CN106334466A - Carbonate spring gas-liquid mixing device - Google Patents
Carbonate spring gas-liquid mixing device Download PDFInfo
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- CN106334466A CN106334466A CN201610952756.5A CN201610952756A CN106334466A CN 106334466 A CN106334466 A CN 106334466A CN 201610952756 A CN201610952756 A CN 201610952756A CN 106334466 A CN106334466 A CN 106334466A
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- Prior art keywords
- spray nozzle
- bubbler
- port
- export
- aperture
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- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 title claims abstract description 28
- 239000007788 liquid Substances 0.000 title abstract description 8
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 77
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 37
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 37
- 238000000889 atomisation Methods 0.000 claims abstract description 29
- 239000007921 spray Substances 0.000 claims description 109
- 238000009434 installation Methods 0.000 claims description 16
- 238000005507 spraying Methods 0.000 claims description 8
- 239000007789 gas Substances 0.000 description 16
- 239000000203 mixture Substances 0.000 description 14
- 239000008399 tap water Substances 0.000 description 6
- 235000020679 tap water Nutrition 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 4
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 239000008280 blood Substances 0.000 description 3
- 210000004369 blood Anatomy 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- FGRBYDKOBBBPOI-UHFFFAOYSA-N 10,10-dioxo-2-[4-(N-phenylanilino)phenyl]thioxanthen-9-one Chemical compound O=C1c2ccccc2S(=O)(=O)c2ccc(cc12)-c1ccc(cc1)N(c1ccccc1)c1ccccc1 FGRBYDKOBBBPOI-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 235000011089 carbon dioxide Nutrition 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 241000790917 Dioxys <bee> Species 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- JYYOBHFYCIDXHH-UHFFFAOYSA-N carbonic acid;hydrate Chemical compound O.OC(O)=O JYYOBHFYCIDXHH-UHFFFAOYSA-N 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000000338 in vitro Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 210000004877 mucosa Anatomy 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000002792 vascular Effects 0.000 description 1
- 210000001835 viscera Anatomy 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2311—Mounting the bubbling devices or the diffusers
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/52—Adding ingredients
- A23L2/54—Mixing with gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2311—Mounting the bubbling devices or the diffusers
- B01F23/23113—Mounting the bubbling devices or the diffusers characterised by the disposition of the bubbling elements in particular configurations, patterns or arrays
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
- B01F25/72—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/06—Mixing of food ingredients
- B01F2101/14—Mixing of ingredients for non-alcoholic beverages; Dissolving sugar in water
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Nozzles (AREA)
Abstract
The invention provides a carbonate spring gas-liquid mixing device. The carbonate spring gas-liquid mixing device comprises a water inlet pipe, a carbon dioxide inlet pipe, a mixing cavity, a first bubbler, a first atomization ejector, a second bubbler, a second atomization ejector, a third atomization ejector and a water outlet pipe, wherein the water outlet end of the water inlet pipe and the gas outlet end of the carbon dioxide inlet pipe are connected with the mixing cavity, the inlet end of the first bubbler is connected with the outlet end of the mixing cavity, the inlet end of the first atomization ejector is connected with the first bubbler, the inlet end of the second bubbler is connected with the outlet end of the first atomization ejector, the inlet end of the second atomization ejector is connected with the outlet end of the second bubbler, the inlet end of the third atomization ejector is connected with the outlet end of the second atomization ejector, and the outlet end of the third atomization ejector is connected with the water outlet pipe. The carbonate spring gas-liquid mixing device is simple in whole structure, high in efficiency and convenient to use and does not need power energy.
Description
Technical field
The present invention relates to a kind of carbonate spring Liqiud-gas mixing device.
Background technology
The main component of carbonate spring is free carbon dioxide, and its content is referred to as carbonate spring in more than 1000mg/l, is commonly called as
" natural soda pop ".
Carbonate spring has many effects to the teleneuron sensor of skin and mucosa.Temperature and tactile can be made to change
Become, during dipping bath, escape and enter in human body in the carbonic acid gas of in the air through respiratory tract, because in blood, carbonic acid Gas content increases, the sea of blood
Middle ph value temporarily changes.
