CN113041874A - Hydrogen water machine - Google Patents
Hydrogen water machine Download PDFInfo
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- CN113041874A CN113041874A CN202110519127.4A CN202110519127A CN113041874A CN 113041874 A CN113041874 A CN 113041874A CN 202110519127 A CN202110519127 A CN 202110519127A CN 113041874 A CN113041874 A CN 113041874A
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- water
- hydrogen
- gas
- pressure
- supply device
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 171
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 128
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 120
- 239000001257 hydrogen Substances 0.000 title claims abstract description 120
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 8
- 239000012528 membrane Substances 0.000 claims description 3
- 238000001223 reverse osmosis Methods 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 abstract description 7
- 239000002245 particle Substances 0.000 abstract description 6
- 230000014759 maintenance of location Effects 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 abstract description 3
- 230000002035 prolonged effect Effects 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 5
- 201000010099 disease Diseases 0.000 description 3
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 208000014674 injury Diseases 0.000 description 2
- 208000024827 Alzheimer disease Diseases 0.000 description 1
- 201000006474 Brain Ischemia Diseases 0.000 description 1
- 208000014644 Brain disease Diseases 0.000 description 1
- 208000001408 Carbon monoxide poisoning Diseases 0.000 description 1
- 206010008120 Cerebral ischaemia Diseases 0.000 description 1
- 206010011878 Deafness Diseases 0.000 description 1
- 201000004624 Dermatitis Diseases 0.000 description 1
- 208000032274 Encephalopathy Diseases 0.000 description 1
- 206010061218 Inflammation Diseases 0.000 description 1
- 206010033645 Pancreatitis Diseases 0.000 description 1
- 206010033647 Pancreatitis acute Diseases 0.000 description 1
- 208000018737 Parkinson disease Diseases 0.000 description 1
- 208000019155 Radiation injury Diseases 0.000 description 1
- 206010039966 Senile dementia Diseases 0.000 description 1
- 201000003229 acute pancreatitis Diseases 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 206010008118 cerebral infarction Diseases 0.000 description 1
- 231100000895 deafness Toxicity 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 208000016354 hearing loss disease Diseases 0.000 description 1
- 230000004054 inflammatory process Effects 0.000 description 1
- 208000028867 ischemia Diseases 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- -1 nitrite anions Chemical class 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 230000004792 oxidative damage Effects 0.000 description 1
- 210000001525 retina Anatomy 0.000 description 1
- 210000000813 small intestine Anatomy 0.000 description 1
- 208000020431 spinal cord injury Diseases 0.000 description 1
- 230000009885 systemic effect Effects 0.000 description 1
- 238000002054 transplantation Methods 0.000 description 1
- 208000001072 type 2 diabetes mellitus Diseases 0.000 description 1
Images
Classifications
-
- 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
- B01F25/64—Pump mixers, i.e. mixing within a pump of the centrifugal-pump type, i.e. turbo-mixers
- B01F25/641—Multi-staged turbo-mixers
-
- 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
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
-
- 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
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
- B01F23/23764—Hydrogen
-
- 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
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/51—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
-
- 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
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/52—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle with a rotary stirrer in the recirculation tube
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
Abstract
The invention relates to a hydrogen water machine which comprises a hydrogen gas supply device, a water supply device, a gas-liquid self-priming mixing pump, a one-way valve, a return pipe and a pressure water storage device, wherein the gas-liquid self-priming mixing pump is provided with a first gas suction port, a first water inlet and a first water outlet, the first gas suction port is communicated with the hydrogen gas supply device, a plurality of impellers for mixing hydrogen and water are arranged in the gas-liquid self-priming mixing pump, the pressure water storage device is provided with a return port, a second water outlet and a second water inlet, the second water inlet is communicated with the first water outlet, the return port is communicated with the first water inlet, and the first water inlet is communicated with the second. The hydrogen water machine is provided with a plurality of impellers in the gas-liquid self-priming mixing pump, so that the particle size of hydrogen bubbles is smaller, and the retention time of hydrogen dissolved in water is prolonged; through setting up the back flow, make pressure water storage device hydrogen water backward flow to the gas-liquid from inhaling the mixing pump in stir the mixture, promote the super high concentration of hydrogen in hydrogen water, maintain the dwell time of hydrogen in water.
