CN111302454A - Oxyhydrogen ultramicro bubble device - Google Patents
Oxyhydrogen ultramicro bubble device Download PDFInfo
- Publication number
- CN111302454A CN111302454A CN201811515593.XA CN201811515593A CN111302454A CN 111302454 A CN111302454 A CN 111302454A CN 201811515593 A CN201811515593 A CN 201811515593A CN 111302454 A CN111302454 A CN 111302454A
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- Prior art keywords
- reverse osmosis
- pipe
- ultra
- fine
- storage tank
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
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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
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/60—Pump mixers, i.e. mixing within a pump
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/26—Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention provides a hydrogen-oxygen ultramicro bubble device, which comprises a storage unit, an ultramicro bubble making unit and a pressure uniform mixing 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 bypasses the air inlet pipe, the ultramicro bubble making unit is arranged on the bracket and comprises two reverse osmosis pump sets, the two reverse osmosis pump sets are respectively connected with the branch pipe, and the pressure uniform mixing unit is arranged on the bracket, is connected with the two reverse osmosis pump sets and the storage tank and comprises a plurality of magnesium particles.
Description
Technical Field
The invention relates to an oxyhydrogen Ultra Fine Bubble (UFB) device, in particular to an oxyhydrogen Ultra Fine Bubble device for preparing Ultra Fine bubbles to achieve a good sterilization effect.
Background
Microbubbles are bubbles with small diameter, common microbubble devices in the market can usually produce bubbles with diameter of about 50 microns, after the microbubbles produced by the microbubble devices are injected into water, because the diameters of the bubbles are micron, the residence time of the microbubbles in the water is longer than that of the bubbles with diameter of millimeter, the residence time of the microbubbles in the water is longer, so that the water can be cloudy white, the water with the microbubbles can emit energy when breaking and disintegrating through the microbubbles, so that the mixture of microorganisms, bacteria or pollutants and the like in the water can be destroyed and destroyed by the disintegration of the microbubbles, the energy emitted by the disintegration of the microbubbles can be physically damaged to achieve physical sterilization, and the water using the microbubble devices is used in industries such as agricultural irrigation, fishery culture or food processing at present.
In the conventional micro bubble device, water mixed with air is delivered by an impeller pump, the impeller pump includes a pump housing and a vane, 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 in the pump housing and communicated with the rotation space, the air inlet is formed in the pump housing and communicated with the water inlet, the outlet is formed in the pump housing and communicated with the rotation space, the vane is rotatably disposed in the rotation space of the pump housing, and in the delivery process, the water input from the water inlet and the air input from the air inlet enable the vane of the impeller pump to rotate and strike, so that hydrogen and oxygen in water are struck by the vane to break the air, thereby generating fine bubbles.
However, the diameter of the bubbles produced by the impeller pump of the existing micro-bubble device is about 50 microns when the impeller pump of the micro-bubble device is hit, the bubbles produced by the micro-bubble device maintain the size of micron diameter, and the micro-bubble device cannot kill microorganisms smaller than 50 microns, so that 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, so that the problem of insufficient functionality of the micro-bubble device is caused.
Disclosure of Invention
The main objective of the present invention is to provide an oxyhydrogen micro bubble device, which can improve the problems that the existing micro bubble device can only produce micro bubbles with a diameter of about 50 microns, and can not kill microorganisms finer than 50 microns, resulting in poor sterilization effect, and that the micro bubbles are made of common air, and have no additional effect, resulting in insufficient functionality of the micro bubble device.
To achieve the above object, the present invention provides an apparatus for producing ultrafine hydrogen-oxygen bubbles, 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, flows through the gas flowmeter and is communicated with the branch pipe, and the pipe diameter of the gas inlet pipe is smaller than that of the branch pipe;
the ultra-fine bubble making unit is arranged on a bracket of the storage unit and comprises two reverse osmosis pump sets and a merging pipe, the two reverse osmosis pump sets are respectively connected with two water inlet pipes of the branch pipe, and the two reverse osmosis pump sets are respectively connected with the merging pipe; and
the pressure uniform mixing unit is arranged on the support and connected with the merging pipe, the pressure uniform mixing unit comprises a mixing barrel, a plurality of magnesium particles and a circulating pipe, the mixing barrel is arranged on the support and connected with the merging pipe, the plurality of magnesium particles are arranged in the mixing barrel, the circulating pipe is connected with the mixing barrel and extends into the storage tank, and the storage unit, the ultra-fine bubble making unit and the pressure uniform mixing unit form a circulating system.
