CN212640177U - Vertical reverse osmosis type hydrogen-rich direct water dispenser - Google Patents
Vertical reverse osmosis type hydrogen-rich direct water dispenser Download PDFInfo
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- CN212640177U CN212640177U CN202021062241.6U CN202021062241U CN212640177U CN 212640177 U CN212640177 U CN 212640177U CN 202021062241 U CN202021062241 U CN 202021062241U CN 212640177 U CN212640177 U CN 212640177U
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- Prior art keywords
- water
- reverse osmosis
- active carbon
- membrane
- purification device
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 94
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 47
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 24
- 239000001257 hydrogen Substances 0.000 title claims abstract description 24
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 24
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 21
- 239000012528 membrane Substances 0.000 claims abstract description 19
- 230000035622 drinking Effects 0.000 claims abstract description 17
- 238000001914 filtration Methods 0.000 claims abstract description 9
- 235000013162 Cocos nucifera Nutrition 0.000 claims abstract description 8
- 244000060011 Cocos nucifera Species 0.000 claims abstract description 8
- 239000010903 husk Substances 0.000 claims abstract description 7
- 239000000155 melt Substances 0.000 claims abstract description 7
- 238000005245 sintering Methods 0.000 claims abstract description 7
- 238000000746 purification Methods 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000003860 storage Methods 0.000 claims description 12
- 230000007246 mechanism Effects 0.000 claims description 10
- 230000002378 acidificating effect Effects 0.000 claims description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 6
- 239000002253 acid Substances 0.000 abstract description 5
- 239000003651 drinking water Substances 0.000 abstract description 4
- 235000020188 drinking water Nutrition 0.000 abstract description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052802 copper Inorganic materials 0.000 abstract description 3
- 239000010949 copper Substances 0.000 abstract description 3
- 229910052742 iron Inorganic materials 0.000 abstract description 3
- 229910021645 metal ion Inorganic materials 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 230000009467 reduction Effects 0.000 description 5
- 230000009471 action Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses a vertical reverse osmosis formula hydrogen-rich straight drinking machine, including 5 grades of RO reverse osmosis purifier, 5 grades of RO reverse osmosis purifier include that PP melts spouts the membrane, UOF coconut husk active carbon, CDO sintering active carbon, TO membrane and T33 rearmounted active carbon, and set gradually in 5 grades of RO reverse osmosis purifier, through the water filtration system among the 5 grades of RO reverse osmosis purifier, handle water, detach contains iron, metal ions such as copper, recycle current SPE electrolysis technique, the drinking water gets into proton membrane electrolysis cell and electrolyzes, prepare hydrogen-containing alkalescent drinking water through electrolysis cell cathodic electrolysis reaction, compare simple reverse osmosis unit, the condition that terminal play water PH is weak acid has been changed, secondly the redox potential is negative potential, possess reducibility. The proton membrane electrolytic cell increases the pure water electrolysis efficiency, the anode acid water is adjustable, the proportion of the reduced wastewater is reduced, and the waste is reduced.
Description
Technical Field
The utility model belongs to the technical field of proton membrane electrolysis, in particular to a vertical reverse osmosis type hydrogen-enriched direct drinking machine.
Background
At present, a vertical direct drinking system does not have a hydrogen-containing water function in the market, mainly because of the relationship of indissolvability and low electrolysis efficiency of hydrogen, so that the hydrogen-containing water function of the vertical direct drinking system needs to solve the problems of solubility and storage of the hydrogen.
Aiming at the problems in the related art, no effective solution is provided at present, and therefore, a vertical reverse osmosis type hydrogen-enriched direct drinking machine is provided.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
The utility model provides a vertical reverse osmosis type hydrogen-rich direct drinking machine, which solves the problem mentioned in the background technology.
(II) technical scheme
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a vertical reverse osmosis formula rich hydrogen straight drinking machine, includes 5 grades of RO reverse osmosis purifier, 5 grades of RO reverse osmosis purifier include that PP melts spouts the membrane, UO coconut husk active carbon, CDO sintering active carbon, TO membrane and T33 postposition active carbon, and set gradually in 5 grades of RO reverse osmosis purifier, form water filtration system, the water that needs TO purify loops through PP melts and spouts the membrane, UO coconut husk active carbon, CDO sintering active carbon, TO membrane and T33 postposition active carbon and is purification treatment, 5 grades of RO reverse osmosis purifier's one end is passed through water conveying mechanism intercommunication electrolysis trough, the delivery port of the positive pole of electrolysis trough passes through the storage water tank of water dispenser of water conveying mechanism connection, the inside heating courage that is used for the drinking machine that is provided with of storage water tank, and the storage water tank is provided with two delivery ports, is normal atmospheric temperature water export and hot water export respectively, connect the step-down power supply module between 5 grades of RO reverse osmosis purifier and the electrolysis, the voltage reduction power supply module comprises a power supply.
