WO2020133349A1 - 电解氢氧超微气泡装置 - Google Patents

电解氢氧超微气泡装置 Download PDF

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Publication number
WO2020133349A1
WO2020133349A1 PCT/CN2018/125343 CN2018125343W WO2020133349A1 WO 2020133349 A1 WO2020133349 A1 WO 2020133349A1 CN 2018125343 W CN2018125343 W CN 2018125343W WO 2020133349 A1 WO2020133349 A1 WO 2020133349A1
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reverse osmosis
pump
bracket
electrolysis
hydrogen
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English (en)
French (fr)
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杨境界
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Season Farm Technology Co Ltd
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Season Farm Technology Co Ltd
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G7/00—Botany in general
    • A01G7/06—Treatment of growing trees or plants, e.g. for preventing decay of wood, for tingeing flowers or wood, for prolonging the life of plants

Definitions

  • the invention relates to a micro-bubble device, in particular to an electrolysis hydrogen-oxygen ultra-micro-bubble device for producing hydrogen and oxygen in an electrolyzer and preparing ultra-micro-bubbles.
  • Microbubble is a kind of bubble with a small diameter.
  • Common microbubble devices on the market can usually produce bubbles with a diameter of about 50 microns. After the microbubbles manufactured by the microbubble device are injected into water, the diameter of the microbubble is micron level.
  • Microbubbles stay in water for a longer time than bubbles with a diameter of millimeters, so the water will appear turbid white, and the energy emitted by water with microbubbles when disintegrating through the microbubbles can be The mixture of microorganisms, bacteria or pollutants in the water is destroyed and destroyed. The energy released by the disintegration of micro-bubbles can be physically harmed to achieve physical sterilization.
  • the water produced by the micro-bubble device has been used for agricultural irrigation , Fish farming or food processing industries.
  • the existing micro-bubble device conveys the water of mixed air by an impeller pump.
  • the impeller pump includes a pump casing and a blade.
  • the pump casing has a rotating space, a water inlet, an air inlet, and an outlet.
  • the rotation space is formed inside the pump casing, the water inlet is formed in the pump casing and communicates with the rotation space, the air inlet is formed in the pump casing and communicates with the water inlet, and the outlet is formed in the pump casing and communicates with the rotation
  • the vane is rotatably arranged in the rotating space of the pump casing. During the transportation process, the water input from the water inlet and the air input from the air inlet are blown by the vane of the impeller pump to make the water The hydrogen and oxygen are struck by the blade and the air is crushed, thereby generating fine bubbles.
  • the blade blow of the impeller pump of the existing micro-bubble device can produce bubbles with a diameter of about 50 microns.
  • the bubbles produced by the micro-bubble device only maintain the level of micron diameter, and cannot kill more than 50 microns in diameter.
  • Tiny microorganisms so the effectiveness of the micro-bubble device is currently limited in the elimination of bacteria, and in the process of making micro-bubbles, the air input into the air inlet is general air, whether it is in agricultural irrigation, fish farming or food processing None of the above has any special effect, causing the problem of insufficient functionality of the micro-bubble device.
  • the main purpose of this technical solution is to provide an electrolysis hydrogen-oxygen ultra-micro-bubble device, by which the existing micro-bubble device can only produce micro-bubbles with a diameter of about 50 microns, and cannot destroy microorganisms smaller than 50 microns, resulting in a sterilization effect
  • the electrolytic hydrogen-oxygen ultrafine bubble device of the present technical solution includes:
  • a storage unit the storage unit includes a bracket, a storage tank, a bifurcation tube, a gas flow meter and an air inlet tube, the storage tank is disposed on the bracket, the bifurcation tube communicates with the storage tank and branches into Two water inlet pipes, the gas flow meter is arranged on the bracket, the gas inlet pipe is arranged on the bracket and communicates with the branch pipe through the gas flow meter, the pipe diameter of the gas inlet pipe is smaller than that of the branch pipe ;
  • An electrolysis unit is installed on the bracket and communicates with the bifurcated pipe.
  • the electrolysis unit includes an electrolyzer and an electrolytic vessel.
