CN211078565U - Electrolytic hydrogen-oxygen ultramicro bubble device - Google Patents
Electrolytic hydrogen-oxygen ultramicro bubble device Download PDFInfo
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- CN211078565U CN211078565U CN201822251226.5U CN201822251226U CN211078565U CN 211078565 U CN211078565 U CN 211078565U CN 201822251226 U CN201822251226 U CN 201822251226U CN 211078565 U CN211078565 U CN 211078565U
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Abstract
The utility model discloses an electrolytic oxyhydrogen ultramicro bubble device, which comprises a storage unit, an electrolytic unit and an ultramicro bubble making unit, wherein the storage unit comprises a bracket, a storage tank, a branch pipe and an air inlet pipe, the storage tank is arranged on the bracket, the branch pipe is communicated with the storage tank and communicated with the air inlet pipe, the electrolytic unit is arranged on the bracket and connected with the branch pipe, the electrolytic unit can electrolyze hydrogen and oxygen, the ultramicro bubble making unit is arranged on the bracket and comprises two reverse osmosis pump sets connected with the branch pipe and a pressure uniform mixing barrel communicated with the two reverse osmosis pump sets, the electrolytic oxyhydrogen ultramicro bubble device of the utility model compresses and breaks the hydrogen and the oxygen in water into ultramicro bubbles with the diameter of 0.2 micron by the reverse osmosis pump sets, can eliminate the mixture of 0.2 micron, and the hydrogen electrolyzed by the electrolysis unit can inhibit bacteria and sterilize, and has the practicability and the function diversity of sterilization.
Description
Technical Field
The utility model relates to a microbubble device, in particular to an electrolytic oxyhydrogen ultramicro bubble device which uses an electrolyzer to generate hydrogen and oxygen and prepare ultramicro bubbles.
Background
The microbubbles are fine bubbles, common microbubble devices in the market can usually produce bubbles with the diameter of about 50 microns, after the microbubbles produced by the microbubble devices are injected into water, because the diameters of the microbubbles are in the micron level, the residence time of the microbubbles in the water is longer than that of the bubbles with the diameters in the millimeter level, so that the water can be cloudy and white, the water with the microbubbles can destroy and kill the mixture of microorganisms, bacteria or pollutants in the water by the energy emitted by the breaking and disintegrating of the microbubbles, and the physical sterilization can be achieved by the physical damage of the energy emitted by the breaking and disintegrating of the microbubbles.
The existing micro bubble device uses an impeller pump to deliver water mixed with air, the impeller pump includes a pump housing and a blade, the pump housing has a rotation space, a water inlet, an air inlet and an outlet, the rotation space is formed inside the pump housing, the water inlet is formed inside the pump housing and is communicated with the rotation space, the air inlet is formed inside the pump housing and is communicated with the water inlet, the outlet is formed inside the pump housing and is communicated with the rotation space, the blade is rotatably disposed in the rotation space of the pump housing, during delivery, the water input from the water inlet and the air input from the air inlet are rotationally hit by the blade of the impeller pump, so that the hydrogen and oxygen in water are hit by the blade to break the air, and further fine bubbles are generated.
However, the diameter of the bubbles produced by the impeller pump of the existing micro-bubble device is about 50 microns, the bubbles produced by the micro-bubble device only maintain the level of micron diameter, and the micro-bubble device cannot kill microorganisms with the diameter smaller than 50 microns, so the micro-bubble device is limited in the effect of killing bacteria at present, and the air input by the air inlet is general air in the process of producing micro-bubbles, and has no special efficacy no matter in agricultural irrigation, fishery culture or food processing, thereby causing the problem of insufficient functionality of the micro-bubble device.
SUMMERY OF THE UTILITY MODEL
The main objective of this technical scheme is to provide an electrolytic hydrogen oxygen ultramicro bubble device to improve the problem that the existing microbubble device can only produce microbubbles with a diameter of about 50 microns, and cannot kill microorganisms finer than 50 microns, which causes poor sterilization effect, and the problem that microbubbles are made of common air and have no additional effect, which causes insufficient functionality of the microbubble device.
