CN219297254U - Hydrogen-rich water-soluble hydrogen mixing equipment - Google Patents

Hydrogen-rich water-soluble hydrogen mixing equipment Download PDF

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CN219297254U
CN219297254U CN202223379305.7U CN202223379305U CN219297254U CN 219297254 U CN219297254 U CN 219297254U CN 202223379305 U CN202223379305 U CN 202223379305U CN 219297254 U CN219297254 U CN 219297254U
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hydrogen
water
tank
outlet
communicated
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李荣海
李义福
于子凡
于文强
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Weifang Yingdatong Water Technology Co ltd
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Weifang Yingdatong Water Technology Co ltd
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    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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Abstract

The utility model belongs to the technical field of hydrogen-rich water, and relates to hydrogen-rich water hydrogen dissolving and mixing equipment, which comprises a pure water tank, wherein the pure water tank is communicated with a polishing resin tank and an ion disrupter; the ultrapure water in the pure water tank is filtered by polishing resin and then enters an electrolytic tank to electrolyze hydrogen, the water pumped from the pure water tank can increase the gap between water molecules after passing through an ion interference device before entering a gas-liquid mixing pump, so that the hydrogen and the water are more easily mixed, then enter a jet device and a static mixer in sequence to be fully mixed, a part of the undissolved hydrogen returns to the gas-liquid mixing pump, and a part returns to the jet pump to enter a circulating hydrogen dissolving process again, so that the hydrogen concentration in the water is promoted again to realize circulation, and the hydrogen content of hydrogen-rich water in the static mixer is kept from being reduced.