  • the electrolyzer is installed on the bracket and connected to the bifurcated pipe.
  • the electrolyzer is connected to the support, and the electrolytic container contains electrolyte, and the electrolyzer can electrolyze the electrolyte into hydrogen and oxygen;
  • the ultra-micro-bubble forming unit includes two reverse osmosis pump sets, a merging tube, a uniform pressure mixing barrel and a Circulation pipe, the two reverse osmosis pumps are connected to the two water inlet pipes of the bifurcated pipe, the two reverse osmosis pumps are connected to the merger pipe, the merged pipe is connected to the two reverse osmosis pumps and the pressure is evenly mixed
  • the barrel, the uniform pressure mixing barrel is arranged on the bracket, the circulation pipe is connected to the uniform pressure mixing barrel and extends into the storage tank, and the storage unit and the ultrafine bubble making unit form a circulation system.
  • the electrolytic hydrogen-oxygen ultrafine bubble device of the present technical solution uses the reverse osmosis pump set of the unit made of the ultrafine bubbles, before the water in the storage tank flows into the unit made of the ultrafine bubbles, the air inlet pipe will input air to make the water Mixed with air, when the water containing air is sent into the two water inlet pipes and enters the two reverse osmosis pump sets, the two reverse osmosis pump sets allow the hydrogen and oxygen in the water to compress and rupture and reduce to fine bubbles.
  • the storage unit and the ultra-micro-bubble forming unit form a circulation system, allowing hydrogen and oxygen in the water to compress and rupture to form ultra-micro-bubbles with a diameter of 0.2 microns, which can kill microorganisms, bacteria or pollutants with a size of 0.2 microns in the water
  • the mixture, and the hydrogen produced by the electrolyzer allows the ultra-fine bubbles of hydrogen to achieve the effect of bacteriostasis and sterilization, to achieve the practicality of sterilization and enhance the diversity of functions.
  • FIG. 1 is a schematic side view of a preferred embodiment of an electrolysis hydrogen-oxygen ultrafine bubble device of the present invention.
  • FIG. 2 is a schematic side view of the operation of a preferred embodiment of the electrolytic hydrogen-oxygen ultrafine bubble device of the present invention.
  • FIG. 3 is a partially enlarged schematic side view of the operation mode of a preferred embodiment of the electrolytic hydrogen-oxygen ultrafine bubble device of the present invention.
  • the electrolysis hydrogen-oxygen ultrafine bubble device of the present invention includes a storage unit 10 and an electrolysis unit 20 ⁇ ubbles made unit 30.
  • the storage unit 10 includes a bracket 11, a storage tank 12, a branch pipe 13, a gas flow meter 14 and an air inlet pipe 15.
  • the storage tank 12 is disposed on the bracket 11, and the branch pipe 13 communicates with the storage
  • the tank 12 is bifurcated into two water inlet pipes 16, the gas flow meter 14 is disposed on the bracket 11, the gas inlet pipe 15 is disposed on the bracket 11 and communicates with the branch pipe 13 through the gas flow meter 14, the The diameter of the air inlet pipe 15 is smaller than the diameter of the branch pipe 13.
  • the storage unit 10 includes an air pump 17 and a filter 18.
  • the air pump 17 is disposed on the bracket 11 and connected to the water inlet pipe 16 and the storage tank 12, the filter 18 is disposed on the bracket 11, the storage tank 12 communicates with the branch pipe 13 through the filter 18 and branches out two water inlet pipes 16 behind the filter 18, further
  • the storage tank 12 has a filling tube 121 and a completion tube 122.
  • the filling tube 121 and the completion tube 122 are both disposed on the storage tank 12 and communicate with the storage tank 12.
  • the electrolysis unit 20 is installed on the bracket 11 and communicates with the branch pipe 13.
  • the electrolysis unit 20 includes an electrolyzer 21 and an electrolytic vessel 22.
  • the electrolyzer 21 is installed on the bracket 11 and connected to the branch pipe 13.
