201033133 環泵,將會一邊溶解於自該處 处视水儲槽所取出之水,一邊 經由該循環通路而儲存於處 ^ ., 水儲槽。另,此處理水儲槽 内之水,可自出水部供應至外 ^ ^ Γ ' 使用者可飲用之。因此, 根據此電解式淨水裝置,儲尨 儲存於處理水儲槽内之水’藉由 該擔環栗之驅動,會峨由猫搭 嘗,左由循環通路而循環,藉此使處理水 中之溶氫量慢慢増加,你用各+ 更用者可在溶氫量接近飽和狀態之 狀態下飲用。 又’第2發明(請求項2所記載之發明),其特徵在於, 係於該第1發明中’該循環通路之中途部於該循環泵與 處理水儲槽之間’設置有用以使該氫氣之氣泡微細化的氣 泡微細化過濾器。 此第2發明之電解式淨水裝置,由於藉由該氣泡微細 化過濾器使氫氣之氣泡微細<匕,因此可更加提高處理水中 之溶氫量。 又,第3發明(請求項3所記載之發明),其特徵在於, 係於該第1或第2發明中’該循環系與氫氣生成部,係連 接於内裝有定時器之控制裝置而成,且此控制裝置連接有 光照度感測器,透過該光照度感測器,當該控制裝置判定 為規定之照度時,則透過定時器,使該循環泵與氫氣生成 部於規定時間内被反覆驅動與停止。 此第3發明之電解式淨水裝置,藉由光照度感測器, 虽控制裝置判斷達到規定之光之照度時,則該循環泵與氫 氣生成部將會一起開始驅動。又,透過定時器,當控制裝 置判疋此等循環泵與氫氣生成部之驅動已經過規定時間 201033133 時,則僅將該循環泵與氫氣生成 ^ ^ 心驅動停止規定時間, 又,進一步虽控制裝置判定該循 α . 娜艰糸與氫氣生成部之停止 已 ',’虽過規疋時間時,則控制裝置具 生法m無 裝置再-次開始循環泵與氫氣 二ΐ以此方式,此第3發明之電解式淨水裝置, =制為反覆循環栗與氣氣生成部之驅動的開始及停止, ❹ 第3發明之電解式淨水裝置,不僅可將處理水中之溶氣量 保持在一定量,而且還可省電。 係於請求項4所記載之發明),其特徵在於, t第2或第3發明t,於該氫氣生成部,連接有 氧氣〜通通路,該氧氣流通 而與氫氣-起生成之氧氣該純水之電解 I軋流通,且此氧氣流通通路之前 端’為用以放出使用者所吸取之氧氣的氧氣放出口。 ^ 4㈣n切水裝置,由對純水進行電解而 1· ^產生之氧氣,將會通過該氧氣流通通路内而自 =氣放出π放出。因此,根據此帛4發日月,使 =放出口所放出之氧吸入體内,而可有效利用由電解所 生成之氧氣。 又’第5發明(請求項5所記载之發明)’其特徵在於, 糸於該第4發明中’在該氧氣流通通路之中途部設置有 ^以將該氧氣加以送出之風扇,且此風扇係連接於該控制 ^且於該控制|置連接有氧放出用開Μ,在該循環果 氣生成部之驅動停止時,當該控制裝置判定該氧放出 用開關為ON的時候:,# θ β & 矸候該風扇與循環泵與氫氣生成部將會開 7 201033133 始驅動。 此第5 #明之電解式淨水裝置,|該循環栗與氮氣生 成部之壤動停止時,當該控制裝置判定該氧放出用開關為 ON的時候’該風扇與循祕與氫氣生成部將會開始驅動。 因此,藉由以上述方式開始驅動氫氣生成部與循環泵,不 僅可生成氩氣,使處理水儲槽内之溶氫量強制增加而且 藉由開始驅動該風扇,可使流入氧氣流 規定之㈣自絲氣放出口放出。因此,㈣;= 之電解式淨水裝置,即使是在循環泵與氣氣生成部之驅動 停止時,當使用者有吸取氧氣之必要性的時候,亦可隨時 藉由使上述開關為ON來吸取氧氣。 a於第i發明(請求項!所記載之發明)中,由該氫氣生成 播P所生成之氫氣’ #由循環栗邊溶解於自該處理水儲 所取出之水’-邊經由該德環通路㈣存於處理水錯 :吾因此可使處理水中之溶氫量慢慢增加,使用者可在溶 =飽和狀態之狀態下㈣,且可不降低所飲用之水 的 >谷氫量而保持在一定的範圍。 又’於S 2發明(請求項2所記載之發明)中由於藉由 微細化繼’使氫氣之氣泡微細化,因 “處理水中之溶氫量’可不降 保持在-定的範圍。 用《水的冷氫量而 又,於第3發明(諳龙 為反覆該循環泵與氫氣生成中,由於控制 一直使循環泵與氫氣生成部 亭 而非 子項驅動。因此不僅可將處理 201033133 χ中之冷氫量保持在一定量,而且還可省電。 又,於第4發明(請求項4所記載 進行電解而與氫氣一 ^由對純水 通通路内而自氧氣放出σ由於會流入該氧氣流 出口所心之==因此使用者可將自氧氣放 之氧氣。 趙内,而可有效利用由電解所生成 發明(請求項5所記載之發明)中,在該循環 e 、成部之驅動停止時,當該控制裝置判定該氧放 出用開關為ON的時候’姻扇與循環泵與氫 開始驅動,藉由以上述方式開始驅動氣氣生成::: 杲,不僅可生錢氣,使處縣賴狀溶氫㈣制增加, 而且藉由開始驅動該風扇,可使流入氧氣流通通路内之 氣以規定之壓力自該氧氣放出口放出。因此,根據此第$ 發明之電解式淨水裝置,即使是在循環果與氣氣生成部之 驅動停止時,當使用者有吸取氧氣之必要性的時候,亦可 隨時藉由使上述開關為ON來吸取氧氣。 w 【實施方式】 以下’ -邊參照圖式,一邊詳細說明用以實施本發明 之實施形態之電解式淨水裝置。 此實施形態之電解式淨水裝置卜係家庭所使用之淨水 裝置’如圖1所示,於成形為長方體狀之框體2内,收納 有後述之冷水儲槽22(本發明之處理水儲槽)、溫水儲槽 23、加壓泵15等。又,於上述框體2之正面的稍微偏上方, 9 201033133 形成有凹部2a ’在此凹部2a内,設置有冷水用出水口 3(本 發明之出水部)、及與此冷水用出水口 3並排之溫水用出水 口 4。上述冷水用出水口 3,係供應後述冷水儲槽(構成本發 明之處理水儲槽)22内之飲用水的部位,上述溫水用出水口 4 ’則是供應後述溫水儲槽23内之飲用水的部位。又,於 上述冷水用出水口 3之後方,設置有構成開關閥之冷水用 開關操作桿5,而於上述溫水用出水口 4之後方,則設置有 構成開關閥之溫水用開關操作桿6。 此等冷水用開關操作桿5及溫水用開關操作桿6,皆連 結於未圖示之開關閥而成,藉由未圖示之彈性材,彈壓於 前方向(關方向)而成,透過未圖示之杯子等容器(或藉由使 用者之手指)由使用者向後方擠壓,藉此可自上述冷水用出 水口 3、溫水用出水口 4供應冷水或溫水。另,於上述凹部 2a内之上述冷水用出水口 3、溫水用出水口 4的下方,設置 有可承載未圖示之杯子的支承板2f()於此支承板2f,形成 有自上述冷水用出水口 3、溫水用出水口 4所供應之冷水或 溫水可通過的通孔2g,在此通孔2g的下方,係連接有未圖 示之排水用管的一端,而該排水用管的另一端則連接於未 圖示之排水用儲槽。又,於圖i所示之框體2的右側板2d, 設置有用以吸取氧氣之氧吸取管7,此氧吸取管7之後端係 連接於後述電解裝置32(本發明之氫氣生成部)的氧氣排出 d 39d 〇 又,於上述凹部2a之上方,固定有上正面面板沘,於 此上正面面板2b,設置有圓形之顯示面板8、及設於此顯 10 201033133[Technical Field] The present invention relates to an electrolytic water purification device for purifying tap water or the like and supplying it to water consumed by a general household, a business office or the like. In the past, the water purification device for purifying the tap water supplied from the sewer is widely used. In particular, the water purification device used in the home has a type in which the water is poured from above, and the weight of the water itself is passed through a filter containing activated carbon, ore, or the like; After the water pipe has passed (4), by using the water (4) or the cock to open, the water pressure of the water pipe is used to make the water flow out; or the water obtained by filtering the tap water supplied by the water pipe is stored in the storage. The trough 'is then properly allowed to flow out of the type of drinking. ◎ It has been proposed so far that the above-mentioned water purifying device is equipped with electric energy. That is, the 'system type is provided by generating hydrogen gas by electrolysis of tap water supplied from the sewer water, and then dissolving the hydrogen gas in the above-mentioned tap water: The main purpose of this water purifying device is to improve the quality of the processing: it is beneficial to: (Oxygen is also used to increase the hydrogen potential by the addition of the original potential). Refer to Patent Documents 1 and 2). (Patent Document 2) Japanese Laid-Open Patent Publication No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. As time passes, it gradually decreases, and most of the dissolved hydrogen hydrazine during drinking becomes extremely small, and the effect of the above-mentioned water reforming is gradually halved with the passage of time. Therefore, the present invention is to solve the above problem. In view of the problems of the conventional electrolytic water purification device, the object of the present invention is to provide a new-type electrolytic water purification device that can maintain a constant range without reducing the amount of dissolved hydrogen in the water to be used. In order to solve the problems described above, the electrolytic water purification device according to the first aspect of the invention (the invention of claim 1) includes a purified water treatment unit for purifying the water purification unit and storing the water purification treatment unit. The treated water storage tank of the water and the water discharge part for supplying the water stored in the treated water storage tank are characterized in that the pure water generating unit that passes through the purified water treatment unit i is used. The hydrogen generation unit that generates hydrogen gas from the pure water generated by the pure water generating unit to the supply passage of the treated water storage tank and a part of the pure water generated by the pure water generating unit is electrolyzed. Taking the treated water from the treated water storage tank, returning it to the water storage tank again, and the treatment water set in the middle of the circulation passage for taking out the treated water storage tank The hydrogen pump is returned to the circulating water pump of the treated water storage tank. x Purifying the two rounds: First, the water such as tap water is beta-formed by the purified water treatment unit, and the pure water generating unit is made pure. Water, in the treatment of water storage tank. Another part, then sent to the ammonia gas: deposit electrolysis. By this electrolysis, the generation of Weng livestock. ^ This is illegally resolved into hydrogen milk. The hydrogen produced by this, by the 201033133 ring pump, It will be dissolved in the water taken out from the water storage tank and stored in the water storage tank through the circulation passage. In addition, the water in the treated water storage tank can be supplied from the water outlet. To the outside ^ ^ Γ ' The user can drink it. Therefore, according to this electrolysis The water purification device, the water stored in the treated water storage tank, is driven by the catguin, and is smashed by the cat, and the left side is circulated by the circulation passage, thereby making the dissolved hydrogen in the treated water slow. In the case of the first invention, the second invention (the invention described in claim 2) is characterized in that it is used in the first invention. In the middle of the circulation path, a bubble refining filter for refining the bubble of the hydrogen gas is provided between the circulation pump and the treated water storage tank. The electrolytic water purification device according to the second invention is In the bubble fine refining filter, the hydrogen gas bubbles are finely sized, so that the amount of hydrogen dissolved in the treated water can be further increased. The third invention (the invention according to claim 3) is characterized in that the first or In the second aspect of the invention, the circulation system and the hydrogen generating unit are connected to a control device having a timer built therein, and the control device is connected to the illuminance sensor, and the illuminance sensor is passed through the illuminance sensor. When the illuminance is specified, Over timer, so that the circulation pump with the hydrogen generation unit within a predetermined period of time is repeatedly driven and stopped. In the electrolytic water purifying apparatus according to the third aspect of the invention, the illuminance sensor detects that the illuminance of the predetermined light is reached, and the circulation pump and the hydrogen generating unit start driving together. Further, when the control device determines that the driving of the circulation pump and the hydrogen generating unit has passed the predetermined time 201033133, the control unit only stops the circulating pump and the hydrogen generating drive for a predetermined time, and further controls the device. It is judged that the cycle of α. Na is difficult and the stop of the hydrogen generation unit has been ',', although the control time has passed, the control device has a method of generating m, no device, and then starts the circulation pump and hydrogen gas in this way. (3) The electrolytic water purification device of the invention is made to start and stop the driving of the reverse cycle pumping and gas generating unit, and the electrolytic water purifying device of the third invention can not only maintain the amount of dissolved gas in the treated water at