Description
Technical Field
The invention relates to the technical field of hydrogen water machines, in particular to a hydrogen water machine.
Background
Numerous biological studies have shown that hydrogen has the effect of selectively neutralizing free radicals and nitrite anions, which underlies the treatment of diseases by hydrogen against oxidative damage. Studies show that the types of diseases treated by hydrogen energy are very many, such as 68 diseases including malignant tumors, colonitis, encephalopathy after carbon monoxide poisoning, cerebral ischemia, senile dementia, Parkinson's disease, depression, spinal cord injury, skin allergy, type 2 diabetes, acute pancreatitis, organ transplantation injury, small intestine ischemia, systemic inflammatory reaction, radiation injury, retina injury, deafness and the like.
The current conventional mode of intake is by drinking ultra-high concentration hydrogen water. The solubility of saturated hydrogen-rich water hydrogen under the general state is 1.608ppm, and the solubility of hydrogen produced by a pressure hydrogen water machine on the market is 2-4.5 ppm. Chinese patent CN108946906A discloses a pressure electrolysis ultrahigh concentration hydrogen water machine, which is provided with a pressure container to pressurize the initially fed water or the electrolyzed water, then the water enters an electrolytic cell after the hydrogen solubility is improved, and the hydrogen solubility in the water can be improved by multiple pressurization cycles in the electrolysis process, wherein the hydrogen solubility can reach 3-5 ppm. Chinese patent CN106512764A discloses a hydrogen water machine, which can utilize a mixing device and a return pipe to dissolve hydrogen in water supplied by a water supply device to form hydrogen water output, and the hydrogen water part flows back via the return pipe and is treated by the mixing device again, so under the effect of repeated circulation, the concentration of hydrogen dissolved in water in hydrogen water is improved, and the retention time of hydrogen dissolved in water is maintained at the same time.
The technology solves the problem of low hydrogen solubility in the prior art, but in the practical use process, the hydrogen water with ultrahigh concentration is just milky, and the hydrogen water gradually changes into the color of the conventional water along with the rapid escape (about 5 seconds) of the hydrogen after separation, so that the hydrogen content in the hydrogen water is greatly reduced. Therefore, how to increase the mixing effect of hydrogen and water in the ultra-high concentration hydrogen water and stabilize the hydrogen concentration of the output hydrogen water is an urgent problem to be solved.
Disclosure of Invention
In view of this, it is necessary to provide a hydrogen water machine capable of prolonging the duration of the hydrogen concentration of the hydrogen water after output, in order to solve the problem that the hydrogen concentration of the hydrogen water of the ultra-high concentration is reduced by rapidly escaping after separation.
A hydrogen water machine comprising a hydrogen gas supply device for supplying hydrogen gas, a water supply device for supplying pure water, a gas-liquid self-priming mixing pump, a check valve, a return pipe, and a pressure water storage device,
the gas-liquid self-priming mixing pump is provided with a first gas suction port, a first water inlet and a first water outlet, the first gas suction port is communicated with the hydrogen supply device, a plurality of impellers for mixing hydrogen and water are arranged in the gas-liquid self-priming mixing pump,
the pressure water storage device is used for storing hydrogen water, the pressure water storage device is provided with backward flow mouth, second delivery port and second water inlet, the second water inlet with first delivery port intercommunication, the backward flow mouth with first water inlet intercommunication, first water inlet passes through the check valve with the second water inlet communicates along rivers direction in proper order, the second delivery port is used for exporting hydrogen water.
In one embodiment, the check valve is provided with a second suction port communicating with the hydrogen supply device, a third water inlet communicating with the water supply device, and a third water outlet communicating with the first water inlet.
In one embodiment, the ratio of the hydrogen supply amount of the first air suction port to the hydrogen supply amount of the second air suction port is 2: 1-3: 2.