Skin capillary vascular expansion during carbonate spring bath, erubescence, lead to internal organs blood to flow to body surface, in vitro all circulatings
Amount can increase and reaches 30%, thus alleviating heart burden, therefore think that carbonic acid bath is a kind of heart exercise factors.
Existing carbonate spring maker typically makes liquids and gases merge under stress using stirring means and obtains carbonic acid
Water.This needs exist for power blade, stirring vane, shaft, bearing, and injection apparatus etc. form, complex structure, and high cost has
Mechanical movement.
Generally use for current carbonate spring maker electronic, cause the technical problem of complex structure high cost, be ability
Domain technical problem urgently to be resolved hurrily.
Content of the invention
It is an object of the invention to provide a kind of carbonate spring Liqiud-gas mixing device, typically made with solving current carbonate spring maker
With electronic, cause the technical problem of complex structure high cost.
For solving above-mentioned technical problem, the invention provides a kind of carbonate spring Liqiud-gas mixing device, comprising:
Water inlet pipe；
Carbon dioxide pipe；
Hybrid chamber, the outlet side of the water side of described water inlet pipe and described carbon dioxide pipe is all connected with described hybrid chamber
Connect；
First bubbler, the entrance point of described first bubbler is connected with the port of export of described hybrid chamber；
First spray nozzle, the entrance point of described first spray nozzle is connected with the port of export of described first bubbler
Connect；
Second bubbler, the entrance point of described second bubbler is connected with the port of export of described first spray nozzle；
Second spray nozzle, the entrance point of described second spray nozzle is connected with the port of export of described second bubbler
Connect；
3rd spray nozzle, the entrance point of described 3rd spray nozzle and the port of export of described second spray nozzle
Connect；The port of export of described 3rd spray nozzle connects outlet pipe.
Further, also include:
It is arranged on described first bubbler, described first spray nozzle, described second bubbler, described second atomization spray
Installation shell outside emitter, described 3rd spray nozzle；Wherein,
Described installation inside the shell is provided with first being connected for described first spray nozzle with described second bubbler
Chamber resettling；
Described inside the shell is installed and is provided be connected with described 3rd spray nozzle for described second spray nozzle
Second chamber resettling；
Described installation inside the shell is provided with and houses for the described 3rd spray nozzle is connected with described outlet pipe the 3rd
Chamber；
Described water inlet pipe is embedded in described installation shell one end and is connected with described hybrid chamber, described carbon dioxide pipe
It is embedded in described installation shell one end region and is connected with described hybrid chamber, described outlet pipe is embedded another in described installation shell
One end.
Further, described carbon dioxide pipe arranges air relief valve.
Further, the port of export aperture of described first spray nozzle is less than the aperture of its entrance point；
The port of export aperture of described second spray nozzle is less than the aperture of its entrance point；
The port of export aperture of described 3rd spray nozzle is less than the aperture of its entrance point.
Further, the port of export aperture of described second spray nozzle is more than the port of export of described first spray nozzle
Aperture；
The port of export aperture of described 3rd spray nozzle is more than the port of export aperture of described second spray nozzle.
Further, described water inlet pipe embeds the described water side installing inside the shell part is bore change narrow structure.
Further, described outlet pipe pipe embeds the described water inlet end installing inside the shell part and broadens structure for bore.
Further, it is provided in described first spray nozzle spraying the porous nozzle clashing into atomization；
It is provided in described second spray nozzle spraying the porous nozzle clashing into atomization；
It is provided in described 3rd spray nozzle spraying the porous nozzle clashing into atomization.
Compared with prior art, the beneficial effects of the present invention is:
The present invention provide a kind of carbonate spring Liqiud-gas mixing device, including water inlet pipe, carbon dioxide pipe, hybrid chamber,
First bubbler, the first spray nozzle, the second bubbler, the second spray nozzle, the 3rd spray nozzle and outlet pipe, its
In, the outlet side of the water side of described water inlet pipe and described carbon dioxide pipe is all connected with described hybrid chamber；Described first
The entrance point of bubbler is connected with the port of export of described hybrid chamber；The entrance point of described first spray nozzle and described the first
The port of export of bubbler connects；The entrance point of described second bubbler is connected with the port of export of described first spray nozzle；Described
The entrance point of the second spray nozzle is connected with the port of export of described second bubbler；The entrance point of described 3rd spray nozzle
It is connected with the port of export of described second spray nozzle；The port of export of described 3rd spray nozzle connects outlet pipe.