Furthermore, the 5-stage RO reverse osmosis purification device is externally connected with a computer control panel.
Further, the water delivery mechanism comprises any one of a conduit, a water pipe and a delivery pipe.
Furthermore, a water inlet is also arranged on the 5-stage RO reverse osmosis purification device.
Further, the electrolytic cell has a generator H2And weakly alkaline water and produces O2And an anode for acidic water.
Furthermore, a concentrated water combination valve, a water inlet electromagnetic valve, a booster pump and a heating tank are further arranged on the water filtration system of the 5-stage RO reverse osmosis purification device, and the concentrated water combination valve, the water inlet electromagnetic valve, the booster pump and the heating tank are all externally connected with a computer control panel.
(III) advantageous effects
Compared with the prior art, the utility model provides a vertical reverse osmosis formula rich hydrogen direct drinking machine possesses following beneficial effect:
through the water filtration system among the 5 grades of RO reverse osmosis purification devices, handle water, detach and contain metal ion such as iron, copper, recycle current SPE electrolytic technology, the drinking water gets into proton membrane electrolysis cell and electrolyzes, prepares hydrogen-containing weak alkaline drinking water through electrolysis cell cathodic electrolysis reaction, compares simple reverse osmosis unit, has changed the condition that terminal play water PH is weak acid, and secondly the redox potential is negative potential, possess the reducibility. The proton membrane electrolytic cell increases the pure water electrolysis efficiency, the anode acid water is adjustable, the proportion of the reduced wastewater is reduced, and the waste is reduced.
Drawings
FIG. 1 is a flow chart of the present invention;
fig. 2 is a schematic diagram of the conventional electrical device connection of the present invention;
FIG. 3 shows the operation principle of the electrolytic cell of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-3, the present invention provides a technical solution: the utility model provides a vertical reverse osmosis formula rich hydrogen straight drinking machine, includes 5 grades of RO reverse osmosis purifier, 5 grades of RO reverse osmosis purifier include that PP melts spouts the membrane, UO coconut husk active carbon, CDO sintering active carbon, TO membrane and T33 postposition active carbon, and set gradually in 5 grades of RO reverse osmosis purifier, form water filtration system, the water that needs TO purify loops through PP melts and spouts the membrane, UO coconut husk active carbon, CDO sintering active carbon, TO membrane and T33 postposition active carbon and is purification treatment, 5 grades of RO reverse osmosis purifier's one end is passed through water conveying mechanism intercommunication electrolysis trough, the delivery port of the positive pole of electrolysis trough passes through the storage water tank of water dispenser of water conveying mechanism connection, the inside heating courage that is used for the drinking machine that is provided with of storage water tank, and the storage water tank is provided with two delivery ports, is normal atmospheric temperature water export and hot water export respectively, connect the step-down power supply module between 5 grades of RO reverse osmosis purifier and the electrolysis, the voltage reduction power supply module comprises a power supply.
As shown in the figure 1-2, the 5-stage RO reverse osmosis purification device is externally connected with a computer control board.
As shown in fig. 1-2, the water delivery mechanism includes any one of a conduit, a water pipe, and a delivery pipe.
As shown in the figure 1-2, the 5-stage RO reverse osmosis purification device is also provided with a water inlet.
As shown in FIGS. 1-2, the electrolytic cell has a production H2And weakly alkaline water and produces O2And an anode for acidic water.
As shown in the figure 1-2, a concentrated water combination valve, a water inlet electromagnetic valve, a booster pump and a heating tank are also arranged on the water filtration system of the 5-stage RO reverse osmosis purification device, and the concentrated water combination valve, the water inlet electromagnetic valve, the booster pump and the heating tank are all externally connected with a computer control panel.
