CN207958041U - The synthesizer of high concentration dissolved oxygen water - Google Patents
The synthesizer of high concentration dissolved oxygen water Download PDFInfo
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- CN207958041U CN207958041U CN201721780712.5U CN201721780712U CN207958041U CN 207958041 U CN207958041 U CN 207958041U CN 201721780712 U CN201721780712 U CN 201721780712U CN 207958041 U CN207958041 U CN 207958041U
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Abstract
The utility model is related to a kind of synthesizers of high concentration dissolved oxygen water, more particularly to a kind of by water through filtering, after deodorizing sterilizing and magnetized process, the high dissolved oxygen liquid of required ratio is synthesized with water by flow control, water temperature is maintained in the state of 5 DEG C to 45 DEG C, with the flow control of 1000mL/min to 10000mL/min design with the device of the synthesis of high dissolved oxygen liquid, wherein the synthesizer includes filter device, deodorizing sterilizing device, flow control valve, control computer and magnetizing assembly, the synthesizer of the utility model can make the oxygen molecule in high dissolved oxygen liquid carry out cladding with the hydrone of water to be combined, and then form high concentration dissolved oxygen water.
Description
Technical field
The utility model is related to a kind of synthesizer of high concentration dissolved oxygen water, more particularly to it is a kind of by water through filtering, deodorization
After sterilization and magnetized process, the high dissolved oxygen liquid of required ratio is synthesized with water by flow control, water temperature is maintained 5
DEG C in the state of 45 DEG C, with the flow control of 1000mL/min to 10000mL/min in being carried out in synthetic reaction slot and Gao Rong
The synthesis of oxygen liquid, and aforementioned water temperature is 5 DEG C to 30 DEG C and is preferred, and then form the device design of high concentration dissolved oxygen water.
Background technology
Normal person is per minute about to need 250~400 milliliters of oxygen of consumption, 360~576 liters of oxygen is about needed altogether within one day, if often
People is proposed and at least drinks 2 liters of water for one day, this number is obviously quite surprising, although human body is very big to the consumption of oxygen,
But storage capacity of the oxygen in human body is quite few, it may be said that is to exhale oxygen to run out once suction one, even if will deposit
Use is all brought in oxygen all in human body, is also merely able to maintain bodily tissue consumption less than a few minutes, so everybody knows
Road, people can not have a meal for several days not to drink water, but cannot a few minutes not inhaling of oxygen.
For normal person under rest state, 100 milliliters of blood of average minute clock are about 5mL oxygen to tissue conveying, and when activity
Oxygen demand will be made to increase, the storage level of oxygen is little in common people's body, estimates per about oxygen-containing 20mL in 100mL blood according to medicine, if with
Blood of human body content is generally 70-80mL/kg, and the oxygen in the blood of human body of 60kg weight stores about 900mL or so, normal condition
Lower human body must continuously feed oxygen in a steady stream from the external world, to ensure the needs of cell biooxidation, maintain human life.
And, mainly there is following four type in the case where human body anoxia：
1, anoxia anoxia, the oxygen concentration being primarily due in sucking air is too low, influences oxygen and diffuses into alveolar membrane
Interior, to carry out gas exchanges, mainly by the anoxic caused by external environment factor, mountain sickness belongs to such anoxic.
2, physiological anoxic：From 30 years old, cardio-pulmonary function started to go down hill people, and the oxygen sucked in human body is just opposite to be subtracted
It is few, therefore the oxygen content in blood is certainly few year by year, brain is affected at first, causes a series of symptom.
3, motility anoxic：It is mostly generated after body strenuous exercise, when movement, body consumption increases, and whole body is located everywhere
Increase in the anerobic glycolysis compensatory of a kind of anaerobic condition, body, lactic acid generation is made to increase, thus muscle generation is made to ache, it is muddy
The state of body inability.
4, pathological hypoxic：Human body because a variety of diseases can cause pathological hypoxic, such as hypertension, artery sclerosis, with
After artery sclerosis, blood vessel official jargon is narrow, and elasticity weakens, and causes thrombosis, and in turn resulting in oxygen therapy effect reduces, and then influences body
Body health.
There are about such as following several for the mode with method of absorption of human body oxygen at present：
1, from respiratory system air-breathing supply oxygen be oxygenated, be the most basic mode of supplying oxygen to body, oxygen supply method also include by
Oxygen cylinder and high pressure oxygen cabin etc., but such as previously mentioned inhaled in one by way of respiratory system oxygen supply one exhales oxygen i.e.