Carry pressure in tap water water inlet pipe, tap water is injected hybrid chamber, meanwhile, carbon dioxide pipe is also by dioxy
Change carbon injection hybrid chamber, bubble with water mixed once and through the first bubbler in mixing intracavity carbon dioxide, through the first foaming
The gas-water mixture of a succession of bubble of self-assembling formation and water after device, gas-water mixture is atomized by the first spray nozzle,
Gas-water mixture local velocity and pressure is made to sharply increase suddenly, formation partial high pressure high-velocity flow is spouting, the height of ejection
Pressure high speed aqueous vapor reaches, through clashing into atomization, the purpose that air water merges at a high speed；By arranging the second bubbler, make carbon dioxide
Utilization rate is higher, finally by the second spray nozzle and the 3rd spray nozzle, makes mixing liquid become highly concentrated nano level
Apollinaris.Overall structure is simple, without the power supply energy, efficiency high, and easy to use.
The carbonate spring made of this carbonate spring Liqiud-gas mixing device, after testing, carbonate spring concentration ph of this device output is
4.9, after in mineral water bottle, lid bottle cap does not deposit 48 hours, ph concentration is 5.2, and tap water ph value is 7.0.
Brief description
Fig. 1 diagrammatically illustrates the structural representation of the embodiment of the present invention.
In figure reference:
1st, water inlet pipe；11. outlet pipes；2nd, carbon dioxide pipe；21st, air relief valve；3rd, hybrid chamber；4th, the first bubbler；
5th, the first spray nozzle；6th, the second bubbler；7th, the second spray nozzle；8th, the 3rd spray nozzle；9th, shell is installed；
91st, the first chamber resettling；92nd, the second chamber resettling；93rd, the 3rd chamber resettling.
Specific embodiment
Hereinafter embodiments of the invention are described in detail, but the present invention can be defined by the claims and cover
Multitude of different ways is implemented.
Refer to shown in Fig. 1, this carbonate spring Liqiud-gas mixing device includes: water inlet pipe 1, carbon dioxide pipe 2, hybrid chamber
3rd, the first bubbler 4, the first spray nozzle 5, the second bubbler 6, the second spray nozzle 7 and the 3rd spray nozzle 8；Enter
The outlet side of the water side of water pipe 1 and carbon dioxide pipe 2 is all connected with hybrid chamber 3；The entrance point of the first bubbler 4 with mixed
The port of export closing chamber 3 connects；The entrance point of the first spray nozzle 5 is connected with the port of export of the first bubbler 4；Second bubbler
6 entrance point is connected with the port of export of the first spray nozzle 5；The entrance point of the second spray nozzle 7 and the second bubbler 6
The port of export connects；The entrance point of the 3rd spray nozzle 8 is connected with the port of export of the second spray nozzle 7；3rd atomized spray
The port of export of device 8 connects outlet pipe 11.
Carry pressure in tap water water inlet pipe 1, tap water is injected hybrid chamber 3, meanwhile, carbon dioxide pipe 2 also will
The carbon dioxide injection hybrid chamber of certain pressure, in hybrid chamber 3, carbon dioxide is with water mixed once and through the first bubbler 4
Bubble, the gas-water mixture of a succession of bubble of self-assembling formation and water after the first bubbler 4, gas-water mixture passes through first and is atomized
Ejector 5 is atomized, and so that gas-water mixture local velocity and pressure is sharply increased suddenly, forms the spray of partial high pressure high-velocity flow
Penetrate, the high-voltage high-speed aqueous vapor of ejection reaches, through clashing into atomization, the purpose that air water merges at a high speed；By arranging second
Bubbler 6, makes utilization rate of carbon dioxide higher, finally by the second spray nozzle 7 and the 3rd spray nozzle 8, makes mixed liquor
Body becomes highly concentrated nano level apollinaris.Overall structure is simple, without other power supplys, efficiency high, and easy to use.