In one embodiment, a pressure sensor for sensing the pressure is arranged in the pressure water storage device, the return pipe is provided with a control valve for controlling the opening or closing of the return pipe, when the pressure is lower than a preset pressure alarm value, the pressure sensor sends an opening instruction to the control valve, and the control valve is opened to enable the return pipe to be communicated.
In one embodiment, the pressure in the pressure water storage device ranges from 0.3MPa to 0.5 MPa.
In one embodiment, the rotating speed of the impeller ranges from 4000 r/min to 6000 r/min.
In one embodiment, the pressure in the gas-liquid self-priming mixing pump ranges from 0.6MPa to 0.8 MPa.
In one embodiment, the hydrogen supply device is a hydrogen generator.
In one embodiment, the water supply device is an ultrafiltration water purifier or an RO membrane reverse osmosis water purifier.
According to the hydrogen water machine, the plurality of impellers are arranged in the gas-liquid self-priming mixing pump, compared with the existing common self-priming mixing pump, the multi-shaft impeller rotation is improved from single-shaft impeller rotation, the impeller size is reduced, the rotating speed is increased, and the bubble particle size of hydrogen is smaller, so that the stability of hydrogen and water fusion is enhanced, and the retention time of hydrogen dissolved in water is prolonged; through setting up the back flow for pressure water storage device hydrogen water backward flows to the gas-liquid from stirring in inhaling the mixing pump and mixes, and under the effect of repeated cycle like this, promote the super high concentration of hydrogen in hydrogen water, maintain the dwell time that hydrogen is dissolved in water simultaneously.
Drawings
FIG. 1 is a schematic structural diagram of a hydrogen water machine according to one embodiment;
fig. 2 is a schematic structural diagram of a gas-liquid self-priming mixing pump according to an embodiment.
Detailed Description
In order to make the aforementioned objects, features and advantages of the present invention comprehensible, embodiments accompanied with figures are described in detail below. In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present invention. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein.
In the description of the present invention, it is to be understood that the terms "central," "longitudinal," "lateral," "length," "width," "thickness," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," "clockwise," "counterclockwise," "axial," "radial," "circumferential," and the like are used in the orientations and positional relationships indicated in the drawings for convenience in describing the invention and to simplify the description, and are not intended to indicate or imply that the referenced device or element must have a particular orientation, be constructed and operated in a particular orientation, and are not to be considered limiting of the invention.
As shown in fig. 1 and 2, the hydrogen water machine comprises a hydrogen gas supply device 10, a water supply device 20, a gas-liquid self-priming mixing pump 30, a one-way valve 40, a return pipe 50 and a pressure water storage device 60, wherein the hydrogen gas supply device 10 is used for supplying hydrogen gas, and the water supply device 20 is used for supplying pure water. Wherein the hydrogen supply device 10 is a hydrogen generator. The water supply device 20 is an ultrafiltration water purifier or an RO membrane reverse osmosis water purifier.
The gas-liquid self-priming mixing pump 30 is provided with a first gas suction port 310, a first water inlet 320 and a first water outlet 330, the first gas suction port 310 is communicated with the hydrogen supply device 10, and a plurality of impellers 330 for mixing hydrogen and water are arranged in the gas-liquid self-priming mixing pump 30. The impeller 330 employs three impellers 340 distributed in a regular triangle.
The pressure water storage device 60 is used for storing hydrogen water, the pressure water storage device 60 is provided with a return port 610, a second water outlet 620 and a second water inlet 630, the second water inlet 630 is communicated with the first water outlet 330, the return port 610 is communicated with the first water inlet 320 through a return pipe 50, the first water inlet 320 is sequentially communicated with the second water inlet 630 through a one-way valve 40 along the water flow direction, and the second water outlet 620 is used for outputting hydrogen water 70.