Description

Hydrogen-rich water-soluble hydrogen mixing equipment
Technical Field
The utility model belongs to the technical field of hydrogen-rich water, and particularly relates to hydrogen-rich water-soluble hydrogen mixing equipment.
Background
Hydrogen-rich water, also known as "molecular hydrogen water," refers to the dissolution of hydrogen gas in drinking water. The hydrogen-rich water is rich in hydrogen simple substances, has good antioxidation effect, can delay human body aging after frequent drinking, and has the effects of preventing atherosclerosis and resisting inflammation of internal organs.
The existing hydrogen-rich water hydrogen dissolving device mostly introduces hydrogen into water through a gas-liquid mixing pump, and then introduces the formed hydrogen-rich water into a water storage tank for residents to drink. CN113149173a discloses a "hydrogen-rich water saturation hydrogen-dissolving device", a physical principle-based design is optimized to provide several effective technical schemes, so that the hydrogen-rich water beverage container based on the technical scheme can effectively increase the contact surface area of hydrogen and drinking water and fully prolong the mutual contact time to prolong the process of dissolving hydrogen in drinking water, thereby realizing long-term and stable provision of saturated dissolved hydrogen high-quality hydrogen-rich water beverage to users at any time. Although the device does not need extra power consumption and maintains the hydrogen content in the hydrogen-rich water for a certain period of time, the hydrogen is lighter and overflows from the water after a long time, so that the hydrogen content in the hydrogen-rich water is reduced.
Disclosure of Invention
The utility model aims to solve the technical problem of providing the hydrogen-rich water-soluble hydrogen mixing equipment which can improve the solubility of hydrogen in water, avoid the decrease of the hydrogen content in hydrogen-rich water and realize the recycling.
In order to solve the technical problems, the technical scheme of the utility model is as follows:
the utility model provides a rich hydrogen water-soluble hydrogen mixes hydrogen equipment, includes the pure water tank, the pure water tank intercommunication has polishing resin jar and ion interference ware, polishing resin jar intercommunication has the electrolysis trough, ion interference ware with the electrolysis trough intercommunication has the gas-liquid mixing pump, the gas-liquid mixing pump intercommunication has the ejector, the ejector intercommunication has static mixer, static mixer intercommunication the pure water tank the ejector with the gas-liquid mixing pump.
As the preferable technical scheme, a pure water inlet and a pure water outlet are arranged on the pure water tank, and a reverse osmosis membrane is arranged in the pure water tank;
the polishing resin tank is filled with polishing resin, the polishing resin tank is provided with a resin tank inlet and a resin tank outlet, and the resin tank inlet is communicated with the pure water outlet;
the electrolytic tank is provided with an electrolytic tank water inlet and a hydrogen outlet, and the electrolytic tank water inlet is communicated with the outlet of the resin tank;
the gas-liquid mixing pump is provided with a mixing pump air inlet, a mixing pump water inlet and a mixing pump water outlet, the mixing pump air inlet is communicated with the hydrogen outlet, and the mixing pump water inlet is communicated with the pure water outlet;
the ejector is provided with a jet air inlet, a jet water inlet and a jet water outlet, and the jet water inlet is communicated with the water outlet of the mixing pump;
the static mixer is provided with a mixer air outlet, a mixer water inlet and a mixer water outlet, the mixer water inlet is communicated with the jet water outlet, the mixer air outlet is respectively communicated with the jet air inlet and the mixing pump air inlet, and the mixer water outlet is communicated with the pure water inlet;
the ion disrupter is provided with an disrupter water inlet and an disrupter water outlet, the disrupter water inlet is communicated with the pure water outlet, and the disrupter water outlet is communicated with the mixing pump water inlet.
As the preferable technical scheme, the static mixer comprises a cylindrical shell, the water inlet of the mixer and the water outlet of the mixer are respectively arranged at two sides of the bottom of the shell, the air outlet of the mixer is arranged at the top of the shell, and a folding filter element is arranged at the center in the shell and is used for cutting big bubbles into small bubbles.
As the preferable technical scheme, the ion disrupter comprises a base, a Tesla coil is arranged in the base, an outer tube with a closed top end and an inner tube sleeved in the outer tube are arranged on the base, the top end of the inner tube is closed, a water flowing cavity is formed between the outer tube and the inner tube, a water inlet of the disrupter is arranged at the lower part of the outer tube, a water outlet of the disrupter is arranged at the upper part of the outer tube, a spherical glass cover is arranged in the inner tube, inert gas and an electrode are arranged in the spherical glass cover, and the bottom end of the electrode extends out of the spherical glass cover and is connected with the Tesla coil.
As a preferable technical scheme, the outer tube and the inner tube are transparent subcritical force tubes.
As a preferable technical scheme, the reverse osmosis membrane is a first-order RO reverse osmosis membrane.
As a preferable technical scheme, the electrolytic tank is a constant-voltage constant-current electrolytic tank.
As the preferable technical scheme, the pure water tank is communicated with an ultrafiltration membrane pretreatment device, and a water outlet of the ultrafiltration membrane pretreatment device is communicated with a pure water inlet of the pure water tank.
Due to the adoption of the technical scheme, the utility model has the beneficial effects that:
the method comprises the steps that ultrapure water manufactured in a pure water tank is filtered by polishing resin in the polishing resin tank to obtain ultrapure water, the ultrapure water enters an electrolytic tank, hydrogen is electrolyzed under the action of a constant-pressure cross-flow power supply, a gas-liquid mixing pump pumps water from the pure water tank, the pumped water firstly changes the electric field structure of original stable water through an ion interference device, the gap between water molecules is increased, the containing space is increased for hydrogen molecules, the electrolyzed hydrogen is easier to dissolve into water molecules, the electrolyzed hydrogen is mixed by the gas-liquid mixing pump and then sequentially enters an ejector to be mixed again, the ejector pumps mixed liquid of the hydrogen and the water into a static mixer to be fully mixed, the fully mixed liquid of the static mixer returns to the pure water tank to be subjected to a hydrogen enrichment step again, and part of undissolved hydrogen still exists after being fully mixed by the static mixer, part of the hydrogen returns to the gas-liquid mixing pump from the static mixer, and part returns to the jet pump to enter the circulating hydrogen dissolving process again to realize the effect of hydrogen dissolving and mixing hydrogen, the concentration of the hydrogen in the water is lifted again, and circulation is realized, and the hydrogen content of the hydrogen in the static mixer is kept not to be reduced.
Drawings
FIG. 1 is a schematic diagram of the workflow of the hydrogen-enriched water-soluble hydrogen mixing apparatus of the present utility model;
FIG. 2 is a schematic structural view of the static mixer of the present utility model;
FIG. 3 is a schematic diagram of an ion disruptor of the present utility model;
in the figure: 1-a pure water tank; 2-polishing the resin tank; 3-an electrolytic cell; 4-a gas-liquid mixing pump; 5-jet means; 6-a static mixer; 61-a housing; 62-folding the filter element; 63-mixer water inlet; 64-a mixer water outlet; 65-mixer air outlet, 71-base, 72-outer tube, 73-inner tube, 74-water flowing cavity, 75-interference device water inlet, 76-interference device water outlet, 77-spherical glass cover and 78-electrode.
Detailed Description
The utility model is further illustrated in the following, in conjunction with the accompanying drawings and examples. In the following detailed description, certain exemplary embodiments of the present utility model are described by way of illustration only. It is needless to say that the person skilled in the art realizes that the described embodiments may be modified in various different ways without departing from the spirit and scope of the utility model. Accordingly, the drawings and description are to be regarded as illustrative in nature and not as restrictive in scope.
As shown in fig. 1 and fig. 2 together, a hydrogen-rich water-soluble hydrogen mixing device comprises a pure water tank 1, wherein the pure water tank 1 is used for storing pure water and process water after hydrogen-rich hydrogen mixing, the pure water tank 1 is communicated with a polishing resin tank 2 and an ion interference device 7, the polishing resin tank 2 and the ion interference device are both communicated with an electrolytic tank 3, the electrolytic tank 3 is communicated with a gas-liquid mixing pump 4, the gas-liquid mixing pump 4 is communicated with an ejector 5, the ejector 5 is communicated with a static mixer 6, and the static mixer 6 is communicated with the pure water tank 1, the ejector 5 and the gas-liquid mixing pump 4; pure water produced in the pure water tank 1 is filtered by polishing resin in the polishing resin tank 2 to form ultrapure water, the ultrapure water enters the electrolytic tank 3, hydrogen is electrolyzed in the electrolytic tank 3, the gas-liquid mixing pump 4 pumps water from the pure water tank 1 and mixes the electrolyzed hydrogen and then enters the ejector 5 along a pipeline to be mixed again, the ejector 5 pumps mixed liquid of the hydrogen and the water into the static mixer 6 to be fully mixed, the fully mixed liquid of the hydrogen and the water returns to the pure water tank 1 to be subjected to hydrogen enrichment step again, less part of undissolved hydrogen still exists after being fully mixed from the static mixer 6, the part of hydrogen comes out from the static mixer 6, the part of hydrogen returns to the gas-liquid mixing pump 4, the part of hydrogen returns to the jet pump to enter the circulating hydrogen dissolving process again, the effect of hydrogen dissolving and hydrogen mixing is realized, the concentration of the hydrogen in the water is lifted again, and circulation is realized.
As shown in fig. 1:
the pure water tank 1 is provided with a pure water inlet and a pure water outlet, and a reverse osmosis membrane is arranged in the pure water tank 1; the reverse osmosis membrane is a primary RO reverse osmosis membrane, the electric conductivity of the effluent regulated by the reverse osmosis membrane is 80-150uS/cm, and the PH of the effluent is 6.5-7.5. Can effectively ensure that hydrogen element is dissolved into drinking water in the form of hydrogen molecules in the subsequent process without generating free H+ ions. The reverse osmosis membrane is an artificial semipermeable membrane with certain characteristics, which is made of a simulated biological semipermeable membrane, and when the reverse osmosis membrane works, water passes through the aperture of the reverse osmosis membrane to intercept impurities and discharge the impurities with concentrated water, so that the effect of filtering the impurities is achieved. In general, the reverse osmosis membrane has higher requirement on water inflow, and if the water inflow cannot meet the requirement, an ultrafiltration membrane is added at present for pretreatment. The preferable technical scheme of the utility model is that water entering the pure water tank 1 is pretreated by an ultrafiltration membrane, the pure water tank 1 is communicated with an ultrafiltration membrane pretreatment device, and a water outlet of the ultrafiltration membrane pretreatment device is communicated with a pure water inlet of the pure water tank 1.
Filtration is typically performed by a quartz sand filter, an activated carbon filter, or a precision filter prior to ultrafiltration membrane pretreatment, and if the hardness of the incoming water is too high, softening may be performed using a softening resin.
The polishing resin tank 2 is filled with polishing resin, the polishing resin tank 2 is provided with a resin tank inlet and a resin tank outlet, and the resin tank inlet is communicated with the pure water outlet; polishing resins, also commonly referred to as anion and cation mixed bed resins, are formed by mixing an anion exchange resin with a cation exchange resin. In the preparation of pure water, the cation in the polishing resin absorbs the cation in water and releases H + The anion resin absorbs anions in water and releases OH - Ions, H + Ions and OH - Ions form H in water 2 O molecules and no other ions in water, thereby achieving the purpose of preparing pure water, and the resistivity can completely reach the standard of 1.0-10.0 mu S/cm.