  • the electrolytic vessel 22 is installed on the support 11 and connected to the electrolyzer 21, and the electrolytic vessel 22 contains an electrolytic solution.
  • the electrolytic vessel 21 can electrolyze the electrolytic solution into hydrogen and oxygen.
  • the electrolytic unit 20 includes a supplement A pump 23 and a supplementary tank 24, the supplementary pump 23 is disposed on the bracket 11 and communicates with the electrolytic vessel 22, the supplementary tank 24 is disposed on the bracket 11 and communicates with the supplementary pump 23, and the supplementary tank 24 contains electrolysis liquid.
  • the ultrafine bubble making unit 30 is disposed on the support 11 of the storage unit 10.
  • the ultrafine bubble making unit 30 includes two reverse osmosis pump sets 31, a combining tube 32, a uniform pressure mixing barrel 33 and a circulation Pipe 34, the two reverse osmosis pump groups 31 are connected to the two water inlet pipes 16 of the bifurcated pipe 13, the combined pipe 32 is connected to the two reverse osmosis pump groups 31 and the uniform pressure mixing barrel 33, the uniform pressure mixing barrel 33 is disposed on the bracket 11, the circulation pipe 34 is connected to the uniform pressure mixing barrel 33 and extends into the storage tank 12, the storage unit 10 and the ultra-micro bubble forming unit 30 form a circulation system, wherein, each The reverse osmosis pump group 31 includes a first reverse osmosis pump 35 and a second reverse osmosis pump 36, two of the first reverse osmosis pumps 35 are connected to the two water inlet pipes 16 of the branch pipe 13, and two of the first reverse osmosis pumps The osmotic pump
  • the electrolytic hydrogen-oxygen ultrafine bubble device includes a cooling unit 40 including a refrigerant coil 41, a temperature barrier 42 and a cooler 43.
  • the refrigerant coil 41 is provided Outside the storage tank 12, the refrigerant coil 41 controls the temperature of the storage tank 12 to be between 10° C. and 20° C.
  • the temperature barrier 42 is disposed outside the cold coal coil 41, and the temperature barrier 42 is maintained The temperature controlled by the refrigerant coil 41 is connected to the refrigerant coil 41 by the cooler 43.
  • a preferred embodiment of the electrolysis hydrogen-oxygen ultrafine bubble device of the present invention is disclosed.
  • the user can fill the filling tube 121 of the storage tank 12 with water 50 to allow the storage tank 12
  • the operation of producing ultra-fine oxyhydrogen bubbles is started.
  • the water 50 in the storage tank 12 will flow from the branch pipe 13 through the filter 18.
  • the filter 18 When passing the filter 18, the water 50 Impurities are removed to ensure that when entering the ultra-micro-bubble forming unit 30, the two reverse osmosis pump units 31 will not be damaged, and then water 50 will flow from the branch pipe 13 into the two water inlet pipes 16 and into the two ⁇ reverse osmosis pump group 31.
  • the user can control the flow rate of the air in the air inlet pipe 15 by controlling the gas flow meter 14, the air will flow into the branch through the air inlet pipe 15
  • the electrolysis unit 20 will pass
  • the electrolyzer 21 electrolyzes the electrolyte in the electrolysis vessel 22, and electrolyzes hydrogen and oxygen into the branch pipe 13, wherein the electrolyte in the electrolysis vessel 22 is gradually reduced after being electrolyzed, and can be passed through the supplementary pump 23
  • the electrolytic solution in the replenishing tank 24 is transferred into the electrolytic vessel 22 for replenishment.
  • each reverse osmosis pump group 31 includes a first reverse osmosis pump 35 and a first Two reverse osmosis pumps 36
  • water 50 with hydrogen and oxygen will pass through the first reverse osmosis pump 35
  • the water 50 is pressurized by the first reverse osmosis pump 35, so that the hydrogen and oxygen in the water 50 is compressed and ruptured
  • the reduction becomes fine air bubbles
  • the water 50 is pressurized and delivered to the second reverse osmosis pump 36, and the hydrogen and oxygen in the water 50 are pressurized by the second reverse osmosis pump 36 to rupture and reduce to more Fine bubbles
  • the first reverse osmosis pump 35 and the second reverse osmosis pump 36 form a series, which can make the hydrogen and oxygen in the water 50 have a stronger pressurized effect, and the compressed hydrogen and oxygen break down and become fine bubbles.
