CN107213835A - Device for preparing carbonated spring - Google Patents
Device for preparing carbonated spring Download PDFInfo
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- CN107213835A CN107213835A CN201710461613.9A CN201710461613A CN107213835A CN 107213835 A CN107213835 A CN 107213835A CN 201710461613 A CN201710461613 A CN 201710461613A CN 107213835 A CN107213835 A CN 107213835A
- Authority
- CN
- China
- Prior art keywords
- gas
- pipe
- liquid
- supercharging
- pressurizing
- Prior art date
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- 239000007788 liquid Substances 0.000 claims abstract description 67
- 238000002156 mixing Methods 0.000 claims abstract description 17
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 25
- 239000011148 porous material Substances 0.000 claims description 6
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 230000001914 calming effect Effects 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 82
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 36
- 239000001569 carbon dioxide Substances 0.000 abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 20
- 238000000554 physical therapy Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 2
- 150000003384 small molecules Chemical class 0.000 abstract description 2
- 230000003139 buffering effect Effects 0.000 abstract 3
- 238000005192 partition Methods 0.000 abstract 3
- 238000007670 refining Methods 0.000 abstract 2
- 238000011065 in-situ storage Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 53
- 229960004424 carbon dioxide Drugs 0.000 description 35
- 239000000203 mixture Substances 0.000 description 8
- 238000005457 optimization Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 208000035475 disorder Diseases 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 208000013016 Hypoglycemia Diseases 0.000 description 1
- 208000004210 Pressure Ulcer Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000017531 blood circulation Effects 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000004087 circulation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 230000002218 hypoglycaemic effect Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000001734 parasympathetic effect Effects 0.000 description 1
- 230000003836 peripheral circulation Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000002889 sympathetic effect Effects 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 230000004218 vascular function Effects 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
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/70—Mixers specially adapted for working at sub- or super-atmospheric pressure, e.g. combined with de-foaming
- B01F33/71—Mixers specially adapted for working at sub- or super-atmospheric pressure, e.g. combined with de-foaming working at super-atmospheric pressure, e.g. in pressurised vessels
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61H—PHYSICAL THERAPY APPARATUS, e.g. DEVICES FOR LOCATING OR STIMULATING REFLEX POINTS IN THE BODY; ARTIFICIAL RESPIRATION; MASSAGE; BATHING DEVICES FOR SPECIAL THERAPEUTIC OR HYGIENIC PURPOSES OR SPECIFIC PARTS OF THE BODY
- A61H33/00—Bathing devices for special therapeutic or hygienic purposes
- A61H33/02—Bathing devices for use with gas-containing liquid, or liquid in which gas is led or generated, e.g. carbon dioxide baths
-
- 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
- B01F23/2312—Diffusers
-
- 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
- B01F23/2366—Parts; Accessories
-
- 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
- B01F23/29—Mixing systems, i.e. flow charts or diagrams
-
- 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
-
- 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
-
- 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
-
- 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
- B01F2101/305—Treatment of water, waste water or sewage
Abstract
The invention discloses a device for preparing carbonated spring, which comprises a gas refining pipe, a mixing pressurizing device and a buffering device, wherein the mixing pressurizing device comprises a gas-liquid mixing pipe and a pressurizing device, the bottom of the gas-liquid mixing pipe is communicated with the top of the pressurizing device, the middle of the pressurizing device is a pressurizing cavity, the bottom of the pressurizing device is provided with a pressurizing partition plate, the pressurizing partition plate is provided with a through hole, the gas outlet end of the gas refining pipe extends into the gas-liquid mixing pipe, the top of the buffering device is hermetically connected with the edge of the pressurizing partition plate, and the middle of the buffering device is provided with a longitudinal cavity. The device can more effectively refine gas molecular groups (such as carbon dioxide), lock small molecules (carbon dioxide) in liquid (such as water), and improve the gas utilization rate; the structure is simple, the maintenance is convenient, the blockage is not easy to happen, and the device can be manufactured and used at the present; the concentration of the carbonated spring prepared in situ by the device can reach over 1000mg/L, thereby having the function of physical therapy.
Description
Technical field
The present invention relates to solution preparing technical field, especially a kind of device for preparing carbonate spring.
Background technology
The pH value of carbon acid solution is in 4.5-5.5 or so, in faintly acid, with sterilizing function, and pH value and the skin head of people
The pH value of hair is close, more has affinity than common water；Concentration is obvious in 1000ppm carbonate spring convalescent effect, for example, carbonic acid
A carbon dioxide part in spring is absorbed, and can be improved vascular function, be reduced blood viscosity；Blood circulation can be improved, dropped
Hypoglycemia and glucose in urine；To bedsore, peripheral circulation disorderses have mitigation abirritation；The self-discipline caused by the factors such as pressure can be improved
The symptoms such as nervous disorder, adjust sympathetic and parasympathetic balance；Playing the role of lifting to exercise performance improves；With reparation
Impaired skin surface and hair ability.Unabsorbed another part has stronger decontamination ability to body surface in carbonate spring.