Above-mentioned hydrogen water machine, through set up a plurality of impeller 330 in gas-liquid is from inhaling mixing pump 30, compare with current ordinary from inhaling mixing pump, has improved multiaxis impeller 330 rotation from the rotation of unipolar impeller 330, and impeller 330 volume reduces, and the rotational speed improves for the bubble particle size of hydrogen is littleer, thereby strengthens the stability of hydrogen and water fusion, prolongs the dwell time of hydrogen in dissolving in water. The concentration of common hydrogen water is reduced rapidly, the color of the hydrogen water is changed from milky white to common water after 5 seconds, and the hydrogen content in the hydrogen water is low, but the hydrogen water produced by the method can maintain the milky white state of the hydrogen water for about 15 seconds, can maintain the high hydrogen solubility of 2-4.5ppm for a long time, and can be reduced to 2ppm within about 2 hours.
In one embodiment, the check valve 40 is provided with a second suction port 410, a third water inlet port 420 and a third water outlet port 430, the second suction port 410 is communicated with the hydrogen gas supplying device 10, the third water inlet port 420 is communicated with the water supplying device 20, and the third water outlet port 430 is communicated with the first water inlet port 320. That is, the second air inlet 410 is added to the one-way valve water inlet 420, and preferably, the ratio of the hydrogen supply amount of the first air inlet 310 to the hydrogen supply amount of the second air inlet 410 is 2:1 to 3: 2. For example, when the first suction port 310 supplies 60ml of hydrogen and the second suction port 410 supplies 40ml of hydrogen, the amount of hydrogen introduced can be increased by replenishing the hydrogen through the first suction port 310 and the second suction port 410.
Through setting up the back flow pipe 50 for the hydrogen water 70 of pressure water storage device 60 flows back to and stirs the mixture in the gas-liquid is from inhaling mixing pump 30, and under the effect of repeated circulation like this, promote the super high concentration of hydrogen in hydrogen water 70, maintains the dwell time of hydrogen in water simultaneously.
In one embodiment, a pressure sensor (not shown) for sensing the pressure is disposed in the pressure water storage device 60, the return pipe 50 is provided with a control valve 80 for controlling the opening or closing of the return pipe 50, when the pressure is lower than a preset pressure alarm value, the pressure sensor sends an opening command to the control valve 80, and the control valve 80 opens to communicate the return pipe 50. By arranging the return pipe 50, the hydrogen water 70 in the pressure water storage device 60 is returned to the gas-liquid self-priming mixing pump 30 to be stirred and mixed, and the circulation is repeated for two to three times, so that the hydrogen solubility of the hydrogen water 70 in the pressure water storage device 60 is maintained at about 4.5 ppm.
In one embodiment, the pressure in the pressurized water storage device 60 ranges from 0.3MPa to 0.5 MPa. Preferably, the pressure in the pressurized water storage device 60 is 0.4MPa, and the hydrogen solubility of the hydrogen water 70 in the tank can be maintained at about 4.5 ppm. The pressurized water storage device 60 may be a conventional pressurized tank structure, and will not be described herein.
In one embodiment, the rotation speed of the impeller 330 is 4000-6000 r/min. The hydrogen bubble particle diameter can be made smaller. Compare with the impeller of conventional 2700r/min among the prior art, the hydrogen bubble particle diameter of making during the gas-liquid mixture of prior art is more than 100um, and multiaxis impeller rotational speed increases, can make the hydrogen bubble particle diameter at 5 ~ 100um for the hydrogen separation slows down, can effectively maintain the dwell time of hydrogen in the ultra high concentration hydrogen water.
In one embodiment, the pressure in the self-priming mixing pump 30 ranges from 0.6MPa to 0.8 MPa. Pressurization is applied to increase the hydrogen solubility of the hydrogen water.
The above-mentioned embodiments only express several embodiments of the present invention, and the description thereof is more specific and detailed, but not construed as limiting the scope of the invention. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention. Therefore, the protection scope of the present patent shall be subject to the appended claims.