The oxyhydrogen ultrafine bubble device of the invention uses the reverse osmosis pump group of the ultrafine bubble making unit, before the water in the storage tank flows into the ultrafine bubble making unit, the air inlet pipe can input air to mix air with 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 groups compress and break the hydrogen and oxygen in the water to reduce the pressure and break the hydrogen and oxygen into fine bubbles, and the storage unit, the ultrafine bubble making unit and the pressure uniform mixing unit form a circulating system, so that the hydrogen and oxygen in the water are compressed and broken to form ultrafine bubbles with the diameter of 0.2 micron, the mixture of microorganisms, bacteria or pollutants with the size of 0.2 micron in the water can be killed, and the hydrogen chemically reacted by a plurality of magnesium particles enables the hydrogen ultrafine bubbles to achieve the effects of bacteriostasis and sterilization, the practicability of sterilization and the diversity of the promotion function are achieved.
Drawings
FIG. 1 is a schematic side view of an apparatus for producing ultra-fine hydrogen-oxygen bubbles according to a preferred embodiment of the present invention.
FIG. 2 is a schematic side view of an operation mode of the oxyhydrogen microbubble device according to a preferred embodiment of the present invention.
FIG. 3 is a partially enlarged side view of the operation of the oxyhydrogen microbubble device according to a preferred embodiment of the present invention.
Detailed Description
Referring to FIG. 1, there is shown a preferred embodiment of the apparatus for producing ultra fine hydrogen-oxygen bubbles according to the present invention, which comprises a storage unit 10, an ultra fine bubble producing unit 20, and a pressure homogenizing and mixing unit 30.
As shown in fig. 1 to 3, the storage unit 10 includes 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 branches 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 flows through the gas flow meter 14 and is communicated with the branch pipe 13, the pipe diameter of the gas inlet pipe 15 is smaller than that of the branch pipe 13, wherein the storage unit 10 includes an air pump 17 and a filter 18, the air pump 17 is disposed on the support 11 and is connected with the gas inlet pipe 15 and the storage tank 12, the filter 18 is disposed on the support 11, the branch pipe 13 is communicated with the filter 18 and branches into two water inlet pipes 16 behind the filter 18, further, the storage tank 12 has a filling pipe 121 and a finishing pipe 122, and both the filling pipe 121 and the finishing pipe 122 are disposed in the storage tank 12 and communicate with the storage tank 12.
As shown in fig. 1 and 2, the ultra-fine bubble making unit 20 is disposed on the support 11 of the storage unit 10, the ultra-fine bubble making unit 20 includes two reverse osmosis pump sets 21 and a combining pipe 22, the two reverse osmosis pump sets 21 are respectively connected to the two water inlet pipes 16 of the branch pipes 13, the two reverse osmosis pump sets 21 are respectively connected to the combining pipe 22, each reverse osmosis pump set 21 includes a first reverse osmosis pump 23 and a second reverse osmosis pump 24, the two first reverse osmosis pumps 23 are respectively connected to the two water inlet pipes 16 of the branch pipes 13, the two first reverse osmosis pumps 23 are respectively connected to the two second reverse osmosis pumps 24, such that each first reverse osmosis pump 23 and the correspondingly connected second reverse osmosis pump 24 are connected in series, and the two second reverse osmosis pumps 24 are respectively connected to the combining pipe 22.