a certain amount. And it can also save electricity. According to the invention of claim 4, in the second or third invention t, the hydrogen generating unit is connected to an oxygen-to-pass passage, and the oxygen is circulated to generate oxygen in the hydrogen gas. The electrolysis of water I is circulated, and the front end of the oxygen flow path is an oxygen discharge port for discharging oxygen absorbed by the user. ^ 4 (4) n water cutting device, the oxygen generated by electrolysis of pure water will be released from the gas circulation passage and released from the gas. Therefore, according to this, the oxygen emitted by the discharge port can be inhaled into the body, and the oxygen generated by the electrolysis can be effectively utilized. According to a fourth aspect of the invention, in the fourth aspect of the invention, a fan that sends the oxygen gas to the middle of the oxygen flow path is provided. The fan is connected to the control unit, and the control unit is connected to the oxygen release opening, and when the driving of the circulating fruit gas generating unit is stopped, when the control unit determines that the oxygen release switch is ON: θ β & The fan and circulation pump and hydrogen generating unit will start driving 7 201033133. When the control device determines that the oxygen release switch is ON, the fan and the secret gas and hydrogen generation unit will be used when the control device determines that the oxygen release switch is turned off. Will start driving. Therefore, by starting to drive the hydrogen generating unit and the circulation pump in the above manner, not only argon gas can be generated, but also the amount of dissolved hydrogen in the treated water storage tank can be forcibly increased, and by initiating driving of the fan, the inflowing oxygen flow can be specified (4) Released from the gas outlet. Therefore, in the electrolytic water purifying device of (4); =, even when the driving of the circulation pump and the gas generating portion is stopped, when the user has the necessity of taking in oxygen, the switch can be turned ON at any time. Draw oxygen. In the invention of claim i (the invention described in the claim!), the hydrogen gas generated by the hydrogen generation P is dissolved in the water taken out from the treated water reservoir by the circulating chestnut edge. Path (4) is in the treatment of water error: I can therefore increase the amount of dissolved hydrogen in the treated water slowly, the user can maintain in the state of dissolved = saturated state (4), and can maintain without reducing the amount of water in the drinking water In a certain range. In the S 2 invention (the invention described in the claim 2), since the bubbles of hydrogen gas are made fine by miniaturization, the amount of dissolved hydrogen in the treated water can be kept within a predetermined range. The amount of cold hydrogen in water, and in the third invention (the dragon is to repeat the circulation pump and hydrogen generation, since the control always drives the circulation pump and the hydrogen generating unit instead of the sub-item. Therefore, not only the treatment 201033133 can be processed. The amount of the cold hydrogen is kept at a certain amount, and the power can be saved. In addition, in the fourth invention (the electrolysis described in the claim 4 is performed, and the hydrogen gas is released from the oxygen in the pure water passage) The oxygen outlet is the center of the == Therefore, the user can put oxygen from the oxygen. In the invention, the invention produced by the electrolysis (the invention described in claim 5) can be effectively utilized in the cycle e, the part When the drive is stopped, when the control device determines that the oxygen release switch is ON, the 'fan and the circulation pump and the hydrogen start to drive, and by starting the driving of the gas generation in the above manner::: 杲, not only can the money be generated, Let the county dissolve (4) The system is increased, and by starting to drive the fan, the gas flowing into the oxygen flow path can be released from the oxygen discharge port at a predetermined pressure. Therefore, the electrolytic water purification device according to the invention is even in circulation. When the driving of the gas generating portion is stopped, when the user has the necessity of taking in oxygen, the oxygen can be taken up by turning the switch ON at any time. w [Embodiment] The following is a reference to the drawing. The electrolytic water purification device for carrying out the embodiment of the present invention will be described in detail. The water purification device of the embodiment of the electrolytic water purification device of the present embodiment is formed into a rectangular parallelepiped frame as shown in FIG. In the body 2, a cold water storage tank 22 (the treated water storage tank of the present invention), a warm water storage tank 23, a pressure pump 15, and the like, which will be described later, are housed. Further, the front side of the casing 2 is slightly above the upper side, 9 201033133 The recessed portion 2a is formed in the recessed portion 2a, and is provided with a water outlet 3 for cold water (the water outlet portion of the present invention) and a water outlet 4 for warm water which is arranged in parallel with the outlet 3 for cold water. Supply In the portion of the cold water storage tank (constituting the treated water storage tank of the present invention) 22, the warm water outlet 4' is a portion for supplying drinking water in the warm water storage tank 23 to be described later. The cold water switch operation lever 5 constituting the on-off valve is provided behind the water outlet 3, and the warm water switch operation lever 6 constituting the on-off valve is provided behind the warm water outlet 4. The cold water switch operating lever 5 and the warm water switch operating lever 6 are all connected to an on-off valve (not shown), and are elastically pressed in a front direction (off direction) by an elastic material (not shown). The container such as the cup (or by the user's finger) is pressed rearward by the user, whereby cold water or warm water can be supplied from the cold water outlet 3 and the warm water outlet 4. Further, below the cold water outlet 3 and the warm water outlet 4 in the recess 2a, a support plate 2f () for carrying a cup (not shown) is provided on the support plate 2f, and the cold water is formed. The through hole 2g through which the cold water or the warm water supplied from the water outlet 4 and the warm water outlet 4 can pass is connected to one end of the drain pipe (not shown) below the through hole 2g, and the drain is used for the drain. The other end of the tube is connected to a drain tank (not shown). Further, in the right side plate 2d of the casing 2 shown in Fig. 2, an oxygen suction pipe 7 for sucking oxygen is provided, and the oxygen suction pipe 7 is connected to an electrolysis device 32 (hydrogen generating portion of the present invention) to be described later. The oxygen discharge d 39d is further provided with an upper front panel 上方 above the recess 2a, and the upper front panel 2b is provided with a circular display panel 8 and is provided on the display 10 201033133

不面板8之下方的操作面板9。此等中,於圖2(a)所示之一 方的顯示面板8上方中央,設置有連接於圖4所示之控制 裝置20的電源工作燈8A,於電解式淨水裝置】之電源為 ON的狀態時,係呈綠色之亮燈,而於〇ff之狀態時,則不 亮燈。於此電源工作燈8A之下方左側,設置有連接於控制 裝置20之溫水狀態顯示燈8B,在後述之溫水儲槽23内的 水溫被加熱至規定溫度之狀態時,係呈紅色之亮燈,而在 常溫之狀態冑,則不亮燈。χ,於上述電源工錢8a之下 方右側,設置有連接於控制裝置2〇之冷水狀態顯示燈8C, 在後述之冷水儲槽22内的水溫被冷卻至規定溫度之狀態 時,係呈藍色之亮燈,而在常溫之狀態時,則不亮燈。 又,於上述溫水狀態顯示燈8B之下方,設置有連接於 控制裝置2G之氫、氧生成中燈8D,藉由後述之電解裝置 32之工作,在氫氣及氧氣生成中時係呈藍色之亮燈。又, 於上述冷水狀態顯示燈8C之下方,設置有連接於控制裝置 之氫、氧休止中燈8E,後述之電解裝置以停止工作使 氫氣及氧氣之生成休止中時,係呈橙色之亮燈。又,於此 等氫、氧生成中燈8D及氫、氧休止中燈8E2下方中央部, 設置有連接於控制裝置2〇之過濾器交換警告燈8卜此過濾 器交換警告燈8F,會藉由連接於控制裝置2Q之過濾器交換 定時器9G到達設定時間的工作訊號,而亮燈為用以警主後 述沉澱物過濾器12及碳過據器13(本發明之淨水處理部)之 交換時期的紅色’平常則不亮燈。另,上述過濾器交換定 時器9G之設定時間,為了維持自來水之淨水性係設定為 11 201033133 約4400小時(約6個月)。 又,於圖2(b)所示之另一方的操作面板9左端。設置 有連接於圖4所示之控制裝置2〇且顯示為Γ〇χΙ」的氧放 出開關9Α ^此氧放出開關9Α,於該氧放出開關9Α未亮燈 且上述氫、氧休止中燈8Ε亮燈中,在後述之電解裝置32 未生成氧氣之休止中的任意時期,可藉由手動按壓,使該 氧放出開關9Α之ON、OFF顯示部亮燈,且該電解裝置32 開始工作而可從上述氧吸取管7吸取氧氣。又,於此氧放 出開關9A之右側’設置有連接於控制裝置2〇且顯示為 「HOT」的溫水溫度開關9B。此溫水溫度開關9B,於該溫 水溫度開關9B及上述溫水狀態顯示燈8B亮燈中,在後述 之溫水儲槽23内之水溫已加熱至規定溫度之狀態(溫水之 狀態)的任意時期,可藉由手動按壓,使該溫水溫度開關9b 之ON、OFF顯示部暗燈’且後述之加熱器27停止工作, 而成為上述溫水儲槽23内之水溫不被加熱至規定溫度的狀 態(常溫之狀態)。 又’於上述溫水溫度開關9B之右側,設置有連接於控 制裝置20之光照度感測器9C。此光照度感測器9c,可感 測室内之照度來設定照度’當達到設定照度時,輸出亮訊 號,當未達到設定照度時,則輸出暗訊號,例如,者 爾至 達到設定照度之亮度時’輸出亮訊號使電解式淨水裝置^ 開始工作,維持自動運轉,且當較設定照度小時,則輸出 暗訊號,停止電解式淨水裝置i之自動運轉,維持休^狀 態。 12 201033133 又,於上述光照度感測器9C之右側,設置有連接於控 制裝置20且顯示為「COLD」的冷水溫度開關9d。此冷水 溫度開關9D ’於該冷水溫度開關9D及上述冷水狀態顯示 燈8C亮燈中’在後述之冷水储槽22内之水溫已冷卻至規 疋溫度之狀態(冷水之狀態)的任意時期,可藉由手動按壓, 使該冷水溫度開關9D之ON、OFF顯示部暗燈,且後述之 冷卻器24停止工作,而成為上述冷水儲槽22内之水溫不 被維持在規定溫度的狀態(常溫之狀態)。又,於上述冷水溫 〇 度開關9D之右側,設置有連接於控制裝置2〇且顯示為 「RESET」的定時器重設開關9E ^此定時器重設開關9E, 為了根據上述過濾器交換警告燈8F之亮燈的警告,於交換 後述之沉澱物過濾器12及碳過濾器13後,使上述過濾器 交換定時器9G開始工作,可藉由按壓上述定時器重設開關 9E ’使該定時器重設開關9E之ON、OFF顯示部亮燈,且 將計數時間重設為零(〇” _ 又,於上述凹部2a之下方,安裝有可裝卸自如的下正 面面板2c,於此下正面面板2c之後方(上述框體2内),收 納有後述之冷水儲槽22、溫水儲槽23、排水用儲槽(省略圖 示)等。包含此等之構成,以下,一邊參照圖3所示之示意 圖,一邊說明此實施形態之電解式淨水裝置1。 此電解式淨水裝置1,係透過配管(省略符號^ )及止水 閥Π連接於公共之上水道’此配管則連接有沉澱物過濾器 12。此沉澱物過濾器12,藉由未圖示之5〜6私m之孔,將 上水道所供給之水中的銹及砂子、塵埃等之微細雜質加以 13 201033133 去除。於此沉澱物過濾器12,連接有碳過濾器13,藉由此 碳過濾器13之未圖示之活性碳的吸附作用,可吸附經由上 述沉澱物過濾器12之水中的氣化合物及少量的色素、惡臭 氣體等。又,於此碳過濾器13,透過電磁閥14連接有加壓 泵15,可將上水道所供給之水加壓傳送至下流側。此等電 磁間14及加壓果15 ’係連接於圖4所示之控制裝置20, 可藉由後述之預備儲槽18内之浮控開關21之工作加以驅 動或停止。 