This carbonate spring Liqiud-gas mixing device also includes: is arranged on the first bubbler 4, the first spray nozzle 5, second bubbles
Installation shell 9 outside device 6, the second spray nozzle 7, the 3rd spray nozzle 8；Wherein, install in shell 9 and be provided with for the
The first chamber resettling 91 that one spray nozzle 5 is connected with the second bubbler 6；Install and be provided with shell 9 for the second atomization
The second chamber resettling 92 that ejector 7 is connected with the 3rd spray nozzle 8；Install and be provided with shell 1 for the 3rd atomization spray
The 3rd chamber resettling 93 that emitter 8 is connected with outlet pipe 11；Water inlet pipe 1 is embedded in installation shell 9 one end and is connected with hybrid chamber 3
Connect, carbon dioxide pipe 2 is embedded in installation shell 9 one end region and is connected with hybrid chamber 3, outlet pipe 11 is embedded to be installed
Shell 9 other end.
Shell 9 is installed by setting, this carbonate spring Liqiud-gas mixing device can be made to be in integrative-structure, integrated connection is compact,
And it is easy to install.
Air relief valve 21 is arranged on carbon dioxide pipe 2.Carbon dioxide pipe 2 can be directly connected to carbon dioxide gas storage
Tank, in order that carbon dioxide pressure is consistent with water inlet pipe pressure, needs to enter the air relief valve 21 on carbon dioxide water inlet pipe 2
Row pressure regulation is reduced pressure, in order to adapt to job demand；And by the design of air relief valve 21, can with regulation of carbon dioxide air inflow,
Outlet pipe 2 is enable to export the carbonate spring of different gas concentration lwevels.
The port of export aperture of the first spray nozzle 5 is less than the aperture of its entrance point；The port of export of the second spray nozzle 7
Aperture is less than the aperture of its entrance point；The port of export aperture of the 3rd spray nozzle 8 is less than the aperture of its entrance point.
By will be little for the port of export bore of the first spray nozzle 5, the second spray nozzle 7 and the 3rd spray nozzle 8
In its entrance point bore, make gas-water mixture when reaching one-level jet atomization, because the aperture of the shower nozzle of spray nozzle is anxious
Reduce sharply little, so that gas-water mixture local velocity and pressure is sharply increased suddenly, formation partial high pressure high-velocity flow is spouting, spray
The high-voltage high-speed aqueous vapor going out reaches, through clashing into atomization, the purpose that air water merges at a high speed.
The port of export aperture of the second spray nozzle 7 is more than the port of export aperture of the first spray nozzle 5；3rd atomization spray
The port of export aperture of emitter 8 is more than the port of export aperture of the second spray nozzle 7.According to the principle of fluid, spray nozzle
The aperture of port of export aperture ratio upper level is larger, that is, the port of export aperture of the second spray nozzle 7 is more than the first mist
Change the port of export aperture of ejector 5；The port of export aperture of the 3rd spray nozzle 8 is more than the port of export of the second spray nozzle 7
Aperture；This structure design is primarily to prevent gas liquid mixture from passing through the pressure ratio after spray nozzle in flow process
Above high, form the phenomenon that builds the pressure, cause whole device failure.
The water side that water inlet pipe 1 embeds installation shell 9 interior part is that bore becomes narrow structure.This structure setting can make water inlet
Pipe 1 intake pressure becomes big, is easy in water inlet pipe water with carbon dioxide mix evenly.
Outlet pipe 11 pipe is embedded to be installed the water inlet end of shell 9 interior part and broadens structure for bore.This structure setting can make
Outlet pipe goes out under 11 water pressures changes, so that water is mixed homogeneously again with carbon dioxide.Setting in described first spray nozzle 5 is used
Clash into the porous nozzle of atomization in injection；It is provided in described second spray nozzle 7 spraying the porous nozzle clashing into atomization；
It is provided in described 3rd spray nozzle 8 spraying the porous nozzle clashing into atomization, by using porous nozzle, one can be entered
Step improves atomizing effect.