  • the water 50 and fine bubbles pressurized by the two reverse osmosis pump groups 31 are sent into the uniform pressure mixing barrel 33 by the combining pipe 32, the water 50 and fine bubbles will be in the uniform pressure mixing barrel 33 Squeezed by a uniform pressure to produce a liquid that is uniformly mixed with hydrogen-containing microbubbles and oxygen microbubbles, and then the circulation tube 34 conveys the liquid containing hydrogen microbubbles and oxygen microbubbles back to the storage tank 12, After circulating the above operation steps for 5 minutes, ultrafine bubbles with a diameter of 0.2 micron ( ⁇ m) of hydrogen and oxygen can be generated, and the cooling unit 40 can maintain the ultrafine bubbles content in the storage tank 12.
  • the ultrafine bubble liquid with a diameter of 0.2 micron hydrogen and oxygen will be stored in the storage tank 12, the user can use the completion tube 122 to obtain the ultrafine Bubble liquid, and can be used in industries such as agricultural irrigation, fish farming or food processing.
  • the energy emitted by the ultra-micro bubbles when they disintegrate can kill 0.2 microns of microorganisms and bacteria in water Or a mixture of pollutants
  • the energy emitted by the disintegration of ultra-micro bubbles can be physically harmed to achieve physical sterilization, and the hydrogen and oxygen produced by the electrolyzer make the gas of ultra-bubbles have both oxygen and hydrogen.
  • hydrogen ultra-micro bubbles generate ultrasonic phenomenon when the ultra-micro bubbles disintegrate, and have the characteristics of negative ions, thereby achieving the effects of bacteriostasis and sterilization, achieving the practicality of sterilization and enhancing the diversity of functions.
  • the electrolysis hydrogen-oxygen ultrafine bubble device of the present invention uses the reverse osmosis pump unit 31 of the ultrafine bubble making unit 30 to send water 50 containing hydrogen and oxygen from the branch pipe 13 into the two
