CN106006913A - Gas supersaturated liquid and preparation method and application thereof - Google Patents
Gas supersaturated liquid and preparation method and application thereof Download PDFInfo
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- CN106006913A CN106006913A CN201610317895.0A CN201610317895A CN106006913A CN 106006913 A CN106006913 A CN 106006913A CN 201610317895 A CN201610317895 A CN 201610317895A CN 106006913 A CN106006913 A CN 106006913A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
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Abstract
The invention provides liquid with gas dissolved in a supersaturated mode. The liquid is water, and the gas is oxygen or hydrogen. The maximum oxygen content of the gas supersaturated liquid reaches 150 mg/L, the oxygen content in water is stabilized at 65 mg/L+/-1 mg/L, and the hydrogen content in water is stabilized at 3 mg/L+/-1 mg/L. The gas is dissolved in water in the supersaturated mode, growth of plants and animals can be remarkably promoted, the liquid is suitable for medical treatment, air improvement, crop production and aquaculture, the growth cycle of plants and animals is remarkably shortened, and the yield is remarkably increased.
Description
Technical field
The present invention relates to a kind of liquid, particularly relate to a kind of liquid containing satiety gas, and produce the side of this kind of liquid
Method and application aborning.
Background technology
Under uniform temperature, pressure, the dissolubility of solute under the concentration of solute has exceeded this temperature, pressure in solution,
And the phenomenon that solute does not separates out is supersaturation.Soda pop is a kind of common drink containing supersaturation carbon dioxide
Material, by the way of pressurization, dissolves in liquid by carbon dioxide.After opening bottle cap, carbon dioxide is continuous
It is distributed in air from liquid.
In all five basic elements sustained life, oxygen is mostly important, and this is colourless, odorless, tasteless element
The 65% of human body is accounted for life is critically important.Do not sleep and can live several days, do not have food can live several week, there is no oxygen
Can only live a few minutes.In health, all functions all lean on oxygen to maintain, and the necessary replacement per second of oxygen, because the life of 90% is lived
Power relies on oxygen, provides cellular energy by biological oxidation, cell can be regenerated.Health utilizes oxygen metabolism food,
Toxin and refuse is reduced by Oxidation.All organs are required for a lot of oxygen could effective operation.Oxygen is uniquely can
Build and maintain the important component of health with other elements.The essential element of protein is oxygen, nitrogen, carbon and hydrogen.Oxygen,
Carbon and hydrogen constitute carbohydrate.Water is to be made up of oxygen and hydrogen.Oxygen in air, water, protein and carbohydrate
Jointly create life energy.So, there is no life without oxygen.
Low oxygen content can make necrocytosis, and immunologic function weakens, and affects cell metabolism, can cause harmful chemical
Generation, cause health problem.It is known by everybody, so ultimate value 8mg/L of Gonna breakthrough oxygen, has produced higher
Metastable oxygen, to meeting the mankind and vegeto-animal growth requirement proposes challenge.
The most operational function of health needs hydrogen.Hydrogen is at electronics conveyer chain (with oxidation and reduction form exchange electronics)
In play a leading role.If unjustified, hydrogen is the most fragile.These impacts must utilize oxidation to be balanced.
Hydrogen is that body is built and repairs immune system, organ, the essential elements of organizational structure.Lead to healthy circuitous path
Needing some form of hydrogen (heavy hydrogen, the isotope that hydrogen family purposes is most) is the power created and sustain life.Lack
Weary hydrogen-oxygen can cause dehydration, causes human body over-drying and produces nerve conduction extremely.Moisture content and superfatted nutrient
Cannot good absorption, be likely to result in brain miopragia, face wrinkles, mucilage secretion reduces and myoneural spasm is taken out
Jerk, cause arthragra, rheumatism, giddy, unconsciousness, Wry Neck, skin allergy and joint aches.Hydrogen Energy has
Effect removes active oxygen, and can reduce the damage that half causes because of cerebral infarction in zoopery.
Everybody faces body constitution and declines, the various different healthy worries such as aging is sick, and research and development negative hydrogen ion product is (high hydrogeneous
Glucose infusion liquid water) contribute to a lot of disease problems that we solve to be faced.Research negative hydrogen ion water purpose be make more
People will appreciate that, recognize and use the effect of hydrogen.
Summary of the invention
It is an object of the present invention to provide a kind of gas supersaturation liquid, gas can be at normal temperatures and pressures with supersaturation
In stable condition it is dissolved in liquid.
Further object is that a kind of method that preparing gas supersaturation liquid is provided so that gas can be satiated
Be dissolved in liquid, and keep stable at normal temperatures and pressures.