The SPE electrolysis technology, which is the most advanced hydrogen/oxygen production technology at present, is mainly used for ships and warships, and is gradually used for civil use in recent years, such as medical hydrogen absorbers, fuel cells and the like, along with the development of technology and materials science, and the hydrogen-rich water preparation is only a branch use direction in the SPE electrolysis technology, and the electrochemical principle is as follows:
and (3) total reaction: 2H2O = (energization) 2H2↑+ O2↑
And (3) anode reaction: 4OH (-) -4e (-) =2H2O+O2↑
Cathode reaction 2H (+) +2e (-) = H2↑
The working principle is as follows: water TO be purified enters a 5-level RO reverse osmosis purification device through a water inlet, metal ions such as iron and copper are removed through sequential filtration of a PP melt-spray film, UOF coconut shell activated carbon, CDO sintered activated carbon, a TO film and T33 post-positioned activated carbon, the processed pure water respectively enters the cathode and the anode of an electrolytic cell for electrolysis, a voltage reduction power supply module in the process finishes voltage reduction and power supply, and a cathode generates H after the voltage reduction power supply2And weakly alkaline water, the anode produces O2And acid water, anode products enter a water storage tank through a water delivery mechanism such as a guide pipe, the water storage tank is equivalent to a common water dispenser in our life and is provided with a heating liner and a normal-temperature water and hot water outlet, the working voltage of an electrolytic cell is 5-8V, the current is 1A-3A, the content of terminal outlet water H2 is 800ppb-1300ppb, the pH is 7.3-8.5, and the oxidation-reduction potential is-400 mv +/-10% when the pH is 8, in addition, as a concentrated water combination valve, a water inlet electromagnetic valve, a booster pump and a heating tank are all externally connected with a computer control panel, the real-time control of a concentrated water combination valve, a water inlet electromagnetic valve, the booster pump and a heating tank can be realized, the electrolysis is ensured, and the pH of the terminal outlet water of the water is 7.3-8.5: 1000ppb or more and the redox potential: -350mv ± 20% service life: more than or equal to 4000 hours.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "front end", "rear end", "both ends", "one end", "the other end" and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element to which the reference is made must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a vertical reverse osmosis formula rich hydrogen straight drinking machine, includes 5 grades of RO reverse osmosis purifier, its characterized in that: 5 level RO reverse osmosis purification device includes that PP melts spouts the membrane, UO coconut husk active carbon, CDO sintering active carbon, TO membrane and T33 rearmounted active carbon, and sets gradually in 5 level RO reverse osmosis purification device, forms water filtration system, and the water that needs TO purify loops through PP melts spouts the membrane, UO coconut husk active carbon, CDO sintering active carbon, TO membrane and T33 rearmounted active carbon and does purification treatment, 5 level RO reverse osmosis purification device's one end is passed through water conveying mechanism intercommunication electrolysis trough, the delivery port of electrolysis trough's positive pole passes through the storage water tank that water conveying mechanism connects the water dispenser, the inside heating courage that is provided with the water dispenser of storage water tank, and the storage water tank is provided with two delivery ports, is normal atmospheric temperature water export and hot water export respectively, connect the step-down power supply module between 5 level RO reverse osmosis purification device and the electrolysis trough, step-down power supply module includes power supply.
2. The vertical reverse osmosis type hydrogen-rich direct drinking machine according to claim 1, characterized in that: and the 5-stage RO reverse osmosis purification device is externally connected with a computer control panel.
3. The vertical reverse osmosis type hydrogen-rich direct drinking machine according to claim 1, characterized in that: the water delivery mechanism comprises any one of a conduit, a water pipe and a delivery pipe.
4. The vertical reverse osmosis type hydrogen-rich direct drinking machine according to claim 1, characterized in that: and the 5-stage RO reverse osmosis purification device is also provided with a water inlet.
5. The vertical reverse osmosis type hydrogen-rich direct drinking machine according to claim 1, characterized in that: the electrolytic cell has a product H2And weakly alkaline water and produces O2And an anode for acidic water.
6. The vertical reverse osmosis type hydrogen-rich direct drinking machine according to claim 2, characterized in that: and a concentrated water combination valve, a water inlet electromagnetic valve, a booster pump and a heating tank are further arranged on the water filtering system of the 5-stage RO reverse osmosis purification device, and the concentrated water combination valve, the water inlet electromagnetic valve, the booster pump and the heating tank are all externally connected with a computer control panel.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021062241.6U CN212640177U (en) | 2020-06-09 | 2020-06-09 | Vertical reverse osmosis type hydrogen-rich direct water dispenser |
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|---|---|---|---|
| CN202021062241.6U CN212640177U (en) | 2020-06-09 | 2020-06-09 | Vertical reverse osmosis type hydrogen-rich direct water dispenser |
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| CN212640177U true CN212640177U (en) | 2021-03-02 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111517538A (en) * | 2020-06-09 | 2020-08-11 | 四川活力氢净水科技有限公司 | Vertical reverse osmosis type hydrogen-rich direct water dispenser |
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- 2020-06-09 CN CN202021062241.6U patent/CN212640177U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111517538A (en) * | 2020-06-09 | 2020-08-11 | 四川活力氢净水科技有限公司 | Vertical reverse osmosis type hydrogen-rich direct water dispenser |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220221 Address after: 637000 No. 2, building 1, No. 70 Yan'an Road, Shunqing District, Nanchong City, Sichuan Province Patentee after: Sichuan vitality core water purification equipment Co.,Ltd. Address before: 637000 Chengnan Industrial Park, Jialing District, Nanchong City, Sichuan Province Patentee before: Sichuan Huoli hydrogen water purification technology Co.,Ltd. |
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| TR01 | Transfer of patent right |