  • the two reverse osmosis pumps 31 reduce the compression and rupture of hydrogen and oxygen in the water 50 to become fine bubbles, and the storage unit 10 and the ultrafine bubbles
  • the manufacturing unit 30 forms a circulation system to circulate the hydrogen and oxygen in the water 50 to form ultra-micro bubbles with a diameter of 0.2 microns, which can kill a mixture of microbes, bacteria or contaminants in the water 50 with a size of 0.2 microns.
  • the hydrogen produced by the electrolyzer 21 allows the ultra-fine bubbles of hydrogen to achieve the effects of bacteriostasis and sterilization, to achieve the practicality of sterilization and to enhance the diversity of functions, and has industrial practicality.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

一种电解氢氧超微气泡装置，其包含一储存单元(10)、一电解单元(20)及一超微气泡制成单元(30)，储存单元(10)包含一支架(11)、一储存槽(12)、一分岔管(13)及一入气管(15)，储存槽(12)设置于支架(11)上，分岔管(13)连通储存槽(12)并连通入气管(15)，电解单元(20)设置于支架(11)上并连接分岔管(13)，电解单元(20)可电解出氢气及氧气，超微气泡制成单元(30)设置于支架(11)上并包含两个连接分岔管(13)的逆渗透泵组(31)及一连通两个逆渗透泵组(31)的压力均匀混合桶(33)；该电解氢氧超微气泡装置借由逆渗透泵组(31)，让水中氢气及氧气压缩破裂成直径0.2微米的超微气泡，可消灭0.2微米的混合物，且电解单元(20)电解出的氢气，抑菌又灭菌，具有杀菌的实用性及功能多样性。

Description

电解氢氧超微气泡装置 技术领域
本发明是关于一种微气泡装置，尤其是指一种以电解器产生氢气氧气及制备超微气泡的电解氢氧超微气泡装置。
背景技术
微气泡是一种直径细小的气泡，市面上常见的微气泡装置通常能制造出直径约为50微米的气泡，该微气泡装置所制造的微气泡注入水中后，因微气泡的直径是微米级别，微气泡于水中停留的时间相较于直径为毫米级别的气泡停留的时间要长，因而水会呈现浊白色，具有微气泡的水在通过微气泡的破裂崩解时所散发的能量，可使得水中的微生物、细菌或污染物等混合物受到破坏而消灭，微气泡崩解所散发的能量为物理性伤害而可达到物理性杀菌，目前该微气泡装置制造出的水已被用于农业灌溉、渔业养殖或食品加工等产业。
现有微气泡装置是以叶轮式泵浦将混合空气的水输送，该叶轮式泵浦包含一泵壳及一叶片，该泵壳具有一旋转空间、一入水口、一入气口及一出口，该旋转空间形成于该泵壳的内部，该入水口形成于该泵壳并连通该旋转空间，该入气口形成于该泵壳并连通该入水口，该出口形成于该泵壳并连通该旋转空间，该叶片可旋转的设置于该泵壳的旋转空间，在输送的过程中，该入水口输入的水跟该入气口输入的空气，被该叶轮式泵浦的叶片旋转打击，使水中的氢气及氧气受到该叶片的打击而使空气被击碎，进而产生细微的气泡。
然而，现有微气泡装置的叶轮式泵浦的叶片打击，所能制造的气泡直径约为50微米，该微气泡装置所制造的气泡仅维持微米直径的级别，无法杀死直径比50微米更细小的微生物，因此目前该微气泡装置在消灭细菌的成效上受到局限，并且在制造微气泡的过程中，该入气口输入的空气为一般的空气，不论是在农业灌溉、渔业养殖或食品加工上皆无任何特别的功效，造成该微气泡装置的功能性不足的问题。