It runs out at once, and supplies oxygen the quality and efficiency of oxygenation from the Nature by respiratory system because of air pollution effect human body again.
2, oxygen supply oxygenation is absorbed from gastronintestinal system, when the gastronintestinal system of people absorbs nutrition moisture content, while also absorbs water oxygen
Gas, in fact early in having been introduced in medical thesis：Human normal absorbs oxygen, and there are two pipelines, and one is respiratory system, and one is stomach
Im system, especially gastronintestinal system, but air pollution is increasingly severe, and water source is also increasingly deteriorating, and makes stomach lining and intestinal mucosa
Oxygen absorption function and red blood cell conveying oxygen function reduce.
For these reasons, then there is the product of high oxygenated water on the market, it is intended to promote the efficiency of absorption of human body oxygen.
High oxygenated water in the prior art is that an obturator is injected in a manner of high pressure using general high voltage oxygen, with strong
Mode processed dissolves in high pressure oxygen in water, and obtains high oxygenated water, such high oxygenated water with high pressure oxygen and water-soluble conjunction, entirely
Process is both needed to be fused in obturator, and because dangerous high, the security requirement of device is high, and the height produced is oxygen-containing
Water, in addition to oxygen content is limited, if not drunk at once after opening bottle cap, the interior oxygen filled will be as general carbonated drink quickly
It is just evaporated completely, and the oxygen of such high oxygenated water still falls within gas, after human body is drunk, sometimes in hiccup as drinking carbonated drink
Just oxygen is dissipated afterwards, therefore its absorption efficiency is very low, and the oxygen content of high oxygenated water in the prior art is low, for human body
It helps little.
Utility model content
The utility model is related to a kind of synthesizer of high concentration dissolved oxygen water, more particularly to it is a kind of by water through filtering, deodorization
After sterilization and magnetized process, the high dissolved oxygen liquid of required ratio is synthesized with water by flow control, water temperature is maintained 5
DEG C in the state of 45 DEG C, the synthesis with high dissolved oxygen liquid is carried out with the flow control of 1000mL/min to 10000mL/min, and preceding
5 DEG C to 30 DEG C of the water temperature stated is preferred, and then forms the device design of high concentration dissolved oxygen water, and wherein the synthesizer includes that filtering fills
Set, deodorizing sterilizing device, flow control valve, control computer and magnetizing assembly, water via filter device be filtered heavy metal,
Impurity etc., then elimination peculiar smell and sterilization are carried out via deodorizing sterilizing device, then carry out hydrone at miniaturization through magnetizing assembly
Reason is additionally provided with flow control valve after the magnetizing assembly, and the flow of water is controlled by a control computer, and in flow
It is imported with high dissolved oxygen liquid at control valve, and water and the default individual mixed proportions of high dissolved oxygen liquid, water are controlled by flow control valve
And high dissolved oxygen liquid then enters in a synthetic reaction slot after controlling flow and carries out reaction synthesis, the reaction synthesis of water and high dissolved oxygen liquid
It about carries out 10-30 minutes, and synthetic reaction trough inner water temperature control system is maintained to 5 DEG C to 45 DEG C of state by a temperature controller, and
Water temperature is preferred between being 5 DEG C to 30 DEG C, and is coated and combined with hydrone after so that the oxygen molecule in high dissolved oxygen liquid is mixed with water, and then shape
At every liter of about 300-1000PPM or the high concentration dissolved oxygen water of more rich oxygen content, then through filling.
The utility model main purpose is so that the building-up process of high concentration dissolved oxygen water can be carried out in normal pressure state, and be closed
At process compared with no danger, synthesizer cost is relatively low.
The another object of the utility model is mainly the oxygen molecule made after being mixed with water by high dissolved oxygen liquid in high dissolved oxygen liquid
It coats and combines with hydrone so that high dissolved oxygen liquid will not volatilize, and after human body is drunk, obtain very high absorption efficiency.
Description of the drawings
Fig. 1 is the device process block diagram that the utility model attempts a wherein preferred embodiment.
Fig. 2 is the device process block diagram that the utility model increases by a deodorizing sterilizing device.
[reference sign]
(1) water
(2) filter device
(3) deodorizing sterilizing device
(4) magnetizing assembly
(5) flow control valve
(6) control computer (61) temperature controller
(7) high dissolved oxygen liquid
(8) synthetic reaction slot
(9) it loads
Specific implementation mode
The invention will now be further described with reference to specific embodiments, the advantages and features of the present invention will be with description and
It is apparent.But examples are merely exemplary for these, and it is not intended to limit the scope of the present invention in any way.People in the art
Member it should be understood that without departing from the spirit and scope of the invention can to the details of technical solution of the present invention and form into
Row modifications or substitutions, but these modifications and replacement are each fallen in protection scope of the present invention.