A further object of the present invention is to provide a kind of gas supersaturation liquid to improve at medical treatment, air, promote plant
Application in growth and aquaculture.
A kind of gas supersaturation liquid that the present invention provides, maximum oxygen content reaches 150mg/L, and oxygen content stationary value exists
65mg/L liquid, the liquid oxygen content detection value after placing 2 hours is at 63mg/L ± 1mg/L, and bottling keeps in Dark Place 1
Liquid oxygen content value after Nian is 35mg/L ± 1mg/L, the liquid oxygen content value after preserving 3 years be 22mg/L ±
1mg/L。
A kind of gas supersaturation liquid that the present invention provides, hydrogen content stationary value scope is at 3mg/L ± 1mg/L.
The gas supersaturation liquid of the present invention, its contained oxygen, it is dissolved in liquid (such as: water) with the form of oxygen molecule
In, and measured by dissolved oxygen water monitoring instrument.Its contained hydrogen, is dissolved in liquid (such as: water) with hydrionic form,
And pass through, hydrogen dissolving water Monitoring and Controlling instrument measures.
In order to obtain above-mentioned various gas supersaturation liquid, the present invention provides the side of a kind of preparing gas supersaturation liquid
Method, comprises the steps:
Pretreatment, the most first by the first water-gas mixer, the first nebulizer, the first ultrasound wave hydrone destroyer, second
Water-gas mixer, the second nebulizer, the second ultrasound wave hydrone destroyer, highfield, the 3rd water-gas mixer and
Two tanks, and connecting line is hydraulically full with each water pump；Then
After second stores the full liquid of water container storage, stop liquid goes successively to the first water-gas mixer, opens entering of gas
QI KOU, starts the first water pump and the 3rd water pump so that second stores the liquid storage in water container and gas, at each water pump
Under driving, successively in the first water-gas mixer, the first nebulizer, the first ultrasound wave hydrone destroyer, the second aqueous vapor
In blender, the second nebulizer, the second ultrasound wave hydrone destroyer, enter between highfield and the 3rd water-gas mixer
Row mixing and flowing, again return to the second storage water container after, enter again the first water-gas mixer, and constantly recycle stream
Dynamic, reach to stop during oxygen-containing stationary value 65mg/L ± 1mg/L or hydrogeneous 3mg/L ± 1mg/L, close gas inlet,
Stablize more than 30 minutes, release excessive gas.
For preparing gas supersaturation liquid of being more convenient for, improving gentle the avoiding of Automated water and pollute, the present invention provides another
The method planting preparing gas supersaturation liquid, comprises the steps:
Liquid enters the first water-gas mixer through the first ejecting device, then is delivered to the first atomization successively through the first water pump
Device, the first ultrasound wave hydrone destroyer, to the second water-gas mixer, the second nebulizer, the second ultrasound wave hydrone
Destroyer, highfield, enter the second tank to the 3rd water-gas mixer and the 3rd water pump；
After second stores the full liquid of water container storage, stop liquid goes successively to the first water-gas mixer, opens entering of gas
QI KOU, starts the first water pump and the 3rd water pump so that second stores the liquid storage in water container and gas, at each water pump
Under driving, successively in the first water-gas mixer, the first nebulizer, the first ultrasound wave hydrone destroyer, the second aqueous vapor
In blender, the second nebulizer, the second ultrasound wave hydrone destroyer, enter between highfield and the 3rd water-gas mixer
Row mixing and flowing, again return to the second storage water container after, enter again the first water-gas mixer, and constantly recycle stream
Dynamic, reach to stop during oxygen-containing stationary value 65mg/L ± 1mg/L or hydrogeneous 3mg/L ± 1mg/L, close gas inlet,
Stablize more than 30 minutes, release excessive gas.
In order to obtain above-mentioned various gas supersaturation liquid, the present invention provides the dress of a kind of preparing gas supersaturation liquid
Standby, including:
Liquid outlet and the first ejecting device connect, the inlet and outlet of the first water-gas mixer respectively with the first cartridge nozzle
Put and connect with the first water pump；First water pump, the first nebulizer, the first ultrasound wave hydrone destroyer, the second aqueous vapor are mixed
Clutch, the second ejecting device, the second nebulizer, the second ultrasound wave hydrone destroyer, highfield and the 3rd aqueous vapor are mixed
Clutch is sequentially connected with；The entrance of the second water pump and the outlet of the 3rd water-gas mixer and the first tank connects, and first
The outlet of tank then enters racking room；
3rd water pump exports with the 3rd water-gas mixer respectively and the entrance of the second tank is connected, the second tank
Outlet be connected with the first water-gas mixer；
The outlet of gas connects with the first water-gas mixer, the second water-gas mixer and the 3rd water-gas mixer respectively.