发明内容
本技术方案的主要目的在于提供一种电解氢氧超微气泡装置，借以改善现有微气泡装置只能制造直径约为50微米的微气泡，无法消灭比50微米更细小的微生物，造成杀菌效果不佳的问题，以及微气泡是以一般空气制成，并无额外功效，造成微气泡装置功能性不足的问题。
为达成上述的目的，本技术方案的电解氢氧超微气泡装置包含：
一储存单元，该储存单元包含一支架、一储存槽、一分岔管、一气体流量计及一入气管，该储存槽设置于该支架上，该分岔管连通该储存槽并分岔为两个入水管，该气体流量计设置 于该支架上，该入气管设置于该支架上并经该气体流量计而连通该分岔管，该入气管的管径小于该分岔管的管径；
一电解单元，该电解单元设置于该支架上并连通该分岔管，该电解单元包含一电解器及一电解容器，该电解器设置于支架上并连接该分岔管，该电解容器设置于支架上并连接该电解器，且该电解容器中容装电解液，该电解器可将该电解液电解成为氢气及氧气；
一超微气泡制成单元，该超微气泡制成单元设置于该储存单元的支架上，该超微气泡制成单元包含两个逆渗透泵组、一合并管、一压力均匀混合桶及一循环管，该两个逆渗透泵组连接该分岔管的两个入水管，该两个逆渗透泵组均连接该合并管，该合并管连接该两个逆渗透泵组及该压力均匀混合桶，该压力均匀混合桶设置于该支架上，该循环管连接该压力均匀混合桶并伸入该储存槽内，该储存单元及该超微气泡制成单元形成一循环系统。
本技术方案的电解氢氧超微气泡装置借由该超微气泡制成单元的逆渗透泵组，在该储存槽的水流入该超微气泡制成单元前，该入气管会输入空气让水中混有空气，含有空气的水被送入该两个入水管而进入该两个逆渗透泵组时，该两个逆渗透泵组让水中的氢气及氧气压缩破裂并减小变成细微气泡，并且该储存单元及该超微气泡制成单元形成一循环系统，让水中的氢气及氧气压缩破裂形成直径为0.2微米的超微气泡，可杀死水中0.2微米大小的微生物、细菌或污染物等混合物，并且由该电解器制造出的氢气，让氢气超微气泡达到抑菌及灭菌的效果，达到杀菌的实用性以及提升功能的多样性。
附图说明
图1为本发明电解氢氧超微气泡装置的一较佳实施例的侧视示意图。
图2为本发明电解氢氧超微气泡装置的一较佳实施例的操作态样的侧视示意图。
图3为本发明电解氢氧超微气泡装置的一较佳实施例的操作态样的局部放大的侧视示意图。
附图中的符号说明：
10储存单元；11支架；12储存槽；121填装管；122完成管；13分岔管；14气体流量计；15入气管；16入水管；17空气泵浦；18过滤器；20电解单元；21电解器；22电解容器；23补充泵；24补充槽；30超微气泡制成单元；31逆渗透泵组；32合并管；33压力均匀混合桶；34循环管；35第一逆渗透泵；36第二逆渗透泵；40冷却单元；41冷媒盘管；42隔温层；43冷却机；50水。
具体实施方式
如图1至图3所示，是揭示本发明电解氢氧超微气泡装置的一较佳实施例，由图式可知，本发明电解氢氧超微气泡装置包含一储存单元10、一电解单元20及一超微气泡制成单元30。
该储存单元10包含一支架11、一储存槽12、一分岔管13、一气体流量计14及一入气管15，该储存槽12设置于该支架11上，该分岔管13连通该储存槽12并分岔为两个入水管16，该气体流量计14设置于该支架11上，该入气管15设置于该支架11上并经该气体流量计14而连通该分岔管13，该入气管15的管径小于该分岔管13的管径，其中，该储存单元10包含一空气泵浦17及一过滤器18，该空气泵浦17设置于该支架11上并连接该入水管16及该储存槽12，该过滤器18设置于该支架11上，该储存槽12通过该过滤器18连通该分岔管13并于过滤器18的后方分岔出两个入水管16，进一步，该储存槽12具有一填装管121及一完成管122，该填装管121及该完成管122皆设置于该储存槽12上并连通该储存槽12。
该电解单元20设置于该支架11上并连通该分岔管13，该电解单元20包含一电解器21及一电解容器22，该电解器21设置于支架11上并连接该分岔管13，该电解容器22设置于支架11上并连接该电解器21，且该电解容器22中容装电解液，该电解器21可将电解液电解成为氢气及氧气，其中，该电解单元20包含一补充泵23及一补充槽24，该补充泵23设置于该支架11上并连通该电解容器22，该补充槽24设置于该支架11上并连通该补充泵23，该补充槽24中容装电解液。