As shown in fig. 1 to 3, the pressure homogenizing and mixing unit 30 is disposed on the support 11 and connected to the combining pipe 22, the pressure homogenizing and mixing unit 30 includes a mixing barrel 31, a plurality of magnesium particles 32, and a circulating pipe 33, the mixing barrel 31 is disposed on the support 11 and connected to the combining pipe 22, the plurality of magnesium particles 32 are disposed inside the mixing barrel 31, the circulating pipe 33 is connected to the mixing barrel 31 and extends into the storage tank 12, and the storage unit 10, the ultra-fine bubble making unit 20, and the pressure homogenizing and mixing unit 30 form a circulating system.
Further, as shown in fig. 1, the oxyhydrogen ultrafine bubble device includes a cooling unit 40, the cooling unit 40 includes a cooling medium coil 41, a heat insulating 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 insulating layer 42 is disposed outside the cooling medium coil, the heat insulating 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, a preferred embodiment of the apparatus for producing ultra fine hydrogen and oxygen bubbles according to the present invention is disclosed, wherein a user can fill the filling pipe 121 of the storage tank 12 with water 50, fill the storage tank 12 with water 50, then start the operation of producing ultra fine hydrogen and oxygen bubbles, the water 50 in the storage tank 12 flows through the branch pipe 13 via the filter 18, removes impurities in the water 50 while passing through the filter 18 to ensure that the two reverse osmosis pump sets 21 are not damaged when entering the ultra fine bubble producing unit 20, then the water 50 flows from the branch pipe 13 into the two water inlet pipes 16 and into the two reverse osmosis pump sets 21, and at the same time air flows into the air inlet pipe 15 and passes through the gas flow meter 14, so that the user can control the flow rate of air in the air inlet pipe 15 by controlling the gas flow meter 14, air flows into the branch pipe 13 through the air inlet pipe 15, and since the pipe diameter of the air inlet pipe 15 is smaller than that of the branch pipe 13, it is known from the Bernoulli theorem that the air is carried to the two water inlet pipes 16 by the water 50.
In the above, the water 50 with air enters the two reverse osmosis pump sets 21 of the ultra fine bubble making unit 20, the water 50 with air passes through the first reverse osmosis pump 23, the water 50 is pressurized by the first reverse osmosis pump 23, the air in the water 50 is pressurized to be broken and reduced into fine bubbles, then the water 50 is pressurized and conveyed to the second reverse osmosis pump 24, the air in the water 50 is pressurized by the second reverse osmosis pump 24 to be broken and reduced into finer bubbles, the first reverse osmosis pump 23 and the second reverse osmosis pump 24 are connected in series, the air in the water 50 is pressurized to be stronger, the compressed air is broken and reduced into fine bubbles to be more effective, the water 50 and the fine bubbles pressurized by the two reverse osmosis pump sets 21 are conveyed to the pressure uniform mixing unit 30 by the merging pipe 22, the water 50 and the fine bubbles enter the mixing tub 31, most of the magnesium particles 32 in the mixing barrel 31 meet the water 50, and generate a chemical reaction to generate hydrogen through activation, the water 50 and the fine bubbles are uniformly pressed and extruded in the mixing barrel 31, so as to generate a liquid for uniformly mixing the microbubbles containing hydrogen and the microbubbles containing oxygen, and the liquid containing the microbubbles containing hydrogen and the microbubbles containing oxygen is conveyed back to the storage tank 12 through the circulation pipe 33, and the above operation steps are circulated for 5 minutes, so as to generate ultra-fine bubbles of oxyhydrogen having a diameter of 0.2 micrometer (μm), and the cooling unit 40 can maintain the content of the ultra-fine bubbles in the storage tank 12.
In the above, after the oxyhydrogen ultra-fine bubble device circulates the above operation steps for 5 minutes, the liquid of ultra-fine bubbles of oxyhydrogen gas with a diameter of 0.2 μm is stored in the storage tank 12, and the user can obtain the liquid of ultra-fine bubbles through the finishing pipe 122, which can be used in the industries of agricultural irrigation, fishery culture, food processing, etc., because the diameter of ultra-fine bubbles is 0.2 μm, the energy emitted by the ultra-fine bubbles during disintegration can kill 0.2 μm of mixture of microorganisms, bacteria or pollutants, etc. in water, the energy emitted by the ultra-fine bubble disintegration can be physically damaged to achieve physical sterilization, and the hydrogen gas chemically reacted by the plurality of magnesium particles 32 allows the gas of the ultra-fine bubbles to have oxygen and hydrogen, and in terms of use, when the hydrogen ultra-fine bubbles are disintegrated through the ultra-fine bubbles, an ultrasonic phenomenon can be generated, and the hydrogen ultra-fine bubbles have a negative ion characteristic, thereby achieving the effects of bacteriostasis and sterilization, the practicability of sterilization and the diversity of the promotion function.