又,於圖3所示之上述加壓泵15,連接有逆滲透膜過 濾器16(本發明之純水生成部),此逆滲透膜過濾器16,藉 由具有Ο.ΟΟΟΙβχη(約頭髮的1〇()萬分之丨)之未圖示的微孔 的半透膜,可得到自上述加壓泵15所加壓傳送之水去除約 95 %之重金屬、各種細菌及有機化合物等雜質的純水且 無法穿過含有雜質之水則從連接於下部之排水用管(省略符 號。)排出至外部。又,於此逆滲透膜過濾器16,連接有一 方之礦石過戚器17,且透過另一方之分支接頭(省略符號。) 連接有離子交換樹脂過濾器31。 此等之中,於一方之礦石過濾器17,積層有未圖示之 天然礦石之醫王石、長石、電氣石等,藉由使純水通過該 方之礦石過濾器17,以使礦物質成分溶解於該純水◦於 此礦石過濾器17,進一步連接有預備儲槽18,於此預備儲 槽18内,儲存有來自上述礦石過濾器17之水。又,於此 預備儲槽18,内設有用以將所儲存之水維持在規定量的浮 控開關21,且於該預備儲槽18之下部,分別連接有冷水儲 201033133 槽22與溫水儲槽23。上述浮控開關2丨,係由密閉成中空 狀且可在水面上浮動的浮動體21a、用以支持此浮動體21& 之呈L字形的支持體21b、及藉由上述浮動體2U之上下動 作而透過上述支持體21b進行電氣上〇N/〇FF工作的微動開 關21c所構成。另,用以將本發明之純水供給至處理水儲槽 的供給通路,係由上述礦石過濾器17及預備儲槽Η所構 成。 因此,若上述預備儲槽18内之儲存水量僅減少一定量 時,則上述浮動體21a之前端侧將會下降,藉由此下降,透 過上述支持體21b,使圖4所示之連接於控制裝置2〇的微 動開關2lc的通電變成〇N,而打開上述電磁閥14且驅動 加壓泵I5將通過碌石過濾器17之水補充於預備儲_ 18 内。又’若上述預備儲槽18内之儲存水量達到:定:槽時18 則上述微動開關21。之通電將會變成⑽,而關閉上述電磁 閥14且停止加壓泵15,使通過上述礦石過濾器η之水不 再補充於預備健槽18内。 、又’於上述預備儲槽18之下方,透過各管體(省略符號。) 連接有冷水儲槽22及溫水儲槽23。於上述冷水儲槽, 安裝有用以冷卻所儲存之水的冷卻器24,且為了將所儲存 之冷=的溫度維持在規定溫度,用以進行溫度檢測之冷水 用怪溫器25 ’係安裝成將溫度檢測部25a設置在水中。此 等之中,冷部器24及冷水用恆溫器25,係連接於圖4所示 之控制裝置2〇 ’當冷水儲槽22内之水溫上升至規定的溫度 、上時藉由使上述冷水用恆溫器25之通電變成〇N, 15 201033133 驅動冷卻器24來冷卻上述儲存水之水溫。相對於此,當水 溫下降至規定的溫度時,則藉由使上述冷水用恆溫器25之 通電變成OFF,以停止冷卻器24之驅動。又,於上述冷水 儲槽22,連接有前端作為可供給冷水之上述冷水用出水口 3的管體(省略符號。)。因此,若將上述冷水用開關操作桿 5向後方操作,則儲存於上述冷水儲槽22内之冷水,將會 因本身的重量而自上述冷水用出水口 3流出,而根據此出 水量,儲存於上述預備儲槽18之水則藉由落差(本身的重量) 補充於冷水儲槽22。 Θ 又,於上述溫水儲槽23,安裝有用以對所儲存之水進 行加熱之加熱器27,且為了將儲存在該溫水儲槽23之溫水 的溫度維持在規定溫度,用以進行溫度檢測之溫水用恆溫 器28 ’係安裝成將溫度檢測部28a設置在水中。此等之中, 加熱器27及溫水用恆溫器28,係連接於圖4所示之控制裝 置20,當溫水儲槽23内之水溫下降至規定之溫度以下時, 藉由使上述溫水用恆溫器28之通電變成〇N,以使加熱器 27工作,來加熱上述儲存水之水溫。相對於此當水溫上 升至規疋之溫度時,則藉由使上述溫水用恆溫器28之通電 變成OFF,以停止加熱器27之工作。又於上述溫水儲槽 23 ’連接有前端作為上述溫水用出水口 4之管體(省略符 號)又’對此溫水儲槽23進行水之補充,若自上述溫水 用出水口 4供給溫水,則儲存於上述預備儲槽18之水將會 透過e雜’藉由落差(本身的重量)而補充於該溫水儲槽23。 又’自上述逆滲透膜過濾器16分支連接之另一方的離 16 201033133 子交換樹脂過濾器31’藉由離子交換樹脂之離子交換作 用,將自上述逆滲透膜過濾器16所加壓傳送之純水中的齊 及一氧化碳等、用以殺菌而存在水中之殘留氣加以去除, 而生成超純水。於此離子交換樹脂過濾器31,連接有用以 對自該離子交換樹脂過濾器31所加壓傳送之超純水進行電The operation panel 9 below the panel 8 is not provided. In this case, a power supply lamp 8A connected to the control device 20 shown in FIG. 4 is provided at the center of the upper display panel 8 shown in FIG. 2(a), and the power supply of the electrolytic water purification device is ON. In the state of the state, it lights up in green, while in the state of 〇ff, it does not light. The warm water state indicator lamp 8B connected to the control device 20 is provided on the left side of the power supply lamp 8A, and is red when the water temperature in the warm water storage tank 23 to be described later is heated to a predetermined temperature. Lights up, and when it is in a normal temperature state, it does not light. In the lower side of the power supply 8a, the cold water state indicator lamp 8C connected to the control device 2 is provided, and when the water temperature in the cold water storage tank 22 to be described later is cooled to a predetermined temperature, it is blue. It lights up, but when it is in normal temperature, it does not light. Further, below the warm water state indicator lamp 8B, a hydrogen and oxygen generating lamp 8D connected to the control device 2G is provided, and the operation of the electrolysis device 32, which will be described later, is blue in the generation of hydrogen gas and oxygen gas. Lights up. Further, below the cold water state indicator lamp 8C, a hydrogen/oxygen suspension lamp 8E connected to the control device is provided, and when the electrolysis device described later stops operating to stop the generation of hydrogen gas and oxygen gas, it is illuminated in orange. . Further, in the central portion below the hydrogen and oxygen generating middle lamp 8D and the hydrogen and oxygen rest light 8E2, a filter exchange warning lamp 8 connected to the control device 2 is provided, and the filter exchange warning lamp 8F is used. The operation signal of the set time is reached by the filter exchange timer 9G connected to the control device 2Q, and is illuminated by the precipitator filter 12 and the carbon filter 13 (the purified water treatment unit of the present invention). The red color of the exchange period does not normally light up. Further, the set time of the filter exchange timer 9G is set to 11 201033133 for about 4400 hours (about 6 months) in order to maintain the clean water content of the tap water. Moreover, it is the left end of the other operation panel 9 shown in FIG. 2(b). An oxygen release switch 9 is connected to the control device 2 shown in FIG. 4 and is shown as "Γ〇χΙ", and the oxygen release switch 9 is not lit, and the hydrogen and oxygen are stopped. In the lighting, at any time during which the electrolysis device 32 does not generate oxygen, the ON/OFF display portion of the oxygen release switch 9A can be turned on by manual pressing, and the electrolysis device 32 can be operated. Oxygen is taken up from the oxygen suction pipe 7 described above. Further, on the right side of the oxygen discharge switch 9A, a warm water temperature switch 9B connected to the control device 2 and displayed as "HOT" is provided. In the warm water temperature switch 9B, the warm water temperature switch 9B and the warm water state indicator lamp 8B are turned on, and the water temperature in the warm water storage tank 23 to be described later is heated to a predetermined temperature (the state of warm water) At any time, the temperature of the warm water temperature switch 9b can be turned on and the display portion of the warm water temperature switch 9b can be turned on, and the heater 27, which will be described later, is stopped, and the water temperature in the warm water storage tank 23 is not The state of heating to a predetermined temperature (state at normal temperature). Further, on the right side of the warm water temperature switch 9B, an illuminance sensor 9C connected to the control device 20 is provided. The illuminance sensor 9c can sense the illuminance in the room to set the illuminance. When the illuminance is reached, the bright signal is output. When the illuminance is not reached, the dark signal is output, for example, when the brightness of the set illuminance is reached. 'The output light signal enables the electrolytic water purification device to start working, maintains automatic operation, and when the set illumination is small, the dark signal is output, and the automatic operation of the electrolytic water purification device i is stopped, and the state of rest is maintained. 12 201033133 Further, on the right side of the illuminance sensor 9C, a cold water temperature switch 9d connected to the control device 20 and displayed as "COLD" is provided. In the cold water temperature switch 9D and the cold water state indicator lamp 8C, the water temperature in the cold water storage tank 22 to be described later is cooled to the temperature (the state of the cold water) at any time. By the manual pressing, the cold water temperature switch 9D is turned ON and the OFF display portion is turned on, and the cooler 24 described later is stopped, and the water temperature in the cold water storage tank 22 is not maintained at a predetermined temperature. (State of normal temperature). Further, on the right side of the cold water temperature switch 9D, a timer reset switch 9E connected to the control device 2 and displayed as "RESET" is provided. This timer reset switch 9E, in order to exchange the warning lamp 8F according to the above filter. The warning of the lighting, after exchanging the sediment filter 12 and the carbon filter 13, which will be described later, causes the filter exchange timer 9G to start operating, and the timer reset switch 9E' can be reset by pressing the timer reset switch 9E' The ON and OFF display portions of 9E are turned on, and the count time is reset to zero (〇" _. Further, a detachable lower front panel 2c is attached below the recess 2a, and the lower front panel 2c is attached thereto. (in the above-mentioned housing 2), a cold water storage tank 22, a warm water storage tank 23, a drainage storage tank (not shown), and the like, which will be described later, are housed, and the like, and the following is shown in FIG. The electrolytic water purification device 1 of the embodiment will be described. The electrolytic water purification device 1 is connected to a common upper water channel through a pipe (not shown) and a water stop valve ', and the pipe is connected with a sediment filter. 12. The sediment filter 12 removes rust, sand, dust, and the like from the water supplied from the sewer by 13 201033133 by a hole of 5 to 6 cm, not shown. 12, the carbon filter 13 is connected, and by the adsorption of activated carbon (not shown) of the carbon filter 13, the gas compound in the water passing through the sediment filter 12, a small amount of a coloring matter, a malodorous gas, or the like can be adsorbed. Further, in the carbon filter 13, a pressure pump 15 is connected to the electromagnetic valve 14, and the water supplied from the sewer can be pressurized and transported to the downstream side. The electromagnetic chamber 14 and the pressurized fruit 15' are connected to FIG. The control device 20 shown can be driven or stopped by the operation of the float switch 21 in the preliminary storage tank 18, which will be described later. Further, the pressure pump 15 shown in Fig. 3 is connected with a reverse osmosis membrane filter. 16 (pure water generating unit according to the present invention), the reverse osmosis membrane filter 16 is provided with a semipermeable membrane having micropores (not shown) of Ο.