CN111659272A - Carbonic acid bath system and carbonization generating device - Google Patents
Carbonic acid bath system and carbonization generating device Download PDFInfo
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- CN111659272A CN111659272A CN202010568884.6A CN202010568884A CN111659272A CN 111659272 A CN111659272 A CN 111659272A CN 202010568884 A CN202010568884 A CN 202010568884A CN 111659272 A CN111659272 A CN 111659272A
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- 238000003763 carbonization Methods 0.000 title claims abstract description 47
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 title description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 177
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 79
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 39
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 39
- 239000007789 gas Substances 0.000 claims abstract description 23
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 239000001301 oxygen Substances 0.000 claims abstract description 11
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000005273 aeration Methods 0.000 claims abstract description 5
- 238000004140 cleaning Methods 0.000 claims abstract description 3
- 238000010438 heat treatment Methods 0.000 claims description 9
- 230000001502 supplementing effect Effects 0.000 claims description 8
- 239000010865 sewage Substances 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 238000011049 filling Methods 0.000 claims description 3
- 238000005452 bending Methods 0.000 claims 1
- 230000036541 health Effects 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 238000003287 bathing Methods 0.000 description 7
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 5
- 239000011148 porous material Substances 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 210000004204 blood vessel Anatomy 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000006210 lotion Substances 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000554 physical therapy Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 238000002560 therapeutic procedure Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F21/00—Dissolving
- B01F21/20—Dissolving using flow mixing
-
- 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
Landscapes
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Public Health (AREA)
- Physical Education & Sports Medicine (AREA)
- Pain & Pain Management (AREA)
- Epidemiology (AREA)
- Rehabilitation Therapy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Veterinary Medicine (AREA)
- Devices For Medical Bathing And Washing (AREA)
Abstract
The invention discloses a carbonic acid bath system and a carbonization generating device: a carbonic acid bath system, the water coming from the boiler is heated up-the water tank, one way enters the shower-discharge; one path enters a carbonization generating device to be carbonized by adding carbon dioxide gas, enters an overflow bath (basin), enters an aeration fine filter, and enters a cleaning part into a boiler; the unique carbonization generating device provided by the invention has high solubility of carbon dioxide in bath liquid; the carbonic acid bath system has the functions of oxygen supply, sound control regulation and rescue, and the function of converting the heat bath to the ice bath with gradually changed temperature, so that the health care effect is better.
Description
Technical Field
The invention relates to the technical field of health preservation and health care, in particular to a carbonation bath system and a carbonation generation device.
Background
At present, the quality of life is higher and higher, the requirements of people on health care are also continuously upgraded, and various types of therapies such as sauna, SPA, sauna and the like are presented in the market, such as patent granted invention: CN104174311B discloses a nanometer microbubble generator for bathing and a bathing system, the nanometer microbubble generator for bathing comprises a gas generator, a water supply device and a mixer, the mixer at least comprises a static mixing element and a mixing pipeline, at least one mixing cavity is formed inside the static mixing element, and a particle filler and/or a porous structure is filled in the mixing cavity. The bubble bath system comprises a bubble bath device and the nanometer microbubble generating device for the bubble bath, and provides a static and dynamic nanometer microbubble generating device, wherein the dynamic generating device is only a stirring structure, and the solubility of gas is not high enough.
Disclosure of Invention
The invention solves the problem of low gas-liquid mixing solubility in the prior art, and provides a more scientific carbonization generating device, a carbonic acid bath system and a carbonization process thereof.
In order to solve the technical problems, the invention adopts the following technical scheme: a carbonic acid bath system, the water coming from the boiler is heated up-the water tank, one way enters the shower-discharge; one path enters a carbonization generating device to be carbonized by adding carbon dioxide gas, enters an overflow bath pool (basin), enters an aeration fine filter, and enters a cleaning part into a boiler.
The biggest bright point of this system lies in that bathtub (basin) is the carbonization water of continuous supply, and the overflow is through filtering, heating, carbonization recycling, and circulation rate can be adjusted, has guaranteed the suitable carbonization degree of bathtub (basin) carbonization water, strengthens the physiotherapy effect.