该超微气泡制成单元30设置于该储存单元10的支架11上，该超微气泡制成单元30包含两个逆渗透泵组31、一合并管32、一压力均匀混合桶33及一循环管34，该两个逆渗透泵组31连接该分岔管13的两个入水管16，该合并管32连接该两个逆渗透泵组31及该压力均匀混合桶33，该压力均匀混合桶33设置于该支架11上，该循环管34连接该压力均匀混合桶33并伸入该储存槽12内，该储存单元10及该超微气泡制成单元30形成一循环系统，其中，每一逆渗透泵组31包含一第一逆渗透泵35及一第二逆渗透泵36，两个该第一逆渗透泵35连接该分岔管13的两个入水管16，两个该第一逆渗透泵35连接两个该第二逆渗透泵36，使得每一第一逆渗透泵35与对应连接的该第二逆渗透泵36形成串联，两个该第二逆渗透泵36均连接该合并管32。
进一步，如图1所示，该电解氢氧超微气泡装置包含一冷却单元40，该冷却单元40包含一冷媒盘管41、一隔温层42及一冷却机43，该冷媒盘管41设置于该储存槽12的外侧，该冷媒盘管41控制该储存槽12的温度介于10℃至20℃，该隔温层42设置于该冷煤盘管41的外侧，该隔温层42维持该冷媒盘管41调控的温度，该冷却机43连接该冷媒盘管41。
如图1至图3所示，是揭示本发明电解氢氧超微气泡装置的一较佳实施例，使用者可于该储存槽12的填装管121填装水50，让该储存槽12充满水50，接着开始进行制造氢氧超微气泡的作业，该储存槽12内的水50会从该分岔管13流经该过滤器18，在经过该过滤器18时将水50中的杂质清除掉，以确保进入该超微气泡制成单元30时不会让该两个逆渗透泵组31损坏，接着水50会从该分岔管13流入该两个入水管16并进入该两个逆渗透泵组31。
上述中，空气会流入该入气管15并经过该气体流量计14，使用者可通过控制该气体流量计14达到控制该入气管15内的空气的流量，空气会由该入气管15流入该分岔管13，因该入气管15的管径小于该分岔管13的管径，由柏努力定理可得知空气会被水50带往该两个入水管16，并且该电解单元20会通过该电解器21电解该电解容器22中的电解液，电解出氢气和氧气并输入该分岔管13，其中，该电解容器22中的电解液被电解后会逐渐减少，可通过该补充泵23运转，将该补充槽24中的电解液输送进该电解容器22中进行补充。
上述中，带有氢气及氧气的水50会进入该超微气泡制成单元30的该两个逆渗透泵组31，每一逆渗透泵组31皆包含一第一逆渗透泵35及一第二逆渗透泵36，带有氢气及氧气的水50会经过该第一逆渗透泵35，水50受到该第一逆渗透泵35的加压，让水50中的氢气及氧气受压而破裂减小变成细微的气泡，接着水50被加压输送至该第二逆渗透泵36，水50中的氢气及氧气又受到该第二逆渗透泵36的加压而破裂减小变成更细微的气泡，该第一逆渗透泵35及该第二逆渗透泵36形成串联，可让水50中的氢气及氧气受到加压的效应更强，压缩氢气及氧气破裂减小变成细微气泡的效果更好，受到该两个逆渗透泵组31加压的水50及细微气泡由该合并管32送进该压力均匀混合桶33，水50及细微气泡会在该压力均匀混合桶33中受到均匀压力挤压，进而产生混和均匀且含有氢气的微气泡及氧气的微气泡的液体，再由该循环管34输送含有氢气的微气泡及氧气的微气泡的液体回到该储存槽12，循环上述作业步骤5分钟，可产生直径为0.2微米(μm)氢氧气的超微气泡，该冷却单元40可保持该储存槽12中的超微气泡含量。
上述中，该电解氢氧超微气泡装置在循环上述作业步骤5分钟之后，直径为0.2微米氢氧气的超微气泡的液体会存放于该储存槽12，使用者可用该完成管122取得超微气泡的液体，并可用于农业灌溉、渔业养殖或食品加工等产业，因超微气泡的直径为0.2微米，超微气泡在崩解时所散发的能量，可杀死水中0.2微米的微生物、细菌或污染物等混合物，超微气泡崩解所散发的能量为物理性伤害而可达到物理性杀菌，并且由该电解器制造出的氢气及氧气，让超微气泡的气体有氧气也有氢气，在使用功能上，氢气超微气泡借由超微气泡崩解时产生超音波现象，并且具有负离子特性，进而达到抑菌及灭菌的效果，达到杀菌的实用性以及提升功能的多样性。
综上所述，本发明电解氢氧超微气泡装置借由该超微气泡制成单元30的逆渗透泵组31，将含有氢气及氧气的水50由该分岔管13送入该两个入水管16并进入该两个逆渗透泵组31时，该两个逆渗透泵组31让水50中的氢气及氧气压缩破裂减小变成细微气泡，并且该储存单元10及该超微气泡制成单元30形成一循环系统，让水50中的氢气及氧气循环形成直径为0.2微米的超微气泡，可杀死水50中0.2微米大小的微生物、细菌或污染物等混合物，并且由该电解 器21制造出的氢气，让氢气超微气泡达到抑菌及灭菌的效果，达到杀菌的实用性以及提升功能的多样性，并具有工业实用性。