In order to achieve the above purpose, the electrolytic hydrogen-oxygen ultramicro bubble device of the technical scheme comprises:
the storage unit comprises a support, a storage tank, a branch pipe, a gas flowmeter and a gas inlet pipe, wherein the storage tank is arranged on the support, the branch pipe is communicated with the storage tank and is branched into two water inlet pipes, the gas flowmeter is arranged on the support, the gas inlet pipe is arranged on the support and is communicated with the branch pipe through the gas flowmeter, and the pipe diameter of the gas inlet pipe is smaller than that of the branch pipe;
the electrolysis unit is arranged on the bracket and communicated with the branch pipe, the electrolysis unit comprises an electrolyzer and an electrolysis container, the electrolyzer is arranged on the bracket and connected with the branch pipe, the electrolysis container is arranged on the bracket and connected with the electrolyzer, and the electrolysis container contains electrolyte which can be electrolyzed into hydrogen and oxygen;
the ultramicro bubble making unit is arranged on a support of the storage unit and comprises two reverse osmosis pump sets, a merging pipe, a pressure uniform mixing barrel and a circulating pipe, the two reverse osmosis pump sets are connected with two water inlet pipes of the branch pipe, the two reverse osmosis pump sets are connected with the merging pipe, the merging pipe is connected with the two reverse osmosis pump sets and the pressure uniform mixing barrel, the pressure uniform mixing barrel is arranged on the support, the circulating pipe is connected with the pressure uniform mixing barrel and extends into the storage tank, and the storage unit and the ultramicro bubble making unit form a circulating system.
The electrolytic oxyhydrogen ultramicro bubble device of the technical proposal utilizes the reverse osmosis pump group of the ultramicro bubble making unit, before the water in the storage tank flows into the ultramicro bubble making unit, the air inlet pipe can input air to mix air in the water, when the water containing air is sent into the two water inlet pipes and enters the two reverse osmosis pump groups, the two reverse osmosis pump sets compress and break hydrogen and oxygen in water and reduce the hydrogen and oxygen into fine bubbles, and the storage unit and the ultramicro bubble making unit form a circulating system, so that hydrogen and oxygen in the water are compressed and broken to form ultramicro bubbles with the diameter of 0.2 micron, and the mixture of microorganisms, bacteria or pollutants with the size of 0.2 micron in the water can be killed, moreover, the hydrogen produced by the electrolyzer enables the hydrogen ultramicro bubbles to achieve the effects of bacteriostasis and sterilization, thereby achieving the practicability of sterilization and improving the diversity of functions.
Drawings
FIG. 1 is a schematic side view of the apparatus for electrolyzing oxyhydrogen ultra-micro bubbles according to a preferred embodiment of the present invention.
FIG. 2 is a schematic side view of an operation mode of the ultra-micro bubble apparatus for electrolyzing oxyhydrogen according to a preferred embodiment of the present invention.
FIG. 3 is a partially enlarged schematic side view of an operation mode of the ultra-micro bubble device for electrolyzing oxyhydrogen according to a preferred embodiment of the present invention.
Symbolic illustration in the drawings:
10 a storage unit; 11 a support; 12 a storage tank; 121 filling a tube; 122 completing the tube; 13 branch pipes; 14 a gas flow meter; 15 into the trachea; 16 water inlet pipes; 17 air pumping; 18 a filter; 20 an electrolysis unit; 21 an electrolyzer; 22 an electrolysis vessel; 23 a supplementary pump; 24 a replenishment tank; 30 ultramicro bubbles are made into a unit; 31 a reverse osmosis pump unit; 32 merging pipes; 33, a pressure uniform mixing barrel; 34 a circulation pipe; 35 a first reverse osmosis pump; 36 a second reverse osmosis pump; 40 a cooling unit; 41 refrigerant coil pipe; 42 a thermal insulation layer; 43 a cooling machine; 50 parts of water.
Detailed Description
Referring to fig. 1 to 3, a preferred embodiment of the present invention is disclosed, wherein the present invention provides an apparatus for electrolyzing oxyhydrogen ultra-micro bubbles, which comprises a storage unit 10, an electrolysis unit 20 and an ultra-micro bubble producing unit 30.