Preferably, the water tanks are two, a high-temperature water tank and a low-temperature water tank. The two water tanks are used for conveniently adjusting the water supply temperature, and the fine filtering water directly returns to the low-temperature water tank. The system has the greatest advantage that the water temperature of the bath can be gradually changed, the bath mostly enters and leaves from the middle temperature, the middle gradually-changed low-temperature ice bath is charm in summer, the favorite high temperature is gradually changed, and the middle temperature leaves the bath.
Preferably, the bathing pool (basin) is provided with a voice control device. Guests can wake up a small bath, request favorite music and songs, control light, select and control circulating water quantity and water temperature, and more importantly call for rescue.
Preferably, an oxygen supplementing device is arranged in the room of the bathing pool (basin). Because the bath lotion continuously releases carbon dioxide, the bather has lower body position, the skin absorbs carbon dioxide, the oxygen supply of the lung is reduced, and the symptom of oxygen deficiency is easily generated. Since oxygen has a lower specific gravity than carbon dioxide gas, oxygen is supplied not only to the room but also to a low location.
Preferably, the carbonization generating device is a cylinder, a bell mouth is arranged below the inside of the cylinder, a water outlet of an axial flow pump is tangentially arranged at the middle part of the cylinder above the bell mouth, a water inlet of the axial flow pump is arranged at the upper part of the cylinder, a water replenishing pipe is inserted into the bent part of the water inlet pipe, the diameter of the water replenishing pipe is smaller than that of the water inlet, the water replenishing pipe is connected with a water tank, an air inlet pipe is arranged in front of the water replenishing pipe and connected with an air bottle, the air inlet pipe is of an arc structure, an air hole is formed in the; a water outlet pipe is arranged above the bell mouth; the top end of the cylinder body is provided with an exhaust valve to ensure the height of the liquid level in the cylinder body, and the lowest end of the cylinder body is provided with a sewage draining outlet.
The carbonization generating device is always in a high liquid level, the upper part of the cylinder body is a liquid rotating device, carbon dioxide gas is added into turbulent water, a small part of the turbulent water is subjected to chemical reaction to generate carbonate, most of the carbonate is dissolved in water through physical reaction, the specific gravity of the carbonate is more than that of carbon dioxide water, and the specific gravity of the carbonate is more than that of the carbon dioxide water, the most needed washing is water with the carbon dioxide dissolving amount exceeding 1200ppm, so the carbonate and precipitate with the maximum specific gravity sink to the outside of a bell mouth and do not participate in rotation, and a drain outlet is opened for discharging periodically; the water inlet of the axial-flow pump is arranged on the upper part of the cylinder, the water with the minimum specific gravity and the fresh water entering from the water replenishing pipe enter the pump body, the air inlet pipe is arranged between the water replenishing pipe and the axial-flow propeller and is a mixing area of water with different water pressures and specific gravities, the water flow speed is high and is in a turbulent flow state, and the air is mixed with the carbon dioxide and starts to rotate at an accelerated speed through the propeller, so that the optimal state of the carbon dioxide and the water mixing is realized. The formula weight of the carbon dioxide is larger than that of water, so that the higher the carbon dioxide solubility of the water is, the higher the specific gravity of the water is, and the water is distributed in the carbonization generating device in a gradient manner with lower height and higher height according to the specific gravity, so that the water inlet, the water replenishing pipe, the water outlet and the sewage discharge outlet of the carbonization generating device are distributed. The carbonization generating device has a spiral dust removal function and is the last line of defense before use. When the carbonization generating device starts to be started, the circulation in the water replenishing pipe is mostly closed, so that the carbon dioxide content of the carbonization generating device is rapidly increased; when the external water demand is not large, the water inlet and the water replenishing pipe are opened simultaneously; when the external water consumption is large, the water inlet can be opened very little or even closed completely.
Preferably, the carbonization generating device is a rectangular shell, a water outlet of an axial flow pump is arranged at the lower part of the narrow side surface of the rectangular shell, an arc surface or an inclined surface is arranged at the opposite corner of the shell, a water inlet of the axial flow pump is arranged at the upper part of the narrow side surface, a water replenishing pipe is inserted into the bent part of the water inlet pipe, the diameter of the water replenishing pipe is smaller than that of the water inlet, the water replenishing pipe is connected with a water tank, an air inlet pipe is arranged in front of the water replenishing pipe and connected with an air bottle, the air inlet pipe is of an arc structure, an air hole is; a water outlet pipe is arranged beside the water inlet; an exhaust valve is arranged at the top end of the rectangular shell, and the height of the liquid level in the rectangular shell is guaranteed.