Equip the path of gas-liquid mixed and flowing in order to control the present invention, also set up some valves, such as: the first water pump and
First valve is set between the first nebulizer；Second valve is set between the 3rd water-gas mixer and the second water pump, and
3rd valve is set between the first tank and racking room, between the 3rd water-gas mixer and the 3rd water pump, arranges
Four valves.
The various gas supersaturation liquid that the present invention provides, can remarkably promote plant and animal growth, it is adaptable to crops
Produce and aquaculture so that plant and animal growth cycle is significantly shortened, and yield significantly improves.
The various gas supersaturation liquid that the present invention provides, moreover it is possible to as excellent solvent, improve the compatibility of material.
Accompanying drawing explanation
Fig. 1 is the route map of method one embodiment of preparing gas supersaturation liquid of the present invention.
Detailed description of the invention
Technical scheme is described in detail below in conjunction with accompanying drawing.The embodiment of the present invention is only in order to illustrate the skill of the present invention
Art scheme and unrestricted, although the present invention being described in detail with reference to preferred embodiment, the ordinary skill of this area
Personnel should be appreciated that and can modify or equivalent, the technical scheme of invention without deviating from the technology of the present invention
The spirit and scope of scheme, it all should be contained in scope of the presently claimed invention.
Fig. 1 is the route map of method one embodiment of preparing gas supersaturation liquid of the present invention.As it is shown in figure 1, liquid
1 outlet is connected with the first ejecting device (disposing nanometer film in it) 21, the inlet and outlet of the first water-gas mixer 20
It is connected with the first ejecting device 21 and the first water pump 3 respectively.First water pump the 3, first nebulizer the 5, first ultrasound wave
Hydrone destroyer the 6, second water-gas mixer the 7, second ejecting device (disposing nanometer film in it) the 22, second atomization
Device the 9, second ultrasound wave hydrone destroyer 10, highfield 11 and the 3rd water-gas mixer 8 are sequentially connected with.Second water
Pump 13 is connected with the outlet of the 3rd water-gas mixer 8 and the entrance of the first tank 14, the first tank 14
Outlet then enter racking room 16.
3rd water pump 18 exports with the 3rd water-gas mixer 8 respectively and the entrance of the second tank 17 is connected, and second
The outlet of tank 17 is connected with the first water-gas mixer 20.
Gas 2 exports and connects with first water-gas mixer the 20, second water-gas mixer 7 and the 3rd water-gas mixer 8 respectively
Logical, and mix with liquid 1.
In order to the gas and liquid that enter different device are controlled, also valve is set everywhere at stream, such as: first
Between water pump 3 and the first nebulizer 5, the first valve 4 is set；Set between 3rd water-gas mixer 8 and the second water pump 13
Put and the 3rd valve 15, the 3rd aqueous vapor are set between the second valve 12, and the first tank 14 and racking room 16
Blender 8 and the first water-gas mixer 20 arrange the 4th valve 19 between connecting.
When needing preparing gas supersaturation liquid, it is necessary to by first water-gas mixer the 20, first nebulizer 5, first
Ultrasound wave hydrone destroyer the 6, second water-gas mixer 7 is interior, second nebulizer the 9, second ultrasound wave hydrone crushes
Gas in the equipment such as device 10, highfield 11 and the 3rd water-gas mixer 8, and pipeline and water pump is discharged and (or is filled
Full liquid 1), then the second storage water container 17 of full for storage liquid 1 is connected with the first water-gas mixer 20, connects
And carry out following steps:
After second stores the full liquid 1 of water container 17 storage, stop liquid 1 enters the first water-gas mixer 20, opens gas
The air inlet of body 2, the first water pump 3 and the 3rd water pump 18 start so that second store liquid storage in water container 17 with
Gas 2, under each water pump drives, successively at first water-gas mixer the 20, first nebulizer the 5, first ultrasound wave
In hydrone destroyer the 6, second water-gas mixer 7, second nebulizer the 9, second ultrasound wave hydrone destroyer 10,
Highfield 11 and the 3rd water-gas mixer 8, again return to the second storage water container 17, and then reenter the first gas-vapor mix
Device 20 equipment room such as grade mixes and circulates, and reaches dissolved oxygen stable value 65mg/L ± 1mg/L (DO dissolved oxygen Monitoring and Controlling
Instrument, model LD3000, measurement range 0mg/L～200mg/L) or molten hydrogen 3mg/L ± 1mg/L (hydrogen dissolving water monitoring control
Instrument measurement range 0.1mg/L processed～10mg/L) quit work, close gas 2 air inlet, stablize more than 30 minutes,
Release excessive gas 2.Close the 4th 19 valve, open the second valve 12, start first water pump the 3, second water pump 13,
Closing the 3rd water pump 18 to make oxygen-containing or hydrogeneous liquid and squeeze in 14 storage buckets, these are through the first gas-vapor mix
Device the 20, second water-gas mixer 7 and the 3rd water-gas mixer 8 are sufficiently mixed, the most not gas in the liquid produced
Body.