The storage unit 10 comprises a support 11, a storage tank 12, a branch pipe 13, a gas flow meter 14 and a gas inlet pipe 15, the storage tank 12 is disposed on the support 11, the branch pipe 13 is communicated with the storage tank 12 and is branched into two water inlet pipes 16, the gas flow meter 14 is disposed on the support 11, the gas inlet pipe 15 is disposed on the support 11 and is communicated with the branch pipe 13 through the gas flow meter 14, the pipe diameter of the gas inlet pipe 15 is smaller than that of the branch pipe 13, wherein the storage unit 10 comprises an air pump 17 and a filter 18, the air pump 17 is disposed on the support 11 and is connected with the water inlet pipe 16 and the storage tank 12, the filter 18 is disposed on the support 11, the storage tank 12 is communicated with the branch pipe 13 through the filter 18 and is provided with the two water inlet pipes 16 behind the filter 18, further, the storage tank 12 has a branched filling pipe 121 and a finishing pipe 122, the filling pipe 121 and the finishing pipe 122 are both disposed on the storage tank 12 and communicate with the storage tank 12.
The electrolysis unit 20 is disposed on the bracket 11 and communicated with the branch pipe 13, the electrolysis unit 20 includes an electrolyzer 21 and an electrolysis container 22, the electrolyzer 21 is disposed on the bracket 11 and connected with the branch pipe 13, the electrolysis container 22 is disposed on the bracket 11 and connected with the electrolyzer 21, and the electrolysis container 22 contains an electrolyte, the electrolysis container 21 can electrolyze the electrolyte into hydrogen and oxygen, wherein the electrolysis unit 20 includes a supplementary pump 23 and a supplementary tank 24, the supplementary pump 23 is disposed on the bracket 11 and communicated with the electrolysis container 22, the supplementary tank 24 is disposed on the bracket 11 and communicated with the supplementary pump 23, and the supplementary tank 24 contains the electrolyte.
The microbubble generating unit 30 is disposed on the support 11 of the storage unit 10, the microbubble generating unit 30 includes two reverse osmosis pump sets 31, a combining pipe 32, a pressure homogenizing mixing barrel 33 and a circulating pipe 34, the two reverse osmosis pump sets 31 are connected to the two water inlet pipes 16 of the branch pipe 13, the combining pipe 32 is connected to the two reverse osmosis pump sets 31 and the pressure homogenizing mixing barrel 33, the pressure homogenizing mixing barrel 33 is disposed on the support 11, the circulating pipe 34 is connected to the pressure homogenizing mixing barrel 33 and extends into the storage tank 12, the storage unit 10 and the microbubble generating unit 30 form a circulating system, wherein each reverse osmosis pump set 31 includes a first reverse osmosis pump 35 and a second reverse osmosis pump 36, the two first reverse osmosis pumps 35 are connected to the two water inlet pipes 16 of the branch pipe 13, the two first reverse osmosis pumps 35 are connected to the two second reverse osmosis pumps 36, so that each first reverse osmosis pump 35 is connected in series with the corresponding second reverse osmosis pump 36, and both second reverse osmosis pumps 36 are connected to the merging pipe 32.
Further, as shown in fig. 1, the oxyhydrogen electrolysis ultramicro-bubble device includes a cooling unit 40, the cooling unit 40 includes a cooling medium coil 41, a heat insulation layer 42 and a cooling machine 43, the cooling medium coil 41 is disposed outside the storage tank 12, the cooling medium coil 41 controls the temperature of the storage tank 12 to be 10 ℃ to 20 ℃, the heat insulation layer 42 is disposed outside the cool coal coil 41, the heat insulation layer 42 maintains the temperature regulated by the cooling medium coil 41, and the cooling machine 43 is connected to the cooling medium coil 41.
Referring to fig. 1 to 3, in order to disclose a preferred embodiment of the present invention, a user can fill water 50 in the filling pipe 121 of the storage tank 12, fill the storage tank 12 with water 50, and then start the operation of producing ultra-micro bubbles of hydrogen and oxygen, the water 50 in the storage tank 12 will flow through the filter 18 from the branch pipe 13, and the impurities in the water 50 will be removed when passing through the filter 18, so as to ensure that the two reverse osmosis pump sets 31 will not be damaged when entering the ultra-micro bubble producing unit 30, and then the water 50 will flow into the two water inlet pipes 16 from the branch pipe 13 and enter the two reverse osmosis pump sets 31.