ΟΟΟΙβχη (about 1 〇 of the hair) The water sent from the pressure pump 15 is pressurized to remove about 95% of the gold Pure water of impurities such as bacteria and organic compounds, and water that does not pass through the impurities, is discharged to the outside from the drain pipe (not shown) attached to the lower portion. Further, the reverse osmosis membrane filter 16 is connected to the reverse osmosis membrane filter 16 One or more of the ore filter 17 is connected to the other side of the branch joint (the symbol is omitted). The ion exchange resin filter 31 is connected. Among them, one of the ore filters 17 is laminated with a natural ore (not shown). The medicinal stone, the feldspar, the tourmaline, etc., by passing the pure water through the ore filter 17 of the side, so that the mineral component is dissolved in the pure water ◦ in the ore filter 17, further connected with the preliminary storage tank 18, In the preliminary storage tank 18, water from the above-described ore filter 17 is stored. Further, the preliminary storage tank 18 is provided with a float switch 21 for maintaining the stored water at a predetermined amount, and a cold water reservoir 201033133 slot 22 and a warm water reservoir are respectively connected to the lower portion of the preliminary storage tank 18. Slot 23. The floating control switch 2 is a floating body 21a that is sealed in a hollow shape and floats on the water surface, an L-shaped support body 21b for supporting the floating body 21& and the upper and lower sides of the floating body 2U The operation is performed by the micro-switch 21c that electrically operates the N/〇FF operation through the support 21b. Further, the supply passage for supplying the pure water of the present invention to the treated water storage tank is constituted by the above-described ore filter 17 and the preliminary storage tank. Therefore, if the amount of stored water in the preliminary storage tank 18 is reduced by only a certain amount, the front end side of the floating body 21a will be lowered, thereby being lowered, and the support body 21b is transmitted to connect the control shown in FIG. The energization of the micro switch 2lc of the device 2 turns into 〇N, and the above-described solenoid valve 14 is opened and the pressure pump I5 is driven to replenish the water passing through the stone filter 17 into the reserve -18. Further, if the amount of stored water in the preliminary storage tank 18 is equal to: 18, the micro switch 21 is provided. The energization will become (10), and the solenoid valve 14 is closed and the pressurizing pump 15 is stopped so that the water passing through the ore filter η is no longer replenished in the preliminary tank 18. Further, below the preliminary storage tank 18, a cold water storage tank 22 and a warm water storage tank 23 are connected to each other through a pipe body (the symbol is omitted). In the cold water storage tank, a cooler 24 for cooling the stored water is installed, and in order to maintain the stored cold=temperature at a predetermined temperature, the cold water mister 25' for installing the temperature is installed. The temperature detecting portion 25a is placed in the water. Among these, the cold unit 24 and the cold water thermostat 25 are connected to the control unit 2 shown in FIG. 4 when the water temperature in the cold water storage tank 22 rises to a predetermined temperature or higher. The energization of the cold water thermostat 25 becomes 〇N, 15 201033133 drives the cooler 24 to cool the water temperature of the above stored water. On the other hand, when the water temperature drops to a predetermined temperature, the cooling of the cooler 24 is stopped by turning off the energization of the cold water thermostat 25. Further, a pipe body (not shown) is attached to the cold water storage tank 22 as a water outlet 3 for supplying cold water to which cold water can be supplied. Therefore, when the cold water switch operating lever 5 is operated backward, the cold water stored in the cold water storage tank 22 will flow out from the cold water outlet 3 due to its own weight, and will be stored according to the water discharge amount. The water in the preliminary storage tank 18 is replenished to the cold water storage tank 22 by the drop (the weight of itself). Further, in the warm water storage tank 23, a heater 27 for heating the stored water is installed, and in order to maintain the temperature of the warm water stored in the warm water storage tank 23 at a predetermined temperature, The warm water thermostat 28' for temperature detection is installed to set the temperature detecting portion 28a in the water. In the above, the heater 27 and the warm water thermostat 28 are connected to the control device 20 shown in FIG. 4, and when the temperature of the water in the warm water storage tank 23 falls below a predetermined temperature, The warm water thermostat 28 is energized to become 〇N to operate the heater 27 to heat the water temperature of the stored water. On the other hand, when the water temperature rises to the temperature of the gauge, the operation of the heater 27 is stopped by turning off the energization of the warm water thermostat 28. Further, in the warm water storage tank 23', a front end is connected as a pipe body (not shown) for the warm water outlet 4, and a water supply is added to the warm water storage tank 23, and the water outlet 4 is used for the warm water. When warm water is supplied, the water stored in the preliminary storage tank 18 will be replenished to the warm water storage tank 23 by the drop (the weight of itself). Further, from the other side of the reverse osmosis membrane filter 16 branched, the 16 201033133 sub-exchange resin filter 31' is pressurized and transported from the reverse osmosis membrane filter 16 by ion exchange of an ion exchange resin. Pure water and carbon monoxide, etc., are used to sterilize residual gases in water to be removed, thereby producing ultrapure water. The ion exchange resin filter 31 is connected to electrically pump ultrapure water pressurized by the ion exchange resin filter 31.

解,以生成氫氣與氧氣的電解裝置(本發明之氫氣生成 部)32。此電解裝置32’如圖5及圖6所示,係由可收納水 的外側容器33、形成間隙設置在此外側容器33之内侧上部 且可將水收納於内側的内侧容器34、固定於此等外侧容器 33及内側容器34之上端的容器蓋35、固定於此容器蓋35 之上面的支持蓋37、及固定於此支持蓋37之氫氣用導管 38及氧氣用導管39所構成之構造體。 此等之中,上述外側容器33,如圖6所示,於下方側 形成有可儲存水(電解液)的胴部33a,於此胴部33a之下 方,形成有用以將所儲存之水加以排出的排出口 33b。於此 排出口 33b叹置有可藉由手動來進行開關的開關閥4【(參 …、圖3)此開關閥41之排水,係用以去除電解裝置^内 因後述之電解所析出之水垢等的排水,由於係將上述逆渗 透膜過濾、器16及離子交換過據器31所過據之純水供給至 此電解裝置32内,因此水垢等之蓄積較少約丨年進行丄 久左右之排水。又,於卜 於上述外側容器33,在與上述胴部33a 鄰接的上方’形成右g 呈V子形傾斜擴寬之擴寬部33d,而在 與此擴寬部33d鄰接夕^如 味 _ 上0P,形成有直立之直立部33f,此 4之圖5所示之左右太 向之側部,係由未圖示之側板密封, 17 201033133 且上述直立部33f之上部,係固定於上述容器蓋35。 又,上述内側容器34,於下端形成有可流通水的流通 口 34a,自此流通口 34a於上方形成有呈乂字形傾斜擴寬之 擴寬部34b,在與此擴寬部34b鄰接之上部,形成有直立之 直立部34c,此直立部34c之上部,係固定於上述容器蓋35。 又,於上述外側容器33之擴寬部33(1及直立部33f、與上 述内側容器34之擴寬部341)及直立部34c之間,形成有後The electrolytic device (hydrogen generating portion of the present invention) 32 for generating hydrogen gas and oxygen gas is obtained. As shown in FIGS. 5 and 6, the electrolysis device 32' is fixed to the outer container 33 that can store water, and the inner container 34 that is provided on the inner upper portion of the outer container 33 and that can accommodate water inside. The container cover 35 at the upper end of the outer container 33 and the inner container 34, the support cover 37 fixed to the upper surface of the container cover 35, and the structure of the hydrogen conduit 38 and the oxygen conduit 39 fixed to the support cover 37 . In the above-described outer container 33, as shown in Fig. 6, a crotch portion 33a capable of storing water (electrolyte) is formed on the lower side, and a lower portion of the crotch portion 33a is formed to serve the stored water. The discharge port 33b is discharged. The discharge port 33b is provided with an on-off valve 4 that can be manually opened and closed. [(..., FIG. 3) The drainage of the on-off valve 41 is used to remove the scale deposited in the electrolysis device by electrolysis described later. Since the drainage water is supplied to the electrolysis device 32 by the reverse osmosis membrane filter, the pure water supplied by the reverse osmosis membrane filter, and the ion exchange reactor 31, the accumulation of scale and the like is less than about a year. . Further, in the outer container 33, a widened portion 33d whose right g is V-shaped obliquely widened is formed on the upper side adjacent to the crotch portion 33a, and is adjacent to the widened portion 33d. Upper 0P is formed with an upright upright portion 33f, and the left and right side portions shown in FIG. 5 of FIG. 4 are sealed by a side plate (not shown), 17 201033133 and the upper portion of the upright portion 33f is fixed to the container. Cover 35. Further, the inner container 34 is formed with a flow port 34a through which water can flow at the lower end, and a widened portion 34b which is obliquely widened in a U shape is formed above the flow port 34a, and the widened portion 34b is adjacent to the upper portion. An upright portion 34c is formed, and the upper portion of the upright portion 34c is fixed to the container lid 35. Further, between the widened portion 33 (1, the upright portion 33f, the widened portion 341 of the inner container 34) and the upright portion 34c of the outer container 33, a rear portion is formed.