The electrolytic tank 3 is provided with an electrolytic tank water inlet and a hydrogen outlet, and the electrolytic tank water inlet is communicated with the outlet of the resin tank; preferably, the electrolytic tank 3 adopts a constant voltage and constant current power supply. The mechanism for preparing electrolyzed water is called an electrolytic tank 3, and the main components in the electrolytic tank are an electrode plate and an ion membrane, which are the prior art for the application of many technological products. The electrolytic cell 3 is composed of a cell body, an anode and a cathode, and the anode chamber and the cathode chamber are separated by a diaphragm. When the direct current passes through the electrolytic tank 3, oxidation reaction occurs at the interface between the anode and the solution, reduction reaction occurs at the interface between the cathode and the solution, and hydrogen is separated out from the cathode of the direct current electrode; the positive electrode separates out oxygen. The oxygen is discharged to the atmosphere through the exhaust pipe, and the hydrogen enters the gas-liquid mixing pump 4 to be mixed with water.
The gas-liquid mixing pump 4 is provided with a mixing pump air inlet, a mixing pump water inlet and a mixing pump water outlet, the mixing pump air inlet is communicated with the hydrogen outlet, and the mixing pump water inlet is communicated with the pure water outlet; the mixing pump inlet is used for introducing a small amount of hydrogen which is not dissolved in the static mixer 6, the mixing pump inlet is used for pumping water from the pure water tank 1, and the mixing pump outlet is used for introducing the water which is fully mixed in the gas-liquid mixing pump 4 and is dissolved with hydrogen into the ejector 5.
The ejector 5 is provided with a jet air inlet, a jet water inlet and a jet water outlet, and the jet water inlet is communicated with the outlet of the mixing pump; the jet flow air inlet is used for introducing a small amount of undissolved hydrogen gas in the static mixer 6, the jet flow water outlet is used for introducing water after hydrogen mixing and hydrogen dissolving into the static mixer 6, and the jet flow water inlet is used for communicating with the water outlet of the mixing pump.
The static mixer 6 is provided with a mixer air outlet 65, a mixer water inlet 63 and a mixer water outlet 64, the mixer water inlet 63 is communicated with the jet water outlet, the mixer air outlet 65 is respectively communicated with the jet air inlet and the mixing pump air inlet, and the mixer water outlet 64 is communicated with the pure water inlet. The mixer air outlet 65 is used for discharging the hydrogen which is not dissolved in the water and continuously conveying the hydrogen to the jet pump and the gas-liquid mixing pump 4, and an air outlet valve is arranged at the mixer air outlet 65, so that the discharge of the hydrogen can be controlled. The water outlet 64 of the mixer is used for outputting water with the standard hydrogen content after hydrogen dissolution and hydrogen mixing as a product, or continuously conveying the water into the pure water tank 1 for continuous hydrogen dissolution and hydrogen mixing. The mixer water inlet 63 is used for being connected with a jet water outlet, and the hydrogen and water in the static mixer 6 are further mixed, so that the hydrogen dissolving and mixing process is realized.
As shown in fig. 2, the static mixer 6 includes a cylindrical housing 61, a mixer water inlet 63 and a mixer water outlet 64 are provided on both sides of the bottom of the housing 61, respectively, a mixer air outlet 65 is provided on the top of the housing 61, and a folded filter element 62 is installed at the center in the housing 61, the folded filter element 62 being used for cutting large bubbles into small bubbles. After water dissolved with hydrogen enters a mixer water inlet 63 from a shell 61 of a static mixer 6, large bubbles are cut into small bubbles under the action of a folding filter element 62, so that the hydrogen is easier to dissolve in the water, and finally discharged from a mixer water outlet 64, and the hydrogen which is not completely dissolved is continuously circulated to a jet pump and a gas-liquid mixing pump 4 to dissolve and mix the hydrogen again.
As shown in fig. 3, the ion disrupter 7 comprises a base 71, a tesla coil is arranged in the base 71, an outer tube 72 and an inner tube 73 are arranged on the base 71, the inner tube 73 is sleeved in the outer tube 72, the top ends of the outer tube 72 and the inner tube 73 are closed ends, a water flowing cavity 74 is formed between the outer tube 72 and the inner tube 73, an disrupter water inlet 75 is arranged at the lower part of the outer tube 72, an disrupter water outlet 76 is arranged at the upper part of the outer tube 72, a spherical glass cover 77 is arranged in the inner tube 73, inert gas and an electrode 78 are arranged in the spherical glass cover 77, the bottom end of the electrode 78 extends out of the spherical glass cover 77 and is connected with the tesla coil, and the tesla coil is connected with a power supply.
The outer tube 72 and the inner tube 73 are preferably transparent sub-gram tubes, with tesla coils converting the normal voltage into a high voltage high frequency voltage, which is applied to the electrodes via two pole coils, with a discharge. After the electric field is electrified, the Tesla coil generates a high-frequency voltage electric field, the energy field of the pure water flowing through can be changed due to the ionization of the high-frequency electric field on the inert gas in the spherical glass cover, so that the gaps among water molecules are increased, the gas containing space among the water molecules is increased, the miscibility of water and hydrogen is facilitated, and the inert gas in the spherical glass cover can be further glaring and shining under the ionization of the high-frequency electric field, so that the transparent sub-gram tube is colorful.
The foregoing has shown and described the basic principles, main features and advantages of the present utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.