It is to pass through water (1) refering to Figure 1, the utility model is related to a kind of synthesizer of high concentration dissolved oxygen water
After filtering and magnetized process, by flow control valve (5) flow control by the high dissolved oxygen liquid (7) of required ratio and water (1) in
Is synthesized in synthetic reaction slot (8), and by one by the temperature controller (61) of control computer (6) control by synthetic reaction slot
(8) the water temperature control in maintains 5 DEG C to 45 DEG C of state, and then forms the device design of high concentration dissolved oxygen water.The wherein conjunction
Include filter device (2), magnetizing assembly (4), flow control valve (5) and control computer (6) at device.Water (1) is via filtering
After device (2) is filtered the process of heavy metal, impurity etc., then will be at the molecule progress miniaturization of water (1) through magnetizing assembly (4)
Reason is additionally provided with flow control valve (5), and control flow control by a control computer (6) after the magnetizing assembly (4)
Valve (5) imports high dissolved oxygen liquid (7) to control the flow of water (1) at flow control valve (5), and by flow control valve (5)
Control water (1) and high dissolved oxygen liquid (7) default mixed proportion.Wherein water (1) is with 1000mL/min to 10000mL/min
Flow control carry out with the synthesis of high dissolved oxygen liquid (7), and the flow of high dissolved oxygen liquid (7) then regard between water (1) needed for mixing
Ratio and adjusted by flow control valve (5), water (1) and high dissolved oxygen liquid (7) then enter a synthetic reaction after controlling flow
Carry out in slot (8) reaction synthesis, water (1) and high dissolved oxygen liquid (7) in the reaction generated time in synthetic reaction slot (8) be 10-30
Minute, and the temperature controller (61) controlled by a control computer (6) controls the temperature in synthetic reaction slot (8) in water temperature 5
DEG C between 45 DEG C, make water (1) and high dissolved oxygen liquid (7) in making oxygen molecule and water in high dissolved oxygen liquid (7) in synthetic reaction slot (8)
(1) hydrone carries out cladding combination, and then forms the high concentration dissolved oxygen of every liter of about 300-1000PPM or more rich oxygen content
Water, then through filling (9).The utility model can be carried out in the building-up process of high concentration dissolved oxygen water in normal pressure state, and be closed
At process compared with no danger, water temperature above-mentioned is to be preferred between 5 DEG C to 30 DEG C, and the flow control of wherein water (1) removes
Outside 1000mL/min to 10000mL/min, it can also be increased or decreased according to required oxygen content (PPM).
The utility model can separately set a deodorizing sterilizing device (3), to carry out eliminating peculiar smell and sterilization to water (1), such as Fig. 2 institutes
Show, wherein deodorizing sterilizing device (3) is provided between filter device (2) and magnetizing assembly (4), and the deodorizing sterilizing device (3)
Ozone or ultraviolet light can be used to carry out deodorizing sterilizing.
Water (1) in the utility model refers under normal temperature and pressure by H2The substantially liquid substance that O molecules are constituted, and can
Including other compositions, such as calcium ion, magnesium ion, potassium ion, sodium ion, chlorion trace element.
The water (1) for reacting synthesis with high dissolved oxygen liquid (7) in the utility model can be through processing or raw water
(1), including but not limited to commercially available various bottled waters, tap water, mineral water, pure water, distilled water, magnetized water, electrolysis water, from
The potable water of any types such as sub- water, ecological water, reverse osmosis water.
In conclusion the utility model has the oxygen molecule and water for providing and making after high dissolved oxygen liquid is mixed with water in high dissolved oxygen liquid
Molecule cladding combines, and high dissolved oxygen liquid will not volatilize, and after human body is drunk, absorption efficiency is very high and building-up process can be in normal pressure
State carries out, and building-up process is compared with no danger, the lower-cost effect of synthesizer.