述之可流通氫氣的氫氣流路43、與後述之可流通氧氣的氧 氣流路44。The hydrogen gas flow path 43 through which hydrogen gas can flow is described, and the oxygen gas flow path 44 through which oxygen can flow, which will be described later.

又,上述氫氣用導管38,於下端形成有可讓來自上域 氫氣流路43之氫氣流通的開口(省略符號。),在與此開口 鄰接之上方,形成有直立之下側直立部38a,在與此下側直 立。P 38a鄰接之上方,形成有縮寬之縮寬部_,而在與此 縮寬部撕鄰接之上方,則形成有直立之氫氣排出部38ce 於此氫氣排出部38c之上端’形成有開口成可排出氫氣之負 氣排出口 38d,此氫氣排出口 38d,係藉由配管構件56,達 接於圖3所示之碳空氣過渡器57。又,上述縮寬部勘, 如圖5所示’係形成為自左右向中央變高之山形,在此山 形之頂部,形成有上述氫氣排出部38e,因此可將後述之陰 極電解板51所生成的氫氣有效地集中於該氫氣排出部π。 又,上述氧氣用導管39,於下端形成有可讓來自上对 ::流路44之氧氣流通的開口 (省略符號。),在與此開。 鄰接之上方’形成有直立之下側直39 立部39a鄰接之卜古加 仗興此下側j 之上方,形成有縮寬之縮寬部39b,而 18 201033133 :寬部地鄰接之上方,則形成有直立 Z氧氣排出部39c之上端,形成有開口成可排出出氧^氧 氣排出口州,此氧氣排出口 39d,係藉由 Π ::圓3所示之氧送以風扇又,上述缩寬部1連Further, the hydrogen gas conduit 38 has an opening (not shown) for allowing hydrogen gas from the upper hydrogen gas flow path 43 to flow at the lower end, and an upright lower standing portion 38a is formed above the opening. Stand upright with this lower side. A converging portion _ is formed above the adjacent portion of the P 38a, and an upright hydrogen discharge portion 38ce is formed above the tear portion adjacent to the constricted portion. The upper end of the hydrogen discharge portion 38c is formed with an opening. The negative gas discharge port 38d of the hydrogen gas can be discharged, and the hydrogen discharge port 38d is connected to the carbon air transition unit 57 shown in Fig. 3 by the pipe member 56. Further, as shown in Fig. 5, the narrowed portion is formed in a mountain shape which is raised from the center to the center, and the hydrogen gas discharge portion 38e is formed at the top of the mountain shape. Therefore, the cathode electrolytic plate 51 to be described later can be used. The generated hydrogen gas is efficiently concentrated on the hydrogen gas discharge portion π. Further, the oxygen conduit 39 has an opening (not shown) for allowing oxygen to flow from the upper pair :: flow path 44 at the lower end, and is opened therewith. The upper side of the adjoining portion is formed with a slanted lower side straight 39 apex 39a adjacent to the upper side of the lower side j, and a narrowed portion 39b is formed, and 18 201033133: a wide portion is adjacent to the upper side, Forming an upper end of the upright Z oxygen discharge portion 39c, an opening is formed to discharge the oxygen and oxygen outlet port state, and the oxygen discharge port 39d is sent to the fan by the oxygen indicated by Π::3, Shrinking unit 1

雖爷略圖示,但與上述氫氣用導管38之縮寬部地相同, 係形成為自左右向中央變高之山形,在此山形之頂部形 成有上述氧氣排出部39c,因此可將後述之陽極電解板μ 所生成的氧氣有效地集中於該氧氣排出部39c。 —又,於上述電解裝置32,如圖5及圖6所示,於上述 容器蓋35固定有供水接頭46,於此供水接頭钧,形成有 用以供給來自上述離子交換樹脂過濾器3丨之超純水的供水 孔46c。於此供水接頭46之上端側,成形有用以將與上述 離子交換樹脂過濾器3 1之排出口連接之管(省略符號)加以 固定的管固定部46a,於此管固定部46a之下方,一體成形 有用以安裝後述之浮控閥體47的閥體安裝部46b »於此閥 體安裝部46b,形成有直徑大於上述供水孔46c的排出孔 46d ’於此排出孔46d之上端,形成有向上述供水孔46c縮 徑之具有錐面的錐孔46f,且上述閥體安裝部46b之一部 分,形成有浮控閥體47之後述之支持體47c可旋動的凹口 (省略符號)。 又’於上述電解裝置32,在上述供水接頭46之閥體安 裝部46b,安裝有用以使上述供水孔46c所供給之超純水維 持在規定之水量的浮控閥體47。此浮控閥體47,用以在上 述超純水達到規定量時阻止該超純水之流入,係由密閉成 19 201033133 中空狀且可在水面上浮動的浮動體47a、閥棒47b、及用以 支持此等浮動體47a及閥棒47b之呈L字形的支持體47c 所構成。此支持體47c ’ 一端側固定有浮動體47a,另一端 侧則藉由插銷47d而可旋動地支持於上述供水接頭46之闕 體安裝部46b。又,於上述支持體47c之另一端側,直立地 設置有閥棒47b,於此閥棒47b之上端,形成有具有藉由上 述支持體47c旋動於圖5所示之反時計方向而可與上述錐孔 46f密合之錐面的錐形凸部47f。 又’上述浮控閥體47,若儲存於上述電解裝置32内之 超純水的水面僅減少一定量時,則上述浮動體47a之前端側 將會下降,藉由此下降透過上述支持體47c,使上述閥棒47b 之錐形凸部47f自上述供水接頭46之錐孔46f分離,形成 間隙,自此間隙將來自上述離子交換樹脂過濾器31之超純 水加壓傳送至内部。又,若上述電解裝置32内之超純水的 儲存水量増大時,則上述浮動體47a的前端側亦隨之上升, 在該儲存水量到達規定量時,透過上述支持體47c,使上述 閥棒47b之錐形凸# 47f密合於上述供水接頭46之錐孔 46f藉由此密合狀態,以阻止來自上述離子交換樹脂過遽 器31所加壓傳送之超純水的供給。 又於上述電解裝置32,在圖6所示之内側容器34之 胴部33a内,讯要士 α置有可藉由電解生成氫氣及氧氣的電解部 40。此電解部4〇,昤 陰極側電極棒48及陽極側電極接49係 以絕緣狀態相斜h m〜^ ' 疋於上述胴部33a,於一方之陰極侧電 極棒48,固定右类 方衣面(形成為板狀)施有鈦鉑鍍敷之陰極電 20 201033133 解板51,於另一方之陽極側電極棒49,則與上述陰極電解 板51面對地固定有表面(形成為板狀)施有鈦鉑鍍敷之陽極 電解板52。此等陰極電解板51及陽極電解板52,係設置 在上述内側容器34之流通口 34a的下方’在陰極電解板51 與陽極電解板52所面對的中央部,形成有間隙且設置有離 子交換臈53,藉由此離子交換膜53,將陰極電解板51與 陽極電解板52加以分離。又,在陰極電解板51及陽極電 解板52之周圍,設置有具有可自由流通純水之網目的網體 54。 又,於以上述方式所構成之電解裝置32,藉由分別通 電於圖6所示之陰極側電極棒48與陽極側電極棒49,對内 部所儲存之純水(電解液)進行電解,而於一方之陰極電解板 51側生成氫氣(HO。此氫氣將會經由氫氣流路杓,排出至 氫氣用導管38之氫氣排出口 38d,並透過與此氫氣排出口 連接之配管構件56(參照圖3),而送至_方之碳空氣過 _濾器^7。又,於另一方之陽極電解板52側生成有氧氣(〇2), 此氧氣將會經由氧氣流路44,排出至氧氣用導管39之氧氣 排出口 39d,並透過與此氧氣排出口 3^連接之配管構件 58 ’而送至另一方之氧送出用風扇59。 *此等之中,一方之碳空氣過濾器57,係藉由未圖示之 1粉末等之濾過將生成於上述電解裝i 32之氮氣中所 含之泡沫加以去除。在此碳空氣過濾器57,透過管體(省略 符號。)連接有循環泵62。此循環泵62,僅 I作時驅動,於該循環“2,設置有與上述== 21 201033133 ^ 57連接之氣體吸人口仏、及與一端連接於上述冷水儲 槽22之管體(省略符號。)的另一端連接之水吸入口咖, 該循環泵62驅動時,係藉由一方之氣體吸入口心,吸入 來自上述碳空氣過濾器57之氫氣,且藉由另-方之水吸入 口 62b,吸入來自上述冷水儲槽22内之水。 又,於上述循環泵62,藉由未圖示之泵機構, 以未加In the same manner as the widened portion of the hydrogen gas conduit 38, it is formed in a mountain shape which is increased from the right and left to the center, and the oxygen discharge portion 39c is formed at the top of the mountain shape, so that it can be described later. The oxygen generated by the anode electrolytic plate μ is effectively concentrated on the oxygen discharge portion 39c. Further, in the electrolysis device 32, as shown in Figs. 5 and 6, a water supply joint 46 is fixed to the container lid 35, and the water supply port is formed to supply the filter from the ion exchange resin filter. Water supply hole 46c of pure water. On the upper end side of the water supply joint 46, a pipe fixing portion 46a for fixing a pipe (not shown) connected to the discharge port of the ion exchange resin filter 31 is formed, and is integrated under the pipe fixing portion 46a. A valve body mounting portion 46b for mounting a float valve body 47 to be described later is formed. The valve body mounting portion 46b is formed with a discharge hole 46d' having a diameter larger than the water supply hole 46c, and an upper end of the discharge hole 46d is formed to form a direction. The water supply hole 46c has a taper hole 46f having a tapered surface, and a portion of the valve body mounting portion 46b is formed with a recess (not shown) in which the support body 47c, which will be described later, is floated by the float valve body 47. Further, in the electrolysis device 32, the valve body mounting portion 46b of the water supply joint 46 is provided with a float valve body 47 for maintaining the ultrapure water supplied from the water supply hole 46c at a predetermined amount of water. The floating control valve body 47 is configured to prevent the inflow of the ultrapure water when the ultrapure water reaches a predetermined amount, and is a floating body 47a, a valve rod 47b, and a floating body 47a that is hollow and can float on the water surface. The support body 47c for supporting the floating body 47a and the valve rod 47b in an L shape is formed. The support body 47c' has a floating body 47a fixed to one end side, and the other end side is rotatably supported by the body mounting portion 46b of the water supply joint 46 by a pin 47d. Further, on the other end side of the support body 47c, a valve rod 47b is provided upright, and the upper end of the valve rod 47b is formed to have a counterclockwise direction shown in Fig. 5 by the support body 47c. A tapered convex portion 47f of a tapered surface that is in close contact with the tapered hole 46f. Further, when the water surface of the ultrapure water stored in the electrolysis device 32 is reduced by a certain amount, the float valve body 47 is lowered, and the front end side of the floating body 47a is lowered, thereby being lowered through the support body 47c. The tapered convex portion 47f of the valve rod 47b is separated from the tapered hole 46f of the water supply joint 46 to form a gap, and the ultrapure water from the ion exchange resin filter 31 is pressurized and transported to the inside. Further, when the amount of stored water of the ultrapure water in the electrolysis device 32 is large, the front end side of the floating body 47a also rises, and when the amount of stored water reaches a predetermined amount, the valve body is passed through the support body 47c. The tapered projection 47 of the 47b is in close contact with the tapered hole 46f of the water supply joint 46 by the close contact state to prevent the supply of the ultrapure water pressurized by the ion exchange resin filter 31. Further, in the above-described electrolysis device 32, in the crotch portion 33a of the inner container 34 shown in Fig. 6, the electro-acoustic portion 40 is