The manufacture method of current carbonate spring：Make the carbon dioxide bubble of medicament reaction generation, with pressurized tank by carbon dioxide
With high pressure, the mode of cooling is pressed into warm water, is forced to make carbon dioxide mix with water with agitating mode.Using medicament and with stirring
The carbonate spring concentration that mode is made does not reach more than 1000mg/L, and pressurized tank prepares carbon dioxide in the way of high pressure, equipment
Complexity, a small amount of manufacture carbonic acid is inconvenient.Medicament and the carbonate spring concentration being made of agitating mode do not reach 1000mg/L, mainly
Because the carbon dioxide molecule group in water is too big, bigger micel is easily gathered into, and escapes.
Number of patent application 201010184456X patent application discloses carbonate spring producing system, and this has invented offer
It is a kind of the carbonate spring generating means of carbonate spring to be efficiently produced without raising hydraulic pressure, including it is mixed with carbon dioxide bubble
The gas bubble stream of water flowing, gas bubble stream has：At least one distributary division and pressure retaining parts, the distributary division
Split carbon dioxide bubble, outlet side one end that the pressure is maintained at gas bubble stream is maintained in gas bubble stream
Hydraulic pressure, the effective diameter of gas bubble stream is determined, to cause the bubble under the flow velocity of the water of gas bubble flow path
Viscous drag, as carbon dioxide bubble for the effective diameter maximum diameter in the case of carbon dioxide bubble buoyancy more than,
The effective diameter of restriction is smaller than gas bubble stream.But due to, without hydraulic pressure is improved, using circulation mixed dissolution in the invention
Stream, not only causes the cost prepared to uprise, preparation amount tails off, and carbonate spring easily causes effusion now in flowing flow process
As so that the concentration of carbonate spring does not reach 1000mg/L, and using effect is not good.
The content of the invention
Based on this, providing one kind it is an object of the invention to overcome in place of above-mentioned the deficiencies in the prior art can be by carbon in water
Acid concentration is promoted to 1000mg/L, and device simple in construction.
To achieve the above object, the technical scheme taken of the present invention is：A kind of device for preparing carbonate spring, including gas are thin
Change pipe, mixing supercharging device and buffer unit, the mixing supercharging device includes gas-liquid mixed pipe and supercharging device, the gas-liquid
The bottom of mixing tube is connected with the top of the supercharging device, and the middle part of the supercharging device is booster cavity, the supercharging device
Bottom provided with supercharging dividing plate, the supercharging dividing plate is provided with through hole, and the gas-liquid is stretched into the outlet side of gas refinement pipe
In mixing tube, the top of the buffer unit is connected with the edge seal of the supercharging dividing plate, is set in the middle part of the buffer unit
There is lengthwise cavity.
Thus, pipe is refined by gas and gas is refined into smaller bubble, gas and liquid are realized in gas-liquid mixed pipe
The mixing of body, subsequently into booster cavity, is rebounded the gas-liquid mixture preferentially entered by supercharging dividing plate, with follow-up gas-liquid mixed
Thing is collided, the gas content in lifting liquid, and then, gas-liquid mixture enters lengthwise cavity by through hole, due to lengthwise cavity
Depth is very big, lengthwise cavity bottom formed one have cushion pad act on puddle, above through hole outflow gas-liquid mixed
Thing little by little flows into puddle, a similar waterfall, and gas is by taking carbon dioxide as an example, because carbonic acid is unstable, the shape in booster cavity
Into carbonic acid, reached by being pressurized dividing plate in lengthwise cavity, a part of carbonic acid can discharge carbon dioxide to above puddle, formation
The carbon dioxide of high concentration, then, puddle is slowly flowed into by the carbon dioxide of through hole and the mixed solution of carbonic acid,
During by high concentration carbon dioxide gas above puddle, a part of carbon dioxide can be absorbed；The cushion pad effect of puddle can
To avoid mixed solution from occurring fierce collision, it is to avoid carbon dioxide is escaped from carbonic acid；Meanwhile, through hole limits gas-liquid mixed
The flow of thing, can slow down contact area and the time of flow velocity, increase gas and liquid, further lift gas in liquid (water)
The concentration of (carbon dioxide).