The embodiment of the present invention is the product made by the technique processing method that liquefied gass are atomized after bubbler；As
Fruit is further added by power source can increase the process of ejector oxygen supplement.
The operation principle of the embodiment of the present invention is:
As shown in figure 1, opening tap water to pass water through the hybrid chamber 3 that water inlet pipe 1 enters carbonate spring Liqiud-gas mixing device, so
After open dioxide bottle switch, adjusting pressure valve 21 makes pressure carbon dioxide be slightly above hydraulic pressure and by carbon dioxide
Pipe 2 enters hybrid chamber 3, water and carbon dioxide mix homogeneously in the hybrid chamber 3 before the first bubbler 4, after the first bubbler 4
The a succession of bubble of self-assembling formation and the gas-water mixture of water.Gas-water mixture is passed onwards to the first spray nozzle 5, due to first
The aperture of spray nozzle 5 strongly reduces, so that gas-water mixture local velocity and pressure sharply increase suddenly, forms local
High-voltage high-speed water flow jet and go out, the high-voltage high-speed aqueous vapor of ejection reaches, through clashing into atomization, the purpose that air water merges at a high speed.
In order to more fully utilize carbon dioxide, perhaps the residual gas after the first spray nozzle atomization can form larger
Bubble, so increased the second bubbler 6, principle as before, is atomized through secondary impact.Obtain more aqueous vapors molten
Solution.Then flow out after the shock atomization of the 3rd spray nozzle again.Obtain highly concentrated nano level apollinaris.
This apparatus structure is simple, small volume.Low cost, easy processing, not electricity consumption, mechanical is moved, non-maintaining.Install and use
Convenient it is only necessary to open faucet and carbon dioxide valve can be obtained by nanoscale high concentration carbon sour water.Change the outfit other gases
Obtain different mixing liquids, if increase ejector both can realize cultivating oxygen supplement.
These are only the preferred embodiments of the present invention, be not limited to the present invention, for those skilled in the art
For member, the present invention can have various modifications and variations.All any modifications within the spirit and principles in the present invention, made,
Equivalent, improvement etc., should be included within the scope of the present invention.
Claims (8)
1. a kind of carbonate spring Liqiud-gas mixing device is it is characterised in that include:
Water inlet pipe (1)；
Carbon dioxide pipe (2)；
Hybrid chamber (3), the water side of described water inlet pipe (1) and the outlet side of described carbon dioxide pipe (2) are all mixed with described
Close chamber (3) to connect；
First bubbler (4), the entrance point of described first bubbler (4) is connected with the port of export of described hybrid chamber (3)；
The outlet of the first spray nozzle (5), the entrance point of described first spray nozzle (5) and described first bubbler (4)
End connects；
Second bubbler (6), the entrance point of described second bubbler (6) is connected with the port of export of described first spray nozzle (5)
Connect；
The outlet of the second spray nozzle (7), the entrance point of described second spray nozzle (7) and described second bubbler (6)
End connects；
3rd spray nozzle (8), the entrance point of described 3rd spray nozzle (8) and described second spray nozzle (7)
The port of export connects；The port of export of described 3rd spray nozzle (8) connects outlet pipe (11).
2. carbonate spring Liqiud-gas mixing device according to claim 1 is it is characterised in that also include:
Be arranged on described first bubbler (4), described first spray nozzle (5), described second bubbler (6), described second
Spray nozzle (7), described 3rd spray nozzle (8) installation shell (9) outward；Wherein,
Described install to be provided with shell (9) be connected with described second bubbler (6) for described first spray nozzle (5)
First chamber resettling (91)；
It is provided with described installation shell (9) for described second spray nozzle (7) with described 3rd spray nozzle (8) even
The second chamber resettling (92) connecing；
Described installation is provided with the being connected for described 3rd spray nozzle (8) with described outlet pipe (11) in shell (1)
Three chamber resettling (93)；
Described water inlet pipe (1) is embedded in described installation shell (9) one end and is connected with described hybrid chamber (3), described carbon dioxide
Air inlet pipe (2) is embedded in described installation shell (9) one end region and is connected with described hybrid chamber (3), described outlet pipe (11)
It is embedded in described installation shell (9) other end.