provided with an electrolysis portion 40 which can generate hydrogen gas and oxygen by electrolysis. In the electrolysis unit 4, the cathode side electrode rod 48 and the anode side electrode connection 49 are insulated from each other in the insulating state, and the cathode side electrode rod 48 is fixed to the cathode side electrode rod 48. (formed in a plate shape) a cathode electric power 20 201033133 plated with titanium platinum plating, and an anode side electrode rod 49 on the other side, a surface (formed in a plate shape) is fixed to the surface of the cathode electrolytic plate 51 An anodic electrolytic plate 52 coated with titanium platinum is applied. The cathode electrolytic plate 51 and the anode electrolytic plate 52 are provided below the flow port 34a of the inner container 34. At the central portion where the cathode electrolytic plate 51 and the anode electrolytic plate 52 face, a gap is formed and ions are provided. The crucible 53 is exchanged, and the cathode electrolytic plate 51 and the anode electrolytic plate 52 are separated by the ion exchange membrane 53. Further, around the cathode electrolytic plate 51 and the anode electrolytic plate 52, a mesh body 54 having a mesh capable of freely flowing pure water is provided. Further, in the electrolysis device 32 configured as described above, the cathode-side electrode rod 48 and the anode-side electrode rod 49 shown in Fig. 6 are respectively supplied with electricity, and the pure water (electrolyte) stored therein is electrolyzed. Hydrogen gas (HO) is generated on the side of the cathode electrolysis plate 51. The hydrogen gas is discharged to the hydrogen gas discharge port 38d of the hydrogen gas conduit 38 through the hydrogen gas flow path, and is passed through the piping member 56 connected to the hydrogen gas discharge port (refer to the figure). 3), and sent to the _ square carbon air through the filter ^7. In addition, on the other side of the anode electrolytic plate 52 side of the formation of oxygen (〇2), this oxygen will be discharged to the oxygen through the oxygen flow path 44 The oxygen discharge port 39d of the duct 39 is sent to the other oxygen delivery fan 59 through the piping member 58' connected to the oxygen discharge port 3^. * Among them, one of the carbon air filters 57 is The foam contained in the nitrogen gas generated in the electrolytic device i 32 is removed by filtration of a powder or the like (not shown). The carbon air filter 57 is connected to a circulation pump 62 through a pipe body (not shown). This circulation pump 62 is only driven by I, at The cycle "2" is provided with a gas suction port connected to the above-mentioned == 21 201033133 ^ 57, and a water suction port connected to the other end of the pipe body (omitted symbol) connected to the cold water storage tank 22 at one end, When the circulation pump 62 is driven, the hydrogen gas from the carbon air filter 57 is sucked in by one of the gas suction ports, and the water from the cold water storage tank 22 is sucked in through the other water suction port 62b. Further, the circulation pump 62 is not added by a pump mechanism (not shown).

以圖示之泵機構將所吸入之氫氣(h2)與水(h2〇)加以混合, 而以水中溶解有氫之加氫水(H2 + h2〇)的形態自排出口 62c 加壓送出。此循環泵62之排出口 62c,係透過管體(省略符 號。)連接於氣泡微細化過濾器63。此氣泡微細化過濾器 63’内裝有半透膜,該半透膜具有〇 〇〇〇1以m(約頭髮的工⑼ 萬分之1)之未圖示的微孔,藉由該半透膜,使自上述循環 泵62所加壓傳送之氫氣之氣泡微細化,具有提高加氫水中 之溶氫量的作用。此氣泡微細化過濾器63,係透過管體(省 略符號。)連接於上述冷水儲槽22。The hydrogen gas (h2) to be sucked is mixed with water (h2〇) by the pump mechanism shown in the figure, and is pressurized and sent out from the discharge port 62c in the form of hydrogenated water (H2 + h2〇) in which hydrogen is dissolved in water. The discharge port 62c of the circulation pump 62 is connected to the bubble refining filter 63 through a pipe body (the symbol is omitted). The bubble miniaturizing filter 63' is provided with a semi-permeable membrane having micropores (not shown) of 〇〇〇〇1 in m (about 1 part per mil of the hair), by the semi-transparent. The membrane refines the bubbles of hydrogen gas pressurized by the circulation pump 62, and has an effect of increasing the amount of hydrogen dissolved in the hydrogenation water. The bubble refining filter 63 is connected to the cold water storage tank 22 through a pipe body (notationally omitted).

因此’如圖3所示,來自氣泡微細化過濾器63之加氣 水,係被加壓傳送而儲存在上述冷水儲槽22内,然後儲存 在此冷水儲槽22内之加氫水’藉由驅動上述循環泵62,再 從該循環泵62之水吸入口 62b被吸進來,且與從氣體吸入 口 62a被吸進來之來自上述碳空氣過濾器57的氫氣混合, 然後從該循環泵62之排出口 62c經由上述氣泡微細化過慮 器63’再一次被加壓傳送而儲存於上述冷水儲槽22内。 即’儲存於上述冷水儲槽22内之加氫水,藉由經由構成本 發明之循環通路的冷水儲槽22、循環泵62及氣泡微細 、1匕過 22 201033133 使用者可在 據器6 3循環,可慢慢增加處理水中之溶氫量 溶氫量接近飽和狀態之狀態下飲用。 又’連接於上述電解裝置32之另一方的氧送出用 59,係僅在上述電解裝置32工作中驅動,於此氧 風扇 . 用風 扇59驅動時,係自該電解裝置32抽取上述電解裝 置3 2所Therefore, as shown in FIG. 3, the aerated water from the bubble refining filter 63 is transported by pressure and stored in the cold water storage tank 22, and then the hydrogenated water stored in the cold water storage tank 22 is borrowed. The circulation pump 62 is driven, and is sucked in from the water suction port 62b of the circulation pump 62, and is mixed with hydrogen gas from the carbon air filter 57 sucked in from the gas suction port 62a, and then from the circulation pump 62. The discharge port 62c is again pressurized and transported through the bubble refining filter 63' and stored in the cold water storage tank 22. That is, the hydrogenated water stored in the above-mentioned cold water storage tank 22 can be passed through the cold water storage tank 22 constituting the circulation passage of the present invention, the circulation pump 62, and the bubble fine, and the user can pass through the apparatus 6 3 3 . The circulation can be gradually increased while the amount of dissolved hydrogen in the treated water is near the state of saturation. Further, the oxygen supply 59 connected to the other of the electrolysis devices 32 is driven only during the operation of the electrolysis device 32, and the oxygen fan is extracted from the electrolysis device 32 when the fan 59 is driven by the electrolysis device 32. 2

生成之氧,且經由該氧送出用風扇59,而送出至圖i所八 之氧吸取管7内。然後,使用者可於上述電解裝置32工 中’自上述氧吸取管7之氧氣放出口 7a吸取氧氣。 另’上述電解裝置32,係藉由上述光照度感測器9(:之 亮訊號而工作,或者即使是在藉由自該光照度感測器9匸之 暗訊號而處於未工作的狀態時,亦可藉由按壓上述氧放出 開關9A而(強制性地)工作,於此電解裝置32工作的同時, 上述循環泵62與氧送出用風扇59亦分別被驅動。又,此 等電解裝置32專工作之時間,藉由圖4所示之連接於控制 裝置20之氫生成工作定時器9JJ,設定在15分,電解裝置 32等停止工作呈休止之時間,則藉由連接於控制裝置2〇之 氫生成休止定時器91,設定在45分。此等之設定時間,並 非僅限疋於上述設定時間,可視從冷水用出水口 3飲用加 氫水的頻率自由地變更。 接著’參照圖7所示之流程圖,説明藉由上述電解式 淨水裝置1生成氫氣’儲存加氫水且生成氧氣的順序及作 用效果°於使此電解式淨水裝置1工作前之準備階段,上 述氫生成工作定時器9H之設定時間係設定在15分鐘,氫 生成休止定時器91之設定時間設定在45分,又,光照度感 23 201033133 測器9C之設定照度,則是設定在與上述電解式淨水裝置^ 之使用時間區段對應的照度(日照時間區段之室内的照 度)。又’圖1所示之止水閥11’可藉由手動事先打開。 於最初之步驟Stl,上述預備儲槽18之水量是否為規定 量’係透過上述浮控開關21之微動開關21c,藉由控制裝 置20來判定,當判定未達到規定量時,則前進至步驟st2, 而判定已達到規定量時,則前進至下一步驟St3。此等之 中,在前進至步驟St2時,則打開上述電磁閥14,且驅動 上述加壓泵15,經由上述沉澱物過濾器12、碳過遽器' © 電磁閥14、逆滲透膜過濾器16及礦石過濾器17,將所純 水化之水加壓傳送而補充於上述預備儲槽18,然後返回步 驟Stl再重複,判定預備儲槽18之水量是否為規定量。另, 藉由上述加壓泵15所加壓傳送之水,亦會自上述逆滲透膜 過濾'器16分流至離子交換樹脂過濾器3丨,當打開設置於上 述電解裝置32之供水接頭46的錐孔46f時,亦會在上述電 解裝置3 2内進行純水化,補充水。 又,在前進至下一步驟St3時,光照度感測器9C之照 © 度是否為設定照度,係透過上述光照度感測器9C,藉由控 制裝置20來判定,當判定未達到設定照度時,則返回步驟 St3再重複,當判定已達到設定照度時,則前進至下一步驟 St4在前進至下一步驟st4時,使上述電解裝置32工作, 且使上述循環泵62及氧送出用風扇59驅動,藉由上述電 解裝置32之電解作用,生成氫氣與氧氣,然後前進至下一 步驟St5。另’於上述步驟st4中,若上述電解裝置32開 24 201033133 * ::作’則圖2所示之顯示面板8之氫、氧生成,燈扣將 冗燈’於後述之步驟st6中至上述電解裝置Μ之工作停 止為止之期間内,將會績哀 會夺續此儿燈狀態。又,由上述電解 生成之氫氣,將會經由上述碳空氣過遽器57被 吸至上述循環泵62, 而與來自上述冷水儲槽22之加氫水混 口 ’然後經由氣泡微細化、两请獎 匕倣細化過濾器63,以溶解有氫氣之加氫 水的形態,再一次回到上述 y 彳上述令水儲槽22。藉由經由此等之 ©循環通路加以据環,可慢慢增加處理水中之溶氫量,使用 者可在溶氫量接近飽和狀態之狀態下飲用。又,由 解裝置32所生成之羞$ , 成之氧虱,可藉由上述氧送出用風扇59送 出,自上述氧吸取管7之前端來吸取。 β又,於下-步驟St5中,上述電解裝置32等之工作時 間是否已經過15分鐘,伤读榀 、透過上述氫生成工作定時器9H, 藉由控制裝置2〇來判定’當判定上述電解裝置32等之工 作時間未經過15分鐘時,則返回步驟⑽再重複,當判定 ❹上述電解裝置32等之工作時間已經過15分鐘時,則前進 步驟St6。在“至下—㈣⑽時,則使上述電解 59之工作停止’且使上述循環泵62及氧送出用風扇 Γ休之驅Γ停止,上述電解裝置32所進行之氳氣與氧氣的生 :休止後’前進至下—步驟st7。另,於上述步驟⑽中, …電解裝置32之工作停止,則圈2所示之顯示面板8 氧休止中燈把將會亮燈,於下次之步驟St4中至上 l電解裝置32之工作開始為止之期間内將會持續此亮燈。 於下一步驟⑽中,氧放出開關9A是否為〇N,係透 25 201033133 過該氧放出關9A,藉由控制裝置2〇來判定,举判定為 ON時,則反回步驟St4再重複,使上述電解裝!3田2工作·, 且使上述循環泵62及氧送出用風扇59驅動,藉由上述電 解裝置32之電解作用’生成氫氣與氧氣,當判定非為ON(為 ㈣時’則前進至下一步驟st8。另,於上述步驟⑽中, 判定氧放出開關9A為〇N的條件,為儘管上述氫、氧休止 中燈8E焭’氫氣及氧氣未生成,然而使用者為了想吸取氧 氣而按壓上述氧放出開關9A之條件。 〜 在前進至下一步驟St8時’電解裝置32等之休止時間 是否已經過45分鐘,係透過上述氫生成休止定時器Μ, 由控制裝置20來判定,當判定上述電解裝置等之休止 時間未經過45分鐘時,則返回步驟⑽再重複,當判一上 :電解裝置32等之工作時間已經過45分鐘 二 驟St3再重複。 ~ w 7 藉由以上方式,本實施形態之電解式淨水裝置1,並 ❹ -直連續地運轉’例如,在無須飲用加氫水或攝取氧氣 深夜(就寢中),藉由上述光照度感測器 風知至内之昭 度,使運轉休止,I即使是在未休止之情形亦: 述氫生成工作定時器9H或氫生成休止定時器 解裝置^循環泵62及氧送出用風扇59反覆進行驅= 分鐘、停止45分鐘之循環。