Claims (9)
1. A hydrogen water machine is characterized by comprising a hydrogen gas supply device, a water supply device, a gas-liquid self-priming mixing pump, a one-way valve, a return pipe and a pressure water storage device, wherein the hydrogen gas supply device is used for supplying hydrogen gas, the water supply device is used for supplying pure water,
the gas-liquid self-priming mixing pump is provided with a first gas suction port, a first water inlet and a first water outlet, the first gas suction port is communicated with the hydrogen supply device, a plurality of impellers for mixing hydrogen and water are arranged in the gas-liquid self-priming mixing pump,
the pressure water storage device is used for storing hydrogen water, the pressure water storage device is provided with backward flow mouth, second delivery port and second water inlet, the second water inlet with first delivery port intercommunication, the backward flow mouth with first water inlet intercommunication, first water inlet passes through the check valve with the second water inlet communicates along rivers direction in proper order, the second delivery port is used for exporting hydrogen water.
2. The hydrogen water machine of claim 1, characterized in that the one-way valve is provided with a second suction port communicating with the hydrogen supply device, a third water inlet communicating with the water supply device, and a third water outlet communicating with the first water inlet.
3. The hydrogen water machine according to claim 2, characterized in that the ratio of the supply amount of hydrogen gas to the first and second suction ports is 2:1 to 3: 2.
4. The hydrogen water machine of claim 1, characterized in that a pressure sensor for sensing the pressure is arranged in the pressure water storage device, the return pipe is provided with a control valve for controlling the opening or closing of the return pipe, when the pressure is lower than a preset pressure alarm value, the pressure sensor sends an opening instruction to the control valve, and the control valve is opened to enable the return pipe to be communicated.
5. The hydrogen water machine of claim 1, characterized in that the pressure in the pressure water storage device ranges from 0.3MPa to 0.5 MPa.
6. The hydrogen water machine of claim 1, characterized in that the rotation speed of the impeller is in the range of 4000-6000 r/min.
7. The hydrogen water machine of claim 1, characterized in that the pressure in the gas-liquid self-priming mixing pump ranges from 0.6MPa to 0.8 MPa.
8. The hydrogen water machine of claim 1, characterized in that the hydrogen gas supply device is a hydrogen gas generator.
9. The hydrogen water machine of claim 1, characterized in that the water supply device is an ultrafiltration water purifier or an RO membrane reverse osmosis water purifier.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110519127.4A CN113041874A (en) | 2021-05-12 | 2021-05-12 | Hydrogen water machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110519127.4A CN113041874A (en) | 2021-05-12 | 2021-05-12 | Hydrogen water machine |
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| Publication Number | Publication Date |
|---|---|
| CN113041874A true CN113041874A (en) | 2021-06-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110519127.4A Pending CN113041874A (en) | 2021-05-12 | 2021-05-12 | Hydrogen water machine |
Country Status (1)
| Country | Link |
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| CN (1) | CN113041874A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113769596A (en) * | 2021-09-30 | 2021-12-10 | 正氢科技(中山市)有限公司 | High fusion device of hydrogen and water |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5765403A (en) * | 1993-04-16 | 1998-06-16 | Tri-Mark Metal Corporation | Water treatment method and apparatus |
| CN106000136A (en) * | 2015-03-30 | 2016-10-12 | 上海纳诺巴伯纳米科技有限公司 | Preparation device of supersaturated hydrogen solution and preparation method thereof |
| CN207385215U (en) * | 2017-08-30 | 2018-05-22 | 中山市精典电器有限公司 | A kind of gas and water high-speed mixing device |
-
2021
- 2021-05-12 CN CN202110519127.4A patent/CN113041874A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5765403A (en) * | 1993-04-16 | 1998-06-16 | Tri-Mark Metal Corporation | Water treatment method and apparatus |
| CN106000136A (en) * | 2015-03-30 | 2016-10-12 | 上海纳诺巴伯纳米科技有限公司 | Preparation device of supersaturated hydrogen solution and preparation method thereof |
| CN207385215U (en) * | 2017-08-30 | 2018-05-22 | 中山市精典电器有限公司 | A kind of gas and water high-speed mixing device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113769596A (en) * | 2021-09-30 | 2021-12-10 | 正氢科技(中山市)有限公司 | High fusion device of hydrogen and water |
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Application publication date: 20210629 |