In conclusion, the apparatus for producing ultra-fine bubbles of hydrogen and oxygen of the present invention uses the reverse osmosis pump 21 of the ultra-fine bubble producing unit 20, when the water 50 containing air is fed from the branch pipe 13 into the two water inlet pipes 16 and into the two reverse osmosis pump units 21, the two reverse osmosis pump sets 21 allow the air in the water 50 to be compressed and broken down and reduced into fine air bubbles, and the storage unit 10, the ultra-fine bubble making unit 20 and the pressure homogenizing and mixing unit 30 form a circulation system, so that the oxygen and hydrogen are circularly broken and reduced to form ultra-fine bubbles with a diameter of 0.2 μm, can kill 0.2 micron-sized microorganisms, bacteria or pollutants in the water 50, and the hydrogen chemically reacted by the magnesium particles 32 enables the hydrogen ultra-fine bubbles to achieve the effects of bacteriostasis and sterilization, thereby achieving the practicability of sterilization and improving the diversity of functions.
Claims (7)
1. An oxyhydrogen ultra-fine bubble device, 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, flows through the gas flowmeter and is communicated with the branch pipe, and the pipe diameter of the gas inlet pipe is smaller than that of the branch pipe;
the ultra-fine bubble making unit is arranged on a bracket of the storage unit and comprises two reverse osmosis pump sets and a merging pipe, the two reverse osmosis pump sets are respectively connected with two water inlet pipes of the branch pipe, and the two reverse osmosis pump sets are respectively connected with the merging pipe; and
the pressure uniform mixing unit is arranged on the support and connected with the merging pipe, the pressure uniform mixing unit comprises a mixing barrel, a plurality of magnesium particles and a circulating pipe, the mixing barrel is arranged on the support and connected with the merging pipe, the plurality of magnesium particles are arranged in the mixing barrel, the circulating pipe is connected with the mixing barrel and extends into the storage tank, and the storage unit, the ultra-fine bubble making unit and the pressure uniform mixing unit form a circulating system.
2. The ultra-fine oxyhydrogen bubble generating apparatus according to claim 1, wherein each reverse osmosis pump set comprises a first reverse osmosis pump and a second reverse osmosis pump, the first reverse osmosis pumps are respectively connected to the two water inlets of the branch pipes, the first reverse osmosis pumps are respectively connected to the second reverse osmosis pumps, such that each first reverse osmosis pump is connected in series with the corresponding second reverse osmosis pump, and the second reverse osmosis pumps are respectively connected to the merging pipes.
3. The ultra-fine oxyhydrogen bubble apparatus according to claim 1, wherein the storage unit comprises an air pump disposed on the rack and connecting the inlet pipe and the storage tank.
4. The ultra-fine oxyhydrogen bubble apparatus according to claim 2, wherein the storage unit comprises an air pump disposed on the rack and connecting the inlet pipe and the storage tank.
5. The ultra-fine hydrogen-oxygen bubble device according to any one of claims 1 to 4, wherein the ultra-fine hydrogen-oxygen bubble device comprises a cooling unit, the cooling unit comprises a cooling medium coil, a heat insulating layer and a cooling machine, the cooling medium coil is disposed outside the storage tank, the heat insulating layer is disposed outside the cooling medium coil, and the cooling machine is connected to the cooling medium coil.
6. The ultrafine bubble apparatus according to any one of claims 1 to 4, wherein the storage unit comprises a filter provided in the holder, and the branch pipe is connected to the filter and branches into two water inlet pipes at the rear of the filter.