The carbonization generating device is a rectangular shell, the narrow side of the shell is provided with a water outlet of an axial flow pump, and the corner in the shell opposite to the water outlet is provided with an arc surface or an inclined surface, so that the water outlet is a water-gas mixture, the water flow is in a turbulent flow state at a high speed, and the water is sprayed out at a high speed through pump blades and turns upwards to be in anticlockwise circulation when encountering the arc surface or the inclined surface, thereby being more beneficial to dissolving carbon dioxide in water and improving the carbonization degree.
Preferably, the carbonization generating device is communicated with a bath (basin). Thus, the temperature and the carbonization degree of the water in the bathing pool (basin) can be adjusted conveniently, and the requirements of health care are met.
Preferably, the air inlet pipe is provided with a heating device. The temperature of the carbon dioxide for carbonization is ensured to be close to the temperature of the inlet water of the carbonization generating device, thereby facilitating large-flow gas supply.
One process parameter for applying the above one carbonation bath system: the temperature range of the high-temperature water tank is 40-45 ℃, and the temperature range of the low-temperature water tank is 25-38 ℃; the pressure of the carbon dioxide gas cylinder is reduced to 0.18-0.25 MPa, the temperature is heated to 28-42 ℃, and the water flow rate of the gas filling section is in a turbulent flow state; the water pressure in the carbonization generating device is 0.16-0.24 MPa, the temperature of the water entering the bath (basin) is 25-42 ℃, the carbon dioxide content of the water entering the bath is more than 1200ppm, and the pH value is 4.5-5.2.
The carbon dioxide bath is a high-temperature and low-temperature carbon acid bath, the temperature of the skin of a human body is generally lower than 37 ℃, so that gas containing water at 39-42 ℃ can release carbon dioxide gas more easily when meeting low temperature, and because the kinetic diameter of carbon dioxide molecules is 0.33nm and the diameter of skin capillary pores is 50000nm, carbon dioxide can enter the body easily, the concentration of carbon dioxide in blood is increased, and then the human body can automatically perform blood vessel expansion and accelerate breathing to absorb more oxygen; meanwhile, carbon dioxide bubbles on the surface of the skin gradually gather and grow up, break and rise, and then gather new bubbles to take away impurities in the capillary pores, so that the capillary pores are cleaned. Because of the unique carbonization generating device, the carbonized water has high carbon dioxide, moderate acidity, pH value of 4.5-5.2 and carbon dioxide content of more than 1200 ppm. The bath water temperature of the bath pool can be gradually changed, the bath is mostly carried in and out from the bath at the medium temperature of 38-40 ℃, the middle gradually-changed low-temperature ice bath is 25-36, the charm of the south in summer is the charm, the favorite high temperature is gradually changed by 40-45, and the middle temperature bath is finished.
Due to the adoption of the technical scheme, the unique carbonization generating device provided by the invention has high solubility of carbon dioxide in bath liquid; the carbonic acid bath system has the functions of oxygen supply, sound control regulation and rescue, and the function of converting the heat bath to the ice bath with gradually changed temperature, so that the health care effect is better.
Drawings
FIG. 1 is a schematic diagram of a carbonation bath system in accordance with the present invention;
FIG. 2 is a front view of a carbonization generator according to the present invention;
FIG. 3 is a top view of a carbonization generator according to the present invention;
FIG. 4 is a schematic view of another carbonic acid bath system of the present invention;
FIG. 5 is a cross-sectional view of another alternative carbonization device in accordance with the invention;
FIG. 6 is a side view of another alternative carbonization generator of the present invention;
in the figure: 11-boiler, 21-low temperature water tank, 22-high temperature water tank, 30-floor drain, 31-shower nozzle, 32-bath (basin), 33-oxygen supplement device, 41-fine filter, 51-cylinder, 52-rectangular shell, 61-carbon dioxide gas cylinder, 62-heating device, 510-exhaust valve, 511-bell mouth, 512-axial pump, 5121-water outlet, 5122-water inlet, 513-water supplement pipe, 514-air inlet pipe, 5141-air outlet, 5142-sealing plate, 515-water outlet pipe, 516-sewage outlet, 521-cambered surface (inclined surface).