Claims (8)
1. a kind of synthesizer of high concentration dissolved oxygen water, it is characterised in that：
The synthesizer includes sequentially connected filter device, magnetizing assembly, flow control valve, control computer and synthetic reaction
Slot makes water be filtered heavy metal, impurity via filter device, then hydrone is carried out miniaturization processing through magnetizing assembly, in
After the magnetizing assembly, continue and be equipped with flow control valve, and the flow control valve is controlled to control water entrance by control computer
The flow of synthetic reaction slot, while high dissolved oxygen liquid is imported at the flow control valve, and controlled water by the flow control valve and be somebody's turn to do
The high default mixed proportion of dissolved oxygen liquid, wherein water are carried out and height with the flow control of 1000mL/min to 10000mL/min
The synthesis of dissolved oxygen liquid, and the flow of high dissolved oxygen liquid is then adjusted depending on mixed proportion required between water by the flow control valve
Whole, water and high dissolved oxygen liquid then enter in a synthetic reaction slot after controlling flow carries out reaction synthesis, and water and high dissolved oxygen liquid are in this
Reaction generated time in synthetic reaction slot is 10-30 minutes, and the temperature controller controlled by the control computer by one should
Temperature control in synthetic reaction slot makes water and high dissolved oxygen liquid in making height in the synthetic reaction slot between water temperature is 5 DEG C to 45 DEG C
Oxygen molecule in dissolved oxygen liquid carries out cladding with the hydrone of water and is combined, and then it is that 300-1000PPM or higher contain to form every liter
The high concentration dissolved oxygen water of oxygen amount, then completed through filling.
2. synthesizer as described in claim 1, which is characterized in that the synthesizer includes separately a deodorizing sterilizing device,
To carry out eliminating peculiar smell and sterilization to water.
3. synthesizer as described in claim 1, which is characterized in that wherein pending water refers under normal temperature and pressure by H2O
The substantially liquid substance that molecule is constituted.
4. synthesizer as claimed in claim 3, which is characterized in that by H2It is also wrapped in the substantially liquid substance that O molecules are constituted
Calcium ions, magnesium ion, potassium ion, sodium ion or chlorion.
5. synthesizer as described in claim 1, which is characterized in that wherein pending water be through processing or it is untreated
Water, including commercially available various bottled waters, tap water, mineral water, pure water, distilled water, magnetized water, electrolysis water, ionized water, ecology
Water and reverse osmosis water.
6. synthesizer as described in claim 1, which is characterized in that through the synthesizer, that treated is oxygen-containing per liters of water
Amount is to carry out the adjustment of individual ratios by the flow of high dissolved oxygen liquid and water, and obtain the high concentration dissolved oxygen water of different oxygen content.
7. synthesizer as claimed in claim 2, which is characterized in that the deodorizing sterilizing device is provided at filter device and magnetization
Between device.
8. synthesizer as claimed in claim 2, which is characterized in that the deodorizing sterilizing device be using ozone or ultraviolet light into
Row deodorizing sterilizing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721780712.5U CN207958041U (en) | 2017-12-19 | 2017-12-19 | The synthesizer of high concentration dissolved oxygen water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721780712.5U CN207958041U (en) | 2017-12-19 | 2017-12-19 | The synthesizer of high concentration dissolved oxygen water |
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| Publication Number | Publication Date |
|---|---|
| CN207958041U true CN207958041U (en) | 2018-10-12 |
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ID=63729296
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721780712.5U Active CN207958041U (en) | 2017-12-19 | 2017-12-19 | The synthesizer of high concentration dissolved oxygen water |
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| Country | Link |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110204135A (en) * | 2019-07-05 | 2019-09-06 | 四川神马泉高溶氧集团有限公司 | A kind of water containing high dissolved oxygen preparation process |
| CN115466002A (en) * | 2021-06-10 | 2022-12-13 | 曾宪群 | Method for preparing high-dissolved oxygen water |
| CN116019970A (en) * | 2021-10-27 | 2023-04-28 | 曾宪群 | Method for producing high-oxygen-content aqueous gel |
-
2017
- 2017-12-19 CN CN201721780712.5U patent/CN207958041U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110204135A (en) * | 2019-07-05 | 2019-09-06 | 四川神马泉高溶氧集团有限公司 | A kind of water containing high dissolved oxygen preparation process |
| WO2021003889A1 (en) * | 2019-07-05 | 2021-01-14 | 四川神马泉高溶氧集团有限公司 | Process for preparing high-dissolved oxygen water |
| CN115466002A (en) * | 2021-06-10 | 2022-12-13 | 曾宪群 | Method for preparing high-dissolved oxygen water |
| CN116019970A (en) * | 2021-10-27 | 2023-04-28 | 曾宪群 | Method for producing high-oxygen-content aqueous gel |
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