The easiest another kind of gas discharged in each equipment, pipeline or parts, for exhaust mode (Purge in place
In Position), i.e. close the second valve 12 (opening the first valve 4 and the 4th valve 19) and the 3rd water pump 18.
Liquid 1 enters the first water-gas mixer 20 (A0200 type, river through the first ejecting device (disposing nanometer film in it) 21
The research and development of Chinese businessman thing Co., Ltd.), then it is delivered to first nebulizer the 5, first ultrasound wave moisture successively through the first water pump 3
Sub-destroyer 6 (purchased from Shenzhen Wei Tu Science and Technology Ltd.), second water-gas mixer the 7, second nebulizer 9, second
Ultrasound wave hydrone destroyer 10, highfield the 11, the 3rd water-gas mixer 8 and the 3rd water pump 18 enter the second water storage
Container 17.Afterwards, then by the liquid storage in the second storage water container 17 and gas 2, under each water pump drives, successively
At first water-gas mixer the 20, first nebulizer the 5, first ultrasound wave hydrone destroyer the 6, second water-gas mixer 7
In, second nebulizer the 9, second ultrasound wave hydrone destroyer 10, highfield 11 and the 3rd water-gas mixer 8, then
Return to the second storage water container 17, and then reenter the equipment room mixing such as the first water-gas mixer 20 and circulate.
From the first tank 14, obtain the oversaturated liquid of oxygen, measure its maximum oxygen content through dissolved oxygen meter and reach
150mg/L±1mg/L.After racking room fill, the oxygen content stationary value that dissolved oxygen meter records at 65mg/L ± 1mg/L,
Oxygen content detected value after placing 2 hours is at 63mg/L ± 1mg/L.After bottling is kept in Dark Place 1 year, then through dissolved oxygen meter
Measuring oxygen content value is 35mg/L ± 1mg/L, and the oxygen content value after preserving 3 years is 22mg/L ± 1mg/L.
By above-mentioned identical method, ionized device (purchased from Wal strange environmental protection (Shenzhen) company limited) is located in advance
The liquid 1 of reason can also prepare the oversaturated liquid of hydrion through surveying hydrogen content stationary value in 3mg/L ± 1mg/L (hydrogen-rich
Water monitoring controller measurement range 0.1mg/L～10mg/L).
The prepared oversaturated liquid of oxygen is used for soilless culture in Shanghai Communications University cultivation base, in identical cultivation
Under the conditions of, use the growth cycle contracting of the plant (such as: Fructus Lycopersici esculenti, Herba Apii graveolentis and Caulis et Folium Lactucae Sativae etc.) of the oversaturated liquid of oxygen
Short by 1/3.
The prepared oversaturated liquid of oxygen is used for breed in stew as water body, significantly improve fish pond anaerobic condition (such as:
Night and overcast and rainy), every mu of fish pond output increased to 30 tons～80 tons can be realized.
The prepared oversaturated liquid of hydrogen is added in cod-liver oil so that cod-liver oil about 1 minute can be by rapid solution.
Claims (14)
1. a gas supersaturation liquid, it is characterised in that described liquid is water, described gas is oxygen or hydrogen.
Gas supersaturation liquid the most according to claim 1, it is characterised in that the maximum oxygen content of described liquid reaches 150mg/L ± 1mg/L.
Gas supersaturation liquid the most according to claim 1, it is characterised in that the oxygen content stationary value of described liquid is at 65mg/L ± 1mg/L.
Gas supersaturation liquid the most according to claim 1, it is characterised in that the oxygen content detected value after described liquid is placed 2 hours is 63mg/L ± 1mg/L.
Gas supersaturation liquid the most according to claim 1, it is characterised in that the oxygen content value after the bottling of described liquid is kept in Dark Place 1 year is 35mg/L ± 1mg/L.
Gas supersaturation liquid the most according to claim 1, it is characterised in that described fluid preservation oxygen content value after 3 years is 22mg/L ± 1mg/L.