因此,此電解式淨水裝置 不僅可將處理水中之溶氫量保持在一定 , £ 疋量,而且還可省電〇 另,於圖2所不之顯示面板8之冷水狀態顯示燈叱 及操作面板9之冷水溫度開關9d亮燈中 冷部中),藉由按 26 201033133 壓該冷水溫度開關9D使其為OFF,可使上述冷卻器24停 止。藉此’使用者可飲用到常溫之加氫水。此冷水溫度開 關9D之ON/OFF操作,可在上述自動運轉中的任意時期 操作。又,於圖2所示之顯示面板8之溫水狀態顯示燈8B、 與操作面板9之溫水溫度開關9B亮燈中(加溫中),藉由按 壓該溫水溫度開關9B使其為〇FF,可使上述加熱器27停 止。藉此’使用者可飲用到常溫之純水。此溫水溫度開關 9B之ΟΝ/OFF操作,可在上述自動運轉中的任意時期操作。 【圖式簡單說明】 圖1 ’係顯示本發明之實施形態之電解式淨水裝置的外 形立體圖。 圖2’係圖1所示之電解式淨水裝置之部分圖,(a)係表 示顯示面板之前視圖,(b)為表示操作面板之前視圖。 Φ 圖3’係顯示本發明之實施形態之電解式淨水裝置之構 成的示意圖。 圖4’係顯示本發明之實施形態之電 制系統的方塊圖。 I衣I仏 紐坡署/系構成本發明之實施形態之電解式淨水裝置的電 解裝置’(a)為前視圖,(b)為⑷之A部放大圖。 解裝構成本發明之實施形態之電解式淨水裝置的電 1剖面圖’(b)為⑷之Β部放大圖。 糸顯不本發明之實施形態之 作的流程圖。 电鮮式淨水裝置之動 27 201033133 【主要元件符號說明】 1 電解式淨水裝置 2 框體 3 冷水用出水口 4 溫水用出水口 7 氧吸取管The generated oxygen is sent to the oxygen suction pipe 7 of Fig. i through the oxygen supply fan 59. Then, the user can suck oxygen from the oxygen discharge port 7a of the oxygen suction pipe 7 at the above-mentioned electrolysis device 32. In addition, the electrolysis device 32 is operated by the illuminance sensor 9 (or the bright signal), or even when it is in an inoperative state by the dark signal from the illuminance sensor 9 The oxygen discharge switch 9A can be pressed (mandatory) to operate, and the circulation pump 62 and the oxygen delivery fan 59 are driven separately while the electrolysis device 32 is operating. Further, the electrolysis devices 32 operate exclusively. At the time, the hydrogen generation work timer 9JJ connected to the control device 20 shown in FIG. 4 is set at 15 minutes, and the electrolysis device 32 and the like are stopped for a rest time, and the hydrogen is connected to the control device 2 The stop timer 91 is generated and set at 45. The set time is not limited to the above-described set time, and the frequency of drinking the hydrogenated water from the cold water outlet 3 can be freely changed. The flow chart illustrates the sequence and effect of generating hydrogen gas by the above-described electrolytic water purification device 1 to store hydrogenated water and generating oxygen. The hydrogen generation is performed in the preparation stage before the electrolytic water purification device 1 is operated. The setting time of the work timer 9H is set to 15 minutes, the set time of the hydrogen generation stop timer 91 is set to 45 minutes, and the illuminance feeling 23 201033133 is set to the illuminance of the detector 9C, which is set in the above-mentioned electrolytic water purification. The illuminance corresponding to the time zone of the device ^ (the illuminance in the room of the sunshine time zone). The water stop valve 11' shown in Fig. 1 can be opened by hand beforehand. In the initial step St1, the above-mentioned preliminary storage tank Whether the amount of water of 18 is a predetermined amount is determined by the control device 20 through the micro switch 21c of the float switch 21, and when it is determined that the predetermined amount has not been reached, the process proceeds to step st2, and when it is determined that the predetermined amount has been reached, Then, the process proceeds to the next step St3. In the above, when the process proceeds to step St2, the solenoid valve 14 is opened, and the pressurizing pump 15 is driven through the deposit filter 12 and the carbon filter ' © electromagnetic The valve 14, the reverse osmosis membrane filter 16, and the ore filter 17 are pressurized and transported to the preliminary storage tank 18, and then returned to step S1 and repeated to determine whether the amount of water in the preliminary storage tank 18 is Further, the water pressurized by the pressure pump 15 is also branched from the reverse osmosis membrane filter 16 to the ion exchange resin filter 3, and the water supply port provided to the electrolysis device 32 is opened. When the taper hole 46f of 46 is also purely hydrated in the electrolysis device 32, the water is replenished. Further, when the process proceeds to the next step St3, whether the illuminance sensor 9C is the illuminance is the set illuminance. The illuminance sensor 9C determines by the control device 20 that when it is determined that the set illuminance has not been reached, the process returns to step St3 and repeats. When it is determined that the set illuminance has been reached, the process proceeds to the next step St4. In the first step st4, the electrolysis device 32 is operated, and the circulation pump 62 and the oxygen delivery fan 59 are driven, and hydrogen gas and oxygen gas are generated by the electrolysis of the electrolysis device 32, and the process proceeds to the next step St5. In the above step st4, if the electrolysis device 32 is opened 24 201033133 * :: "the hydrogen and oxygen of the display panel 8 shown in FIG. 2 are generated, the lamp buckle will be redundant" in the step st6 described later to the above During the period when the operation of the electrolyzer is stopped, the performance of the lamp will be resumed. Further, the hydrogen gas generated by the above-described electrolysis is sucked into the circulation pump 62 via the carbon air filter 57, and is mixed with the hydrogenated water from the cold water storage tank 22, and then refined by the bubble. The prize-like refinement filter 63 is returned to the above-described water storage tank 22 in the form of hydrogenated water in which hydrogen is dissolved. By applying a loop through the © circulation path, the amount of dissolved hydrogen in the treated water can be gradually increased, and the user can drink while the amount of dissolved hydrogen is close to saturation. Further, the shyness generated by the decomposing means 32, and the oxygen enthalpy, can be sent by the oxygen sending fan 59, and sucked from the front end of the oxygen suction pipe 7. In addition, in the next step St5, whether the working time of the electrolysis device 32 or the like has passed 15 minutes, the damage reading, the hydrogen generation work timer 9H, and the control device 2〇 determine that the electrolysis is determined. When the operation time of the device 32 or the like has not passed for 15 minutes, the process returns to the step (10) and is repeated. When it is determined that the operation time of the electrolysis device 32 or the like has elapsed for 15 minutes, the process proceeds to step St6. In the case of "to the next - (4) (10), the operation of the electrolysis 59 is stopped", and the circulation pump 62 and the fan for the oxygen delivery fan are stopped, and the helium gas and the oxygen gas generated by the electrolysis device 32 are stopped. After 'going forward to step-step st7. In addition, in the above step (10), the operation of the electrolysis device 32 is stopped, and the display panel 8 shown in circle 2 is turned on in the oxygen stop, in the next step St4 In the next step (10), the oxygen release switch 9A is 〇N, and the system is permeable to 25A through the 2010 When the device 2 determines that the determination is ON, the process returns to step St4 again, and the electrolysis device 3 is operated, and the circulation pump 62 and the oxygen delivery fan 59 are driven by the electrolysis device. The electrolysis action of 32 'generates hydrogen and oxygen, and when it is judged that it is not ON (when (4)', proceeds to the next step st8. Further, in the above step (10), it is determined that the oxygen release switch 9A is 〇N, in spite of the above Hydrogen and oxygen in the middle of the lamp 8E焭' hydrogen and oxygen The condition for pressing the oxygen discharge switch 9A in order to take in oxygen is not generated. When the user proceeds to the next step St8, the operation time of the electrolysis device 32 or the like has elapsed for 45 minutes, and the hydrogen generation rest time is transmitted through the hydrogen generation. The device 判定 is determined by the control device 20, and when it is determined that the rest time of the electrolysis device or the like has not passed for 45 minutes, the process returns to the step (10) and is repeated. When the operation time of the electrolysis device 32 or the like has passed 45 minutes, St3 is repeated again. ~ w 7 By the above manner, the electrolytic water purification device 1 of the present embodiment is operated continuously and continuously 'for example, without drinking hydrogenated water or ingesting oxygen late at night (in bedtime), by The illuminance sensor is known to be within the visibility, so that the operation is stopped, and even if it is not stopped: the hydrogen generation work timer 9H or the hydrogen generation stop timer solution device 循环 pump 62 and oxygen delivery The fan 59 repeatedly performs the cycle of driving for 5 minutes and stopping for 45 minutes. Therefore, the electrolytic water purifying device can not only keep the amount of dissolved hydrogen in the treated water constant, but also In addition, in the cold water state display panel of the display panel 8 and the cold water temperature switch 9d of the operation panel 9 in the light-cooling section, the cold water temperature switch 9D is pressed by 26 201033133 to make it OFF, the cooler 24 can be stopped, whereby the user can drink the hydrogenated water at normal temperature. The ON/OFF operation of the cold water temperature switch 9D can be operated at any time during the above automatic operation. 