In the above, the air will flow into the air inlet pipe 15 and pass through the gas flow meter 14, 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 pipe 13 from the air inlet pipe 15, because the pipe diameter of the air inlet pipe 15 is smaller than that of the branch pipe 13, the air will be carried to the two water inlet pipes 16 by the water 50 according to the boldi theorem, and the electrolysis unit 20 will electrolyze the electrolyte in the electrolysis container 22 by the electrolysis device 21, electrolyze the hydrogen and oxygen and input the hydrogen and oxygen into the branch pipe 13, wherein the electrolyte in the electrolysis container 22 will gradually decrease after being electrolyzed, and the electrolyte in the replenishment tank 24 can be input into the electrolysis container 22 for replenishment by the operation of the replenishment pump 23.
The water 50 with hydrogen and oxygen enters the two reverse osmosis pump sets 31 of the microbubble generating unit 30, each reverse osmosis pump set 31 comprises a first reverse osmosis pump 35 and a second reverse osmosis pump 36, the water 50 with hydrogen and oxygen passes through the first reverse osmosis pump 35, the water 50 is pressurized by the first reverse osmosis pump 35, the hydrogen and oxygen in the water 50 are pressurized to be broken and reduced into fine bubbles, then the water 50 is pressurized and conveyed to the second reverse osmosis pump 36, the hydrogen and oxygen in the water 50 are pressurized by the second reverse osmosis pump 36 to be broken and reduced into finer bubbles, the first reverse osmosis pump 35 and the second reverse osmosis pump 36 are connected in series, the effect of pressurizing the hydrogen and oxygen in the water 50 is stronger, the effect of breaking and reducing the compressed hydrogen and oxygen into fine bubbles is better, and the water 50 and fine bubbles pressurized by the two reverse osmosis pump sets 31 are conveyed into the pressure uniform mixing barrel 32 by the combining pipe 32 33, the water 50 and the fine bubbles are uniformly pressed in the pressure-uniform mixing barrel 33 to generate a liquid which is uniformly mixed and contains microbubbles of hydrogen and microbubbles of oxygen, and the liquid containing microbubbles of hydrogen and microbubbles of oxygen is sent back to the storage tank 12 by the circulation pipe 34, and the operation steps are circulated for 5 minutes to generate ultra-fine bubbles of hydrogen and oxygen with a diameter of 0.2 micrometer (mum), and the cooling unit 40 can maintain the content of the ultra-fine bubbles in the storage tank 12.
In the above, after the operation steps are circulated for 5 minutes, the liquid of the ultra-micro bubbles with the diameter of 0.2 micron oxyhydrogen gas can be stored in the storage tank 12, and the user can use the finishing pipe 122 to obtain the liquid of the ultra-micro bubbles, and can be used in the industries of agricultural irrigation, fishery culture or food processing, etc., because the diameter of the ultra-micro bubbles is 0.2 micron, the energy emitted by the ultra-micro bubbles during disintegration can kill 0.2 micron of mixture of microorganism, bacteria or pollutants, etc. in water, the energy emitted by the ultra-micro bubbles disintegration can achieve physical sterilization for physical damage, and the hydrogen and oxygen produced by the electrolyzer can make the gas of the ultra-micro bubbles have oxygen and hydrogen, in terms of use function, the hydrogen ultra-micro bubbles generate ultrasonic wave phenomenon during disintegration by the ultra-micro bubbles, and have negative ion characteristics, thereby achieving the effects of bacteriostasis and sterilization, the practicability of sterilization and the diversity of the promotion function are achieved.
To sum up, the utility model discloses electrolysis oxyhydrogen ultramicro bubble device borrows by this hyperfine bubble to make the reverse osmosis pump package 31 of unit 30, when sending into these two oral siphon 16 and entering these two hyperfine pump packages 31 by this branch pipe 13 with the water 50 that contains hydrogen and oxygen, these two reverse osmosis pump packages 31 let hydrogen and oxygen compression fracture in water 50 reduce and become the fine bubble, and this storage unit 10 and this hyperfine bubble make unit 30 form a circulation system, let hydrogen and oxygen circulation in water 50 form the diameter and be 0.2 micron's hyperfine bubble, can kill 0.2 micron's mixture such as little organism, bacterium or pollutant in water 50, and the hydrogen that produces by this electrolyser 21, let hydrogen hyperfine bubble reach antibacterial and sterile effect, reach the practicality of disinfecting and promote the diversity of function.