As the further optimization of such scheme, the outlet side of the gas refinement pipe is provided with shower nozzle, the shower nozzle
Provided with pore.Thus, due to foring the carbon dioxide molecule groups of many agglomerates in high pressure titanium dioxide gas, it is difficult to be dissolved into water
In, and easily escape, the micel formed in gases at high pressure can be refined and cut by a diameter of 0.2~0.5mm pore
For micron-sized bubble, the solubility of gas in a liquid is improved；The number of pore can be adjusted as needed, Ke Yishi
It is 1,2,3,5, even more.
As the further optimization of such scheme, the bottom of the gas-liquid mixed pipe is provided with liquid outlet, the liquid outlet position
The lower section of the outlet side of pipe is refined in the gas.Thus, booster cavity, gas-liquid mixture are immediately entered after gas and liquid mixing
Most of kinetic energy is remained, then, gas-liquid mixture is higher by the speed after the bounce-back of supercharging dividing plate, improve the fierce journey of collision
Degree, more gases are pressed into liquid.
As the further optimization of such scheme, the supercharging dividing plate is provided with multiple through holes, and the multiple through hole is located at
The liquid outlet with it is described supercharging dividing plate just to position outside.Thus, the gas-liquid mixture into booster cavity all rebounds, with
Fierce collide occurs for follow-up gas-liquid mixture.
As the further optimization of such scheme, the internal diameter of the gas-liquid mixed pipe gradually becomes from liquid feeding end to liquid outlet
It is small.Thus, the similar taper of passage in gas-liquid mixed pipe, the liquid that can be accelerated into, the collision of lift gas and liquid swashs
Strong degree.
As the further optimization of such scheme, the device for preparing carbonate spring also includes feed tube, the feed tube
Connected with the gas-liquid mixed pipe, the feed tube is provided with flow sensor.Thus, it is possible to which monitoring in real time and regulation gas-liquid are mixed
Close the flow of the liquid in pipe.
As the further optimization of such scheme, the device for preparing carbonate spring also includes high pressure gas holder and communicating pipe,
The inlet end that described communicating pipe one end refines pipe with the gas is connected, and the other end of the communicating pipe connects with the high pressure gas holder
It is logical.
As the further optimization of such scheme, be additionally provided with the communicating pipe pressure regulator valve, pressure sensor, magnetic valve,
At least one of check valve and regulating valve.Thus, pressure regulator valve can adjust the air pressure that gas in pipe is refined into gas, pressure
Sensor facilitates background computer to monitor and adjust in real time the air pressure that interior gas is managed in gas refinement by software, and solenoid valve control connects
The folding of siphunculus, check valve ensures that gas refinement may not flow into liquid in managing, and regulating valve can control communicating pipe relevant position
Internal diameter size.
In summary, beneficial effects of the present invention are：
The more effective attenuating gas micel (such as carbon dioxide) of device energy of the present invention, small molecule (carbon dioxide) is locked
In liquid (such as water), gas effciency is improved；Its is simple in construction, easy to maintenance, is difficult to block up, can now-making-now-using；By this
The carbonate spring concentration that the device of invention is now made can reach more than 1000mg/L, thus with physiotherapy function.
Brief description of the drawings
Fig. 1 is the structural representation of embodiments of the invention one；
Fig. 2 is the structural representation that gas refines pipe；
Fig. 3 is the structural representation of shower nozzle；
Wherein, 1, high pressure gas holder, 2, communicating pipe, 3, feed tube, 4, gas refinement pipe, 5, buffer unit, 6, gas-liquid mixed
Pipe, 7, supercharging device, 8, booster cavity, 9, supercharging dividing plate, 10, through hole, 11, lengthwise cavity, 12, flow sensor, 13, air inlet
End, 14, shower nozzle, 15, pore, 16, liquid outlet, 17, pressure regulator valve, 18, pressure sensor, 19, magnetic valve, 20, check valve, 21,
Regulating valve.
Embodiment
To better illustrate the object, technical solutions and advantages of the present invention, below in conjunction with the drawings and specific embodiments pair
The present invention is described further.