Gas supersaturation liquid the most according to claim 1, it is characterised in that described liquid hydrogen content stationary value is at 3mg/L ± 1mg/L.
Gas supersaturation liquid the most according to claim 1 is for medical treatment, air improvement, production estimation and aquaculture.
9. the method for the gas supersaturation liquid that one kind is produced described in claim 1, it is characterised in that comprise the steps:
Pretreatment, the most first by the first water-gas mixer, the first nebulizer, the first ultrasound wave hydrone destroyer, the second water-gas mixer, the second nebulizer, the second ultrasound wave hydrone destroyer, highfield, the 3rd water-gas mixer and the second tank, and connecting line is hydraulically full with each water pump；Then
After second stores the full liquid of water container storage, stop liquid goes successively to the first water-gas mixer, open the air inlet of gas, start the first water pump and the 3rd water pump, make the liquid storage in the second storage water container and gas, under each water pump drives, successively at the first water-gas mixer 20, first nebulizer 5, first ultrasound wave hydrone destroyer 6, in second water-gas mixer 7, second nebulizer 9, second ultrasound wave hydrone destroyer 10, highfield 11, carry out mixing and flowing between 3rd water-gas mixer 8, again return to the second described storage water container, and constantly circulate, stop when reaching oxygen-containing stationary value 65mg/L ± 1mg/L or hydrogeneous 3mg/L ± 1mg/L, close gas inlet, stablize more than 30 minutes, release excessive gas.
Method the most according to claim 9, it is characterised in that described pretreatment is:
Liquid enter through described first ejecting device described in the first water-gas mixer, then through the first described water pump be delivered to successively the first described nebulizer, the first described ultrasound wave hydrone destroyer, the second described water-gas mixer, the second described nebulizer, the second described ultrasound wave hydrone destroyer, described highfield, the 3rd described water-gas mixer and the 3rd described water pump enter described in the second tank.
11. methods according to claim 9, it is characterised in that mix with described gas after described liquid is also carried out ionizing pretreatment, and prepare the hydrogeneous liquid of supersaturation.
The equipment of the gas supersaturation liquid that 12. 1 kinds are produced described in claim 1, it is characterised in that including:
Liquid outlet and the first ejecting device connect, and the inlet and outlet of the first water-gas mixer is connected with the first described ejecting device and the first water pump respectively；First water pump, the first nebulizer, the first ultrasound wave hydrone destroyer, the second water-gas mixer, the second ejecting device, the second nebulizer, the second ultrasound wave hydrone destroyer, highfield and the 3rd water-gas mixer are sequentially connected with；Second water pump is connected with the outlet of the 3rd described water-gas mixer and the entrance of the first tank, and the outlet of the first tank then enters racking room；
3rd water pump exports with the 3rd described water-gas mixer respectively and the entrance of the second described tank is connected, and the outlet of the second tank is connected with the first water-gas mixer；
The outlet of described gas connects with the first described water-gas mixer, the second described water-gas mixer and the 3rd described water-gas mixer respectively.
13. equipments according to claim 12, it is characterised in that also include some valves.
14. equipments according to claim 12, it is characterised in that also include one or more following valves:
First valve, it is arranged between the first described water pump and the first described nebulizer；
Second valve, it is arranged between described the 3rd water-gas mixer and the second described water pump；
3rd valve, it is arranged between described the first tank and described racking room；And
4th valve, it is arranged between described the 3rd water-gas mixer and the 3rd described water pump.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610317895.0A CN106006913A (en) | 2016-05-12 | 2016-05-12 | Gas supersaturated liquid and preparation method and application thereof |
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| CN201610317895.0A CN106006913A (en) | 2016-05-12 | 2016-05-12 | Gas supersaturated liquid and preparation method and application thereof |
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| CN201610317895.0A Pending CN106006913A (en) | 2016-05-12 | 2016-05-12 | Gas supersaturated liquid and preparation method and application thereof |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108862536A (en) * | 2018-07-11 | 2018-11-23 | 王开明 | A kind of preparation method of the oxygen-containing hydrogeneous water of over-saturation |
| CN112956445A (en) * | 2021-04-09 | 2021-06-15 | 江皓 | System and method for transporting live fish by adopting nano bubble water |
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| CN101045588A (en) * | 2007-04-26 | 2007-10-03 | 陈启东 | Integral dispersion atomization aeration water quality regulating device |
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| CN112956445B (en) * | 2021-04-09 | 2024-03-26 | 江皓 | System and method for transporting live fish by using nano bubble water |
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Application publication date: 20161012 |
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