2, the warm water state indicator lamp 8B of the display panel 8 and the warm water temperature switch 9B of the operation panel 9 are illuminated (in warming), and the temperature of the warm water temperature switch 9B is pressed to make it 〇FF. The heater 27 is stopped, whereby the user can drink pure water at normal temperature. The ΟΝ/OFF operation of the warm water temperature switch 9B can be operated at any time during the above automatic operation. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is an external perspective view showing an electrolytic water purification apparatus according to an embodiment of the present invention. Fig. 2' is a partial view of the electrolytic water purifying device shown in Fig. 1, (a) showing a front view of the display panel, and (b) showing a front view of the operation panel. Φ Fig. 3' is a schematic view showing the configuration of an electrolytic water purification apparatus according to an embodiment of the present invention. Fig. 4' is a block diagram showing an electrical system of an embodiment of the present invention. I(I) is an enlarged view of the A portion of (4) which is an electrolysis device of the electrolytic water purification device according to the embodiment of the present invention. The electric cross-sectional view (b) of the electrolytic water purification apparatus constituting the embodiment of the present invention is an enlarged view of the crotch portion of (4). A flowchart showing an embodiment of the present invention is shown. Operation of electric fresh water purifier 27 201033133 [Explanation of main components] 1 Electrolytic water purifier 2 Frame 3 Cool water outlet 4 Warm water outlet 7 Oxygen suction tube

7a 氧氣放出口 12 沉澱物過濾器 13 碳過濾器 15 加壓泵 16 逆滲透膜過濾器 17 礦石過濾器 18 預備儲槽 20 控制裝置7a Oxygen discharge port 12 Sediment filter 13 Carbon filter 15 Pressurizing pump 16 Reverse osmosis membrane filter 17 Ore filter 18 Pre-storage tank 20 Control unit

22 冷水儲槽 23 溫水儲槽 31 離子交換樹脂過濾器 32 電解裝置 38 d 氫氣排出口 39 d 氧氣排出口 40 電解部 51 陰極電解板 52 陽極電解板 28 20103313322 Cold water storage tank 23 Warm water storage tank 31 Ion exchange resin filter 32 Electrolytic unit 38 d Hydrogen discharge port 39 d Oxygen discharge port 40 Electrolysis unit 51 Cathodic electrolysis plate 52 Anode electrolysis plate 28 201033133

57 碳空氣過濾器 59 氧送出用風扇 62 循環泵 63 氣泡微細化過濾、器 2957 Carbon Air Filter 59 Oxygen Delivery Fan 62 Circulating Pump 63 Bubble Refinement Filter 29

Claims (1)

201033133 七、申請專利範圍: 1 ·一種電解式淨水裝置’具備有用以將水加以淨化之淨 水處理部、儲存經由此淨水處理部之水的處理水健槽及 用以供應儲存在此處理水儲槽之水的出水部,其特徵在 於’具備有: 自經由該淨水處理部之水生成純水的純水生成部、 用以將自此純水生成部所生成之純水供給至該處理水 儲槽的供給通路、 用以對該純水生成部所生成之純水的一部分進行電 ❹ 解’藉此生成氫氣的氩氣生成部、 用以自該處理水儲槽内取出處理水,再一次使其回到 該處理水儲槽的循環通路、及 設置在此循環通路之中途部,用以使自該處理水儲槽 所取出之處理水與該氫氣一起回到該處理水儲槽的循環 泵》 2.如申請專利範圍第1項之電解式淨水裝置,其中,該 循環通路之中途部,於該循環泵與處理水儲槽之間,設置 〇 有用以使該氫氣之氣泡微細化的氣泡微細化過濾器。 3_如申请專利範圍第1或2項之電解式淨水裝置,其 中該循環泵與氫氣生成部,係連接於内裝有定時器之控 制裝置而成,且此控制裝置連接有光照度感測器,透過該 光”、、度感測器,當該控制裝置判定為規定之照度時則透 過疋時器,使該循環泵與氫氣生成部於規定時間内被反覆 驅動與停止。 30 201033133 中,4二申氫1專:範圍第…項之電解式淨水裝置,其 路用=二成:連接有氧氣流通通路,該氧氣流通通 二:此氣氣流通通路之前端,為用以故出使用4;: 之氧氣的氧氣放出口。 所吸取 如申請專利範圍第3項之電解式淨水裝置,其中 該風氣生成部連接有氧氣流通通路,該氧氣流it通路用 參 =由該純水之電解而與聽—起生成之氧氣流通且此 氡氣机通通路之剛#,為用以放出使用者所吸取 氧氣放出口。 I氣的 6. 如申請專利範圍第4項之電解式淨水裝置,其中,在 該氧氣流通通路之中途部,設置有用以將該氧氣加以送出 之風扇,且此風扇係連接於該控制裝置,且於該控制裝置 連接有氧放出用開關,在該循環泵與氫氣生成部之驅動停 止時,當該控制裝置判定該氧放出用開關為〇Ν的時候,該 風扇與循環泵與氫氣生成部將會開始驅動。 7. 如申請專利範圍第5項之電解式淨水裝置,其中,在 該氧氣流通通路之中途部,設置有用以將該氧氣加以送出 之風扇,且此風扇係連接於該控制裝置,且於該控制裝置 連接有氧放出用開關,在該循環泵與氫氣生成部之驅動停 止時’當該控制裝置判定該氧放出用開關為ON的時候,該 風扇與循環泵與氫氣生成部將會開始驅動。 31201033133 VII. Patent application scope: 1 · An electrolytic water purification device 'has a water treatment unit for purifying water, a treatment water tank for storing water passing through the water treatment unit, and for storing and storing therein The water discharge unit that processes the water in the water storage tank is characterized in that: a pure water generating unit that generates pure water from the water passing through the water purification unit, and supplies pure water generated from the pure water generating unit a supply passage to the treated water storage tank, and an argon gas generating portion for generating hydrogen gas by electrically extracting a part of the pure water generated by the pure water generating portion, for taking out from the treated water storage tank Treating the water, returning it to the circulation passage of the treated water storage tank again, and setting it in the middle of the circulation passage, so that the treated water taken out from the treated water storage tank is returned to the treatment together with the hydrogen The circulating water pump of the water storage tank according to the first aspect of the invention, wherein the intermediate portion of the circulation passage is disposed between the circulation pump and the treated water storage tank, so that the Hydrogen The bubble refinement filter in which the bubbles are fine. 3_ The electrolytic water purification device of claim 1 or 2, wherein the circulation pump and the hydrogen generating unit are connected to a control device having a timer, and the control device is connected with illuminance sensing When the control device determines that the predetermined illuminance is determined, the circulator and the hydrogen generating unit are repeatedly driven and stopped for a predetermined period of time through the illuminator. 30 201033133 , 4 2 Shen hydrogen 1 special: the scope of the ... item of the electrolytic water purification device, its road = 20%: connected with oxygen circulation path, the oxygen circulation through two: the front end of the gas flow through the passage, for the purpose The oxygen-purifying outlet of the oxygen is used as the oxygen-containing water purifying device of the third aspect of the patent application, wherein the gas generating portion is connected with an oxygen flow passage, and the oxygen flow is used for the passage The electrolysis of water is circulated with the oxygen generated by the hearing and the passage of the helium gas passage is used to release the oxygen outlet of the user. I. 6. The electrolytic method of claim 4 Water purification device, Wherein, a fan for sending the oxygen gas is provided in the middle of the oxygen flow path, and the fan is connected to the control device, and an oxygen release switch is connected to the control device, and the circulation pump and the hydrogen gas are connected to the control device. When the driving of the generating unit is stopped, when the control device determines that the oxygen releasing switch is 〇Ν, the fan and the circulation pump and the hydrogen generating unit will start driving. 7. The electrolytic net according to item 5 of the patent application. In the water device, a fan for sending the oxygen gas is provided in the middle of the oxygen flow path, and the fan is connected to the control device, and the control device is connected to the oxygen release switch. When the drive of the pump and the hydrogen generating unit is stopped, 'When the control device determines that the oxygen release switch is ON, the fan and the circulation pump and the hydrogen generating unit will start driving. 31
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