Embodiment 1
As shown in Figure 1, Figure 2 and Figure 3, a kind of device for preparing carbonate spring, including high pressure gas holder 1, communicating pipe 2, feed tube
3rd, gas refinement pipe 4, mixing supercharging device and buffer unit 5, mixing supercharging device include gas-liquid mixed pipe 6 and supercharging device 7,
The bottom of gas-liquid mixed pipe 6 is connected with the top of supercharging device, and the middle part of supercharging device is booster cavity 8, the bottom of supercharging device 7
Provided with supercharging dividing plate 9, supercharging dividing plate is provided with multiple through holes 10, and the outlet side of gas refinement pipe 4 is stretched into gas-liquid mixed pipe, delayed
The top of flushing device is connected with being pressurized the edge seal of dividing plate, and the middle part of buffer unit is provided with lengthwise cavity 11；Feed tube 3 and gas
Liquid mixing tube 6 is connected, and feed tube 2 is provided with flow sensor 12；Communicating pipe one end with gas refine pipe 4 inlet end 13 connect
Connect, the other end of communicating pipe is connected with high pressure gas holder 1.
Wherein, the outlet side of gas refinement pipe 4 is provided with shower nozzle 14, and the shower nozzle is provided with multiple pores 15；Gas-liquid is mixed
The bottom for closing pipe 6 is provided with liquid outlet 16, and liquid outlet 16 is located at the underface that gas refines the outlet side of pipe 4；
Multiple through holes 10 be located at liquid outlet 16 with supercharging dividing plate 9 just to position outside；The internal diameter of gas-liquid mixed pipe 6 is from entering
Liquid end is tapered into liquid outlet；Pressure regulator valve 17, pressure sensor 18, magnetic valve 19, check valve are also sequentially provided with communicating pipe 2
20 and regulating valve 21.
The device of the present embodiment is when applied to carbonate spring is prepared, and water flows through feed tube into gas-liquid mixed pipe, and by gas
The carbon dioxide that body refinement pipe enters, collides mutually be sufficiently mixed here, carbon dioxide is refined as micron-sized two through shower nozzle
After carbonoxide bubble, squeeze between hydrone at a high speed, carbon dioxide can be made more preferably to be dissolved into water, form carbonate spring；Fierce
Impact improves the concentration of carbon dioxide in carbonate spring, and the carbonate spring of subsequent high concentration is flowed into booster cavity, newly-generated carbonic acid
Spring is in the case where the pressure of booster cavity is kept, and carbon dioxide is substantially dissolved in water, forms higher concentration and stable carbonate spring, then
More carbon dioxide are further absorbed in into the lengthwise cavity of buffer unit, so that condition of the carbon dioxide at 40 DEG C
Under concentration in water reach more than 1000mg/L.
Compared to general agitating mode, the mixing of carbon dioxide and 40 degree of warm water, the utilization rate of gas is about 20%~
35%；Under the same conditions, using the device of the present embodiment, the utilization rate of carbon dioxide is up to more than 55%.
On the other hand, the carbon dioxide in high pressure gas holder is successively by pressure regulator valve, pressure sensor, and pressure sensor is letter
Number send control centre to, judge whether air pressure meets preparation condition by control centre；Warm water enters from feed tube, flows through flow
Sensor, enters back into gas-liquid mixed pipe, afterwards into booster cavity, and flow signal is sent to control centre by flow sensor, by
Control centre judges whether water-carrying capacity situation meets preparation condition；
When air pressure and warm water flow reach the scope of setting, control centre provides the electric signal that can be prepared；Pass through control
The electric signal break-make is made, magnetic valve folding is controlled, the break-make purpose of control gas circuit is reached.Electric signal turn on, then magnetic valve from
Normally off is opened.Carbon dioxide in high pressure gas holder is by the magnetic valve of unlatching, after check valve, into gas-liquid mixed pipe.
Compared with prior art, its advantage is the device of the present embodiment：Gas refinement pipe is built-in with can be by gas
It is refined as the shower nozzle of microbubble, gas-liquid mixture is successively sufficiently mixed in the lengthwise cavity of booster cavity, buffer unit again, is carried
High solubility of the carbon dioxide in water, and carbon dioxide utilization rate so that bar of the carbon dioxide at 40 DEG C in water
Under part, once prepare concentration and reach more than 1000mg/L, so as to meet the requirement of physiotherapy.
Finally, it should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention rather than the present invention is protected
The limitation of scope is protected, although being explained in detail with reference to preferred embodiment to the present invention, one of ordinary skill in the art should
Understand, technical scheme can be modified or equivalent substitution, without departing from the essence of technical solution of the present invention
And scope.
Claims (8)
1. a kind of device for preparing carbonate spring, it is characterised in that including gas refinement pipe, mixing supercharging device and buffer unit,
The mixing supercharging device includes gas-liquid mixed pipe and supercharging device, bottom and the supercharging device of the gas-liquid mixed pipe
Top is connected, and the middle part of the supercharging device is booster cavity, the bottom of the supercharging device provided with supercharging dividing plate, the supercharging every
Plate is provided with through hole,
The outlet side of the gas refinement pipe is stretched into the gas-liquid mixed pipe,
The top of the buffer unit is connected with the edge seal of the supercharging dividing plate, and the middle part of the buffer unit is provided with lengthwise
Cavity.