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
The first embodiment is as follows: with reference to fig. 1-3, a carbonation bath system comprises an air energy boiler (11) respectively connected with a low temperature water tank (21) and a high temperature water tank (22), wherein one path of the high temperature water tank (22) enters a shower nozzle (31) and is discharged through a floor drain (30); one path of low-temperature water tank (21) and one path of high-temperature water tank (22) are connected in parallel and enter the cylinder (51) carbonization generating device, and the gas in the carbon dioxide gas cylinder (61) also enters the cylinder (51) carbonization generating device through the heating device (62); the generated carbonized water enters a bath pool (32), enters the bath pool (32) with an oxygen supplementing device (33), the water in the bath pool (32) overflows into an aeration fine filter (41), the water is filtered and discharged, and the clean water enters an air energy boiler (11).
The carbonization generating device comprises a cylinder body (51), wherein a bell mouth (511) is arranged below the inside of the cylinder body (51), a water outlet (5121) of an axial flow pump (512) is tangentially arranged at the middle part of the cylinder body (51) above the bell mouth (511), a water inlet (5122) of the axial flow pump (512) is arranged at the upper part of the cylinder body (51), a water supplementing pipe (513) is inserted into the bent part of the water inlet pipe, the diameter of the water supplementing pipe (513) is smaller than that of the water inlet, the water supplementing pipe (513) is provided with a low-temperature water tank (21) and a high-temperature water tank (22), an air inlet pipe (514) is arranged in front of the water supplementing pipe (513), the air inlet pipe (514) is connected with an air bottle (61) through a heating device (62), the air inlet pipe (514) is of an; a water outlet pipe (515) is arranged above the bell mouth (511); the top end of the cylinder body (51) is provided with an exhaust valve (510) for ensuring the height of the liquid level in the cylinder body (51), and the lowest end of the cylinder body (51) is provided with a sewage discharge port (516).
The bath water temperature of the bath pool (32) can be gradually changed, the bath is mostly carried in and out at the medium temperature of 38-40 ℃, the middle gradually-changed low-temperature ice bath is 25-36, the charm of the south in summer is in, the favorite high temperature is gradually changed again to 40-45, and then the middle gradually-changed bath is finished. Because the water flow velocity at the gas-water fusion part is in a turbulent flow state, the carbonization degree is high, and the carbon dioxide concentration reaches over 1200 ppm. Is suitable for high carbonic acid health bath.
Example two: with reference to fig. 4-6, a carbonation bath system comprises an air energy boiler (11) respectively connected with a low temperature water tank (21) and a high temperature water tank (22), wherein one path of the high temperature water tank (22) enters a shower nozzle (31) and is discharged through a floor drain (30); one path of low-temperature water tank (21) and one path of high-temperature water tank (22) are connected in parallel and respectively enter four groups of rectangular shell (52) carbonization generating devices, and one path of gas of a carbon dioxide gas cylinder (61) also enters each rectangular shell (52) carbonization generating device through a heating device (62); the carbonized water generated by each carbonization generating device enters a respective bath pool (32), enters the bath pool (32) with an oxygen supplementing device (33), the water in the bath pool (32) overflows into an aeration fine filter (41), the filtered sewage is discharged, and the clean water enters an air energy boiler (11).
The carbonization generating device comprises a rectangular shell (52), wherein a water outlet (5121) of an axial flow pump (512) is formed in the lower portion of the narrow side face of the rectangular shell (52), an arc face (521) is formed in the corner, opposite to the water outlet (5121), of the rectangular shell (52), a water inlet (5122) of the axial flow pump (512) is formed in the upper portion of the narrow side face, a water replenishing pipe (513) is inserted into the bent portion of the water inlet pipe, the diameter of the water replenishing pipe (513) is smaller than that of the water inlet, the water replenishing pipe (513) is connected with a low-temperature water tank (21) and a high-temperature water tank (22), an air inlet pipe (514) is arranged in front of the water replenishing pipe (513), the air inlet pipe (514) is connected with an air bottle (61) through a heating device (62), the air inlet pipe (514) is of; a water outlet pipe (515) is arranged beside the water inlet (5122); the top end of the rectangular shell (52) is provided with an exhaust valve (510) to ensure the height of the liquid level in the rectangular shell (52).