Claims (7)
1. An electrolytic oxyhydrogen microbubble device, characterized by comprising:
the storage unit comprises a support, a storage tank, a branch pipe, a gas flowmeter and a gas inlet pipe, wherein the storage tank is arranged on the support, the branch pipe is communicated with the storage tank and is branched into two water inlet pipes, the gas flowmeter is arranged on the support, the gas inlet pipe is arranged on the support and is communicated with the branch pipe through the gas flowmeter, and the pipe diameter of the gas inlet pipe is smaller than that of the branch pipe;
the electrolytic unit comprises an electrolyzer and an electrolytic container, the electrolyzer is arranged on the bracket and connected with the branch pipe, the electrolytic container is arranged on the bracket and connected with the electrolyzer, electrolyte is contained in the electrolytic container, and the electrolyzer can electrolyze the electrolyte into hydrogen and oxygen; and
the ultramicro bubble making unit is arranged on a support of the storage unit and comprises two reverse osmosis pump sets, a merging pipe, a pressure uniform mixing barrel and a circulating pipe, the two reverse osmosis pump sets are connected with two water inlet pipes of the branch pipe, the merging pipe is connected with the two reverse osmosis pump sets and the pressure uniform mixing barrel, the circulating pipe is connected with the pressure uniform mixing barrel and extends into the storage tank, and the storage unit and the ultramicro bubble making unit form a circulating system.
2. The apparatus of claim 1, wherein each reverse osmosis pump set comprises a first reverse osmosis pump and a second reverse osmosis pump, two first reverse osmosis pumps are connected to two water inlets of the branch pipe, two first reverse osmosis pumps are connected to two second reverse osmosis pumps, such that each first reverse osmosis pump is connected in series with the corresponding second reverse osmosis pump, and both second reverse osmosis pumps are connected to the merging pipe.
3. The apparatus of claim 1, wherein the storage unit comprises an air pump and a filter, the air pump is disposed on the frame and connected to the water inlet pipe and the storage tank, the filter is disposed on the frame, and the storage tank is connected to the branch pipe via the filter and branches into two water inlet pipes at the rear of the filter.
4. The apparatus of claim 2, wherein the storage unit comprises an air pump and a filter, the air pump is disposed on the frame and connected to the water inlet pipe and the storage tank, the filter is disposed on the frame, and the storage tank is connected to the branch pipe via the filter and branches into two water inlet pipes at the rear of the filter.
5. The oxyhydrogen microbubble device according to any one of claims 1 to 4, wherein the oxyhydrogen microbubble device comprises a cooling unit, the cooling unit comprises a cooling medium coil, a heat insulation layer and a cooler, the cooling medium coil is disposed outside the storage tank, the heat insulation layer is disposed outside the cooling medium coil, and the cooler is connected to the cooling medium coil.
6. The apparatus of any one of claims 1-4, wherein the electrolysis unit comprises a replenishing pump and a replenishing tank, the replenishing pump is disposed on the frame and connected to the electrolysis vessel, the replenishing tank is disposed on the frame and connected to the replenishing pump, and the replenishing tank contains electrolyte.
7. The apparatus of claim 5, wherein the electrolysis unit comprises a replenishing pump and a replenishing tank, the replenishing pump is disposed on the frame and connected to the electrolysis vessel, the replenishing tank is disposed on the frame and connected to the replenishing pump, and the replenishing tank contains an electrolyte.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201822251226.5U CN211078565U (en) | 2018-12-29 | 2018-12-29 | Electrolytic hydrogen-oxygen ultramicro bubble device |
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| CN201822251226.5U CN211078565U (en) | 2018-12-29 | 2018-12-29 | Electrolytic hydrogen-oxygen ultramicro bubble device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111377505A (en) * | 2018-12-29 | 2020-07-07 | 四季洋圃生物机电股份有限公司 | Electrolytic hydrogen-oxygen ultramicro bubble device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111377505A (en) * | 2018-12-29 | 2020-07-07 | 四季洋圃生物机电股份有限公司 | Electrolytic hydrogen-oxygen ultramicro bubble device |
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