Claims (7)

  1. 一种电解氢氧超微气泡装置，其中，包含：
    一储存单元，该储存单元包含一支架、一储存槽、一分岔管、一气体流量计及一入气管，该储存槽设置于该支架上，该分岔管连通该储存槽并分岔为两个入水管，该气体流量计设置于该支架上，该入气管设置于该支架上并经该气体流量计而连通该分岔管，该入气管的管径小于该分岔管的管径；
    一电解单元，该电解单元包含一电解器及一电解容器，该电解器设置于支架上并连接该分岔管，该电解容器设置于支架上并连接该电解器，且该电解容器中容装电解液，该电解器能够将该电解液电解成为氢气及氧气；以及
    一超微气泡制成单元，该超微气泡制成单元设置于该储存单元的支架上，该超微气泡制成单元包含两个逆渗透泵组、一合并管、一压力均匀混合桶及一循环管，该两个逆渗透泵组连接该分岔管的两个入水管，该合并管连接该两个逆渗透泵组及该压力均匀混合桶，该循环管连接该压力均匀混合桶并伸入该储存槽内，该储存单元及该超微气泡制成单元形成一循环系统。
  2. 如权利要求1所述的电解氢氧超微气泡装置，其中，每一逆渗透泵组包含一第一逆渗透泵及一第二逆渗透泵，两个该第一逆渗透泵连接该分岔管的两个入水管，两个该第一逆渗透泵连接两个该第二逆渗透泵，使得每一第一逆渗透泵与对应连接的该第二逆渗透泵形成串联，两个该第二逆渗透泵均连接该合并管。
  3. 如权利要求1所述的电解氢氧超微气泡装置，其中，该储存单元包含一空气泵浦及一过滤器，该空气泵浦设置于该支架上并连接该入水管及该储存槽，该过滤器设置于该支架上，该储存槽通过该过滤器连通该分岔管并于过滤器的后方分岔出两个入水管。
  4. 如权利要求2所述的电解氢氧超微气泡装置，其中，该储存单元包含一空气泵浦及一过滤器，该空气泵浦设置于该支架上并连接该入水管及该储存槽，该过滤器设置于该支架上，该储存槽通过该过滤器连通该分岔管并于过滤器的后方分岔出两个入水管。
  5. 如权利要求1至4中任一项所述的电解氢氧超微气泡装置，其中，该电解氢氧超微气泡装置包含一冷却单元，该冷却单元包含一冷媒盘管、一隔温层及一冷却机，该冷媒盘管设置于该储存槽的外侧，该隔温层设置于该冷煤盘管的外侧，该冷却机连接该冷媒盘管。
  6. 如权利要求1至4中任一项所述的电解氢氧超微气泡装置，其中，该电解单元包含一补充泵及一补充槽，该补充泵设置于该支架上并连通该电解容器，该补充槽设置于该支架上并连通该补充泵，该补充槽中容装电解液。
  7. 如权利要求5所述的电解氢氧超微气泡装置，其中，该电解单元包含一补充泵及一补充槽，该补充泵设置于该支架上并连通该电解容器，该补充槽设置于该支架上并连通该补充泵，该补充槽中容装电解液。
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CN1840231A (zh) * 2005-03-30 2006-10-04 株式会社日立制作所 超微细气泡的生成方法、生成装置、及利用其的杀菌·消毒设备
WO2015068989A1 (ko) * 2013-11-05 2015-05-14 대웅이엔에스(주) 초미세기포 발생장치 및 이를 갖는 수처리설비
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CN208229691U (zh) * 2018-03-06 2018-12-14 四季洋圃生物机电股份有限公司 超微氢气泡水制造装置

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CN1840231A (zh) * 2005-03-30 2006-10-04 株式会社日立制作所 超微细气泡的生成方法、生成装置、及利用其的杀菌·消毒设备
WO2015068989A1 (ko) * 2013-11-05 2015-05-14 대웅이엔에스(주) 초미세기포 발생장치 및 이를 갖는 수처리설비
CN208104016U (zh) * 2017-06-12 2018-11-16 大连双迪创新科技研究院有限公司 可产生富氢超微气泡水的洗浴装置
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