7. The ultra fine hydrogen and oxygen bubble apparatus according to claim 5, wherein the storage unit comprises a filter disposed in the holder, and the branch pipe is connected to the filter and branched to form two water inlet pipes at the rear of the filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811515593.XA CN111302454A (en) | 2018-12-12 | 2018-12-12 | Oxyhydrogen ultramicro bubble device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811515593.XA CN111302454A (en) | 2018-12-12 | 2018-12-12 | Oxyhydrogen ultramicro bubble device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111302454A true CN111302454A (en) | 2020-06-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811515593.XA Withdrawn CN111302454A (en) | 2018-12-12 | 2018-12-12 | Oxyhydrogen ultramicro bubble device |
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| Country | Link |
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| CN (1) | CN111302454A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111302453A (en) * | 2018-12-12 | 2020-06-19 | 四季洋圃生物机电股份有限公司 | Apparatus for electrolyzing ultra-fine bubbles of hydrogen and oxygen |
| CN111377510A (en) * | 2018-12-29 | 2020-07-07 | 四季洋圃生物机电股份有限公司 | Hydrogen-oxygen ultramicro bubble device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1840231A (en) * | 2005-03-30 | 2006-10-04 | 株式会社日立制作所 | Superfine air bubble generation method and device and sterilization device using same |
| CN105476480A (en) * | 2016-01-21 | 2016-04-13 | 茌平县蓝天使赤泥科技有限公司 | Micro-nano gas-liquid mixed hydrogen-rich water dispenser |
| TWM528784U (en) * | 2016-04-25 | 2016-09-21 | Fairy Water Ind Co Ltd | Water purifier structure with hydrogen |
| CN107912527A (en) * | 2017-11-03 | 2018-04-17 | 东莞市天恩奶业生态科技有限公司 | A kind of lactogenesis processing method |
| CN108411326A (en) * | 2018-06-04 | 2018-08-17 | 深圳市赫拉铂氢时代科技有限公司 | A kind of nano bubble electrolyzed water machine |
| CN108862536A (en) * | 2018-07-11 | 2018-11-23 | 王开明 | A kind of preparation method of the oxygen-containing hydrogeneous water of over-saturation |
| CN209428200U (en) * | 2018-12-12 | 2019-09-24 | 四季洋圃生物机电股份有限公司 | Hydrogen-oxygen superfine air bubble device |
-
2018
- 2018-12-12 CN CN201811515593.XA patent/CN111302454A/en not_active Withdrawn
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1840231A (en) * | 2005-03-30 | 2006-10-04 | 株式会社日立制作所 | Superfine air bubble generation method and device and sterilization device using same |
| CN105476480A (en) * | 2016-01-21 | 2016-04-13 | 茌平县蓝天使赤泥科技有限公司 | Micro-nano gas-liquid mixed hydrogen-rich water dispenser |
| TWM528784U (en) * | 2016-04-25 | 2016-09-21 | Fairy Water Ind Co Ltd | Water purifier structure with hydrogen |
| CN107912527A (en) * | 2017-11-03 | 2018-04-17 | 东莞市天恩奶业生态科技有限公司 | A kind of lactogenesis processing method |
| CN108411326A (en) * | 2018-06-04 | 2018-08-17 | 深圳市赫拉铂氢时代科技有限公司 | A kind of nano bubble electrolyzed water machine |
| CN108862536A (en) * | 2018-07-11 | 2018-11-23 | 王开明 | A kind of preparation method of the oxygen-containing hydrogeneous water of over-saturation |
| CN209428200U (en) * | 2018-12-12 | 2019-09-24 | 四季洋圃生物机电股份有限公司 | Hydrogen-oxygen superfine air bubble device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111302453A (en) * | 2018-12-12 | 2020-06-19 | 四季洋圃生物机电股份有限公司 | Apparatus for electrolyzing ultra-fine bubbles of hydrogen and oxygen |
| CN111377510A (en) * | 2018-12-29 | 2020-07-07 | 四季洋圃生物机电股份有限公司 | Hydrogen-oxygen ultramicro bubble device |
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Application publication date: 20200619 |