2. device according to claim 1, it is characterised in that the outlet side of the gas refinement pipe is provided with shower nozzle, institute
Shower nozzle is stated provided with pore.
3. device according to claim 1, it is characterised in that the bottom of the gas-liquid mixed pipe is provided with liquid outlet, described
Liquid outlet is located at the lower section that the gas refines the outlet side of pipe.
4. device according to claim 3, it is characterised in that the supercharging dividing plate is provided with multiple through holes, the multiple
Through hole be located at the liquid outlet with it is described supercharging dividing plate just to position outside.
5. the device according to claim 3 or 4, it is characterised in that the internal diameter of the gas-liquid mixed pipe is from liquid feeding end to going out
Liquid mouthful is tapered into.
6. device according to claim 1, it is characterised in that the device for preparing carbonate spring also includes feed tube, institute
State feed tube to connect with the gas-liquid mixed pipe, the feed tube is provided with flow sensor.
7. device according to claim 1, it is characterised in that the device for preparing carbonate spring also include high pressure gas holder and
Communicating pipe, the inlet end that described communicating pipe one end refines pipe with the gas is connected, the other end of the communicating pipe and the height
Tank of calming the anger is connected.
8. device according to claim 7, it is characterised in that be additionally provided with the communicating pipe pressure regulator valve, pressure sensor,
At least one of magnetic valve, check valve and regulating valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710461613.9A CN107213835A (en) | 2017-06-16 | 2017-06-16 | Device for preparing carbonated spring |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710461613.9A CN107213835A (en) | 2017-06-16 | 2017-06-16 | Device for preparing carbonated spring |
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| CN107213835A true CN107213835A (en) | 2017-09-29 |
Family
ID=59949820
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| Application Number | Title | Priority Date | Filing Date |
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| CN201710461613.9A Pending CN107213835A (en) | 2017-06-16 | 2017-06-16 | Device for preparing carbonated spring |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107827187A (en) * | 2017-11-06 | 2018-03-23 | 深圳市长天长空智能设备科技有限公司 | A kind of water sludge interface nanometer air floatation machine |
| CN108295683A (en) * | 2018-02-01 | 2018-07-20 | 苏州碳酸泉贸易有限公司 | A kind of novel carbonate spring manufacturing 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 |
| CN111115787A (en) * | 2020-01-17 | 2020-05-08 | 南京昭凌精密机械有限公司 | Fusion device for preparing high-concentration carbonic acid spring |
| CN111420605A (en) * | 2020-04-22 | 2020-07-17 | 重庆冷泉科技有限公司 | Carbonic acid spring preparation facilities |
| CN111659272A (en) * | 2020-06-19 | 2020-09-15 | 御府汤(宁波)温泉开发有限公司 | Carbonic acid bath system and carbonization generating device |
| CN112007530A (en) * | 2020-07-08 | 2020-12-01 | 浙江大学 | Microbubble generator and microbubble generating method thereof |
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| CN104602800A (en) * | 2012-09-28 | 2015-05-06 | 日之出控股株式会社 | Gas dissolving device |
| CN105708679A (en) * | 2016-01-26 | 2016-06-29 | 胥常委 | Carbonate spring preparation device and method |
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| CN107827187A (en) * | 2017-11-06 | 2018-03-23 | 深圳市长天长空智能设备科技有限公司 | A kind of water sludge interface nanometer air floatation machine |
| CN108295683A (en) * | 2018-02-01 | 2018-07-20 | 苏州碳酸泉贸易有限公司 | A kind of novel carbonate spring manufacturing 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 |
| CN111115787A (en) * | 2020-01-17 | 2020-05-08 | 南京昭凌精密机械有限公司 | Fusion device for preparing high-concentration carbonic acid spring |
| CN111420605A (en) * | 2020-04-22 | 2020-07-17 | 重庆冷泉科技有限公司 | Carbonic acid spring preparation facilities |
| CN111659272A (en) * | 2020-06-19 | 2020-09-15 | 御府汤(宁波)温泉开发有限公司 | Carbonic acid bath system and carbonization generating device |
| CN111659272B (en) * | 2020-06-19 | 2024-02-23 | 御府汤(宁波)温泉开发有限公司 | Carbonic acid bath system and carbonization generating device |
| CN112007530A (en) * | 2020-07-08 | 2020-12-01 | 浙江大学 | Microbubble generator and microbubble generating method thereof |
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Application publication date: 20170929 |