Claims (8)

1. The utility model provides a rich hydrogen water-soluble hydrogen mixes hydrogen equipment, its characterized in that, includes the pure water tank, the pure water tank intercommunication has polishing resin jar and ion interference ware, polishing resin jar intercommunication has the electrolysis trough, ion interference ware with the electrolysis trough intercommunication has the gas-liquid mixing pump, the gas-liquid mixing pump intercommunication has the ejector, the ejector intercommunication has static mixer, static mixer intercommunication the pure water tank the ejector with the gas-liquid mixing pump.
2. The hydrogen-rich water-soluble hydrogen mixing apparatus according to claim 1, wherein,
the pure water tank is provided with a pure water inlet and a pure water outlet, and a reverse osmosis membrane is arranged in the pure water tank;
the polishing resin tank is filled with polishing resin, the polishing resin tank is provided with a resin tank inlet and a resin tank outlet, and the resin tank inlet is communicated with the pure water outlet;
the electrolytic tank is provided with an electrolytic tank water inlet and a hydrogen outlet, and the electrolytic tank water inlet is communicated with the outlet of the resin tank;
the gas-liquid mixing pump is provided with a mixing pump air inlet, a mixing pump water inlet and a mixing pump water outlet, the mixing pump air inlet is communicated with the hydrogen outlet, and the mixing pump water inlet is communicated with the pure water outlet;
the ejector is provided with a jet air inlet, a jet water inlet and a jet water outlet, and the jet water inlet is communicated with the water outlet of the mixing pump;
the static mixer is provided with a mixer air outlet, a mixer water inlet and a mixer water outlet, the mixer water inlet is communicated with the jet water outlet, the mixer air outlet is respectively communicated with the jet air inlet and the mixing pump air inlet, and the mixer water outlet is communicated with the pure water inlet;
the ion disrupter is provided with an disrupter water inlet and an disrupter water outlet, the disrupter water inlet is communicated with the pure water outlet, and the disrupter water outlet is communicated with the mixing pump water inlet.
3. The hydrogen-rich water-soluble hydrogen mixing device of claim 2, wherein the static mixer comprises a cylindrical shell, the water inlet and the water outlet of the mixer are respectively arranged at two sides of the bottom of the shell, the air outlet of the mixer is arranged at the top of the shell, and a folding filter element is arranged at the center in the shell.
4. The hydrogen-rich water-soluble hydrogen mixing device as claimed in claim 2, wherein the ion disrupter comprises a base, a tesla coil is arranged in the base, an outer tube with a closed top end and an inner tube sleeved in the outer tube are arranged on the base, the top end of the inner tube is closed, a water flowing cavity is formed between the outer tube and the inner tube, the disrupter water inlet is arranged at the lower part of the outer tube, the disrupter water outlet is arranged at the upper part of the outer tube, a spherical glass cover is arranged in the inner tube, inert gas and an electrode are arranged in the spherical glass cover, and the bottom end of the electrode extends out of the spherical glass cover and is connected with the tesla coil.
5. The hydrogen-enriched water-soluble hydrogen mixing apparatus of claim 4, wherein the outer tube and the inner tube are transparent sub-gram force tubes.
6. The hydrogen-enriched water-soluble hydrogen mixing apparatus according to any one of claims 2 to 5, wherein the reverse osmosis membrane is a primary RO reverse osmosis membrane.
7. The hydrogen-enriched water-soluble hydrogen mixing device according to any one of claims 1 to 5, wherein the electrolytic tank is a constant voltage constant current power electrolytic tank.
8. The hydrogen-rich water-soluble hydrogen mixing apparatus as claimed in any one of claims 1 to 5, wherein the pure water tank is communicated with an ultrafiltration membrane pretreatment device, and a water outlet of the ultrafiltration membrane pretreatment device is communicated with a pure water inlet of the pure water tank.
CN202223379305.7U 2022-12-16 2022-12-16 Hydrogen-rich water-soluble hydrogen mixing equipment Active CN219297254U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202223379305.7U CN219297254U (en) 2022-12-16 2022-12-16 Hydrogen-rich water-soluble hydrogen mixing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202223379305.7U CN219297254U (en) 2022-12-16 2022-12-16 Hydrogen-rich water-soluble hydrogen mixing equipment

Publications (1)

Publication Number Publication Date
CN219297254U true CN219297254U (en) 2023-07-04

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202223379305.7U Active CN219297254U (en) 2022-12-16 2022-12-16 Hydrogen-rich water-soluble hydrogen mixing equipment

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