3. carbonate spring Liqiud-gas mixing device according to claim 2 is it is characterised in that described carbon dioxide pipe (2)
Upper setting air relief valve (21).
4. carbonate spring Liqiud-gas mixing device according to claim 3 is it is characterised in that described first spray nozzle (5)
Port of export aperture be less than its entrance point aperture；
The port of export aperture of described second spray nozzle (7) is less than the aperture of its entrance point；
The port of export aperture of described 3rd spray nozzle (8) is less than the aperture of its entrance point.
5. carbonate spring Liqiud-gas mixing device according to claim 4 is it is characterised in that described second spray nozzle (7)
Port of export aperture be more than described first spray nozzle (5) port of export aperture；
The port of export aperture of described 3rd spray nozzle (8) is more than the port of export aperture of described second spray nozzle (7).
6. carbonate spring Liqiud-gas mixing device according to claim 5 is it is characterised in that described water inlet pipe (1) is embedded described
The water side installing shell (9) interior part becomes narrow structure for bore.
7. carbonate spring Liqiud-gas mixing device according to claim 5 is it is characterised in that described outlet pipe (11) pipe embeds institute
State and the water inlet end of shell (9) interior part is installed broadens structure for bore.
8. carbonate spring Liqiud-gas mixing device according to claim 5 is it is characterised in that described first spray nozzle (5)
Inside it is provided for spraying the porous nozzle clashing into atomization；
It is provided in described second spray nozzle (7) spraying the porous nozzle clashing into atomization；
It is provided in described 3rd spray nozzle (8) spraying the porous nozzle clashing into atomization.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610952756.5A CN106334466A (en) | 2016-11-02 | 2016-11-02 | Carbonate spring gas-liquid mixing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610952756.5A CN106334466A (en) | 2016-11-02 | 2016-11-02 | Carbonate spring gas-liquid mixing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106334466A true CN106334466A (en) | 2017-01-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610952756.5A Pending CN106334466A (en) | 2016-11-02 | 2016-11-02 | Carbonate spring gas-liquid mixing device |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108543430A (en) * | 2018-07-02 | 2018-09-18 | 厦门松霖科技股份有限公司 | Discharging device |
| CN109663518A (en) * | 2019-01-16 | 2019-04-23 | 凡吾科技(上海)有限公司 | The preparation method and preparation facilities of the gas liquid mixture of a kind of carbon dioxide and water |
| CN109966941A (en) * | 2019-05-13 | 2019-07-05 | 江苏炬焰智能科技有限公司 | Carbonate spring mixer |
| CN110732283A (en) * | 2019-09-30 | 2020-01-31 | 中国矿业大学 | Preparation system and use method of coal-electricity -integrated three-waste-base foaming material |
| CN111810955A (en) * | 2019-04-10 | 2020-10-23 | 金泰旭 | Fine dust reducing device for incineration facility |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108543430A (en) * | 2018-07-02 | 2018-09-18 | 厦门松霖科技股份有限公司 | Discharging device |
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| CN111810955A (en) * | 2019-04-10 | 2020-10-23 | 金泰旭 | Fine dust reducing device for incineration facility |
| CN111810955B (en) * | 2019-04-10 | 2022-11-29 | 金泰旭 | Fine dust reducing device for incineration facility |
| CN109966941A (en) * | 2019-05-13 | 2019-07-05 | 江苏炬焰智能科技有限公司 | Carbonate spring mixer |
| CN110732283A (en) * | 2019-09-30 | 2020-01-31 | 中国矿业大学 | Preparation system and use method of coal-electricity -integrated three-waste-base foaming material |
| CN110732283B (en) * | 2019-09-30 | 2023-07-18 | 中国矿业大学 | Preparation system of coal-electricity integrated three-waste-based foaming material and application method thereof |
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