The carbonization generating device is a rectangular shell, the narrow side of the shell is provided with a water outlet of an axial flow pump, and the corner in the shell opposite to the water outlet is provided with an arc surface or an inclined surface, so that the water outlet is sprayed out of a water-gas mixture at a high speed, and the arc surface turns upwards to form anticlockwise circulation, which is more beneficial to dissolving carbon dioxide in water and improving the carbonization degree. Because the water flow velocity at the gas-water fusion part is in a turbulent flow state, the carbonization degree is high, and the carbon dioxide concentration reaches over 1200 ppm. Is suitable for high carbonic acid health bath.
According to the carbonation bath system, each bath pool is independently supplied with carbonated water through one carbonation generation device, so that the temperature and the carbonation degree of bathing are more convenient to control, and the carbonation bath system is energy-saving and environment-friendly.
The above two embodiments are provided to explain the present invention in detail. The principles and embodiments of the present invention are explained herein using specific examples, which are presented only to assist in understanding the core concepts of the present invention. It should be noted that, for those skilled in the art, it is possible to make several modifications to the present invention without departing from the core idea of the present invention, such as the modification of the carbonated water clockwise and counterclockwise rotation and the change of the rotation position, and the like, and it should fall within the protection scope of the claims of the present invention.
Claims (10)
1. A carbonation bath system, comprising: the incoming water is heated by a boiler to raise the temperature, namely a water tank, and one path of the incoming water enters a shower and is discharged; one path enters a carbonization generating device to be carbonized by adding carbon dioxide gas, enters an overflow bath pool (basin), enters an aeration fine filter, and enters a cleaning part into a boiler.
2. A carbonation bath system according to claim 1 and wherein said tanks are two, a high temperature tank and a low temperature tank.
3. A carbonation bath system according to claim 2 and characterised in that said bath (basin) is preferably provided with voice control means.
4. A carbonation bath system according to claim 3, characterized in that oxygen supplementing means are provided in said bath (basin) chamber.
5. The carbonation bath system according to the claim 1, 2, 3 or 4, wherein the carbonation generation device is a cylinder, a bell mouth is arranged at the lower part inside the cylinder, a water outlet of an axial flow pump is tangentially arranged at the middle part of the cylinder above the bell mouth, a water inlet of the axial flow pump is arranged at the upper part of the cylinder, a water replenishing pipe is inserted into the bending part of the water inlet pipe, the diameter of the water replenishing pipe is smaller than that of the water inlet, the water replenishing pipe is connected with a water tank, an air inlet pipe is arranged in front of the water replenishing pipe and connected with an air bottle, the air inlet pipe is of an arc structure, the inner arc surface is provided with an air hole; a water outlet pipe is arranged above the bell mouth; the top end of the cylinder body is provided with an exhaust valve to ensure the height of the liquid level in the cylinder body, and the lowest end of the cylinder body is provided with a sewage draining outlet.
6. A carbonation bath system according to claim 5 and wherein said inlet conduit is provided with heating means.
7. A process parameter for applying a carbonation bath system according to claim 6: it is characterized in that the temperature range of the high-temperature water tank is 40-45 ℃, and the temperature range of the low-temperature water tank is 25-38 ℃; the pressure of the carbon dioxide gas cylinder is reduced to 0.18-0.25 MPa, the temperature is heated to 28-42 ℃, and the water flow rate of the gas filling section is in a turbulent flow state; the water pressure in the carbonization generating device is 0.16-0.24 MPa, the temperature of the water entering the bath (basin) is 25-42 ℃, the carbon dioxide content of the water entering the bath is more than 1200ppm, and the pH value is 4.5-5.2.
8. The carbonation bath system according to the claim 1, 2, 3 or 4, wherein the carbonation generation device is a rectangular shell, the lower part of the narrow side of the rectangular shell is provided with a water outlet of an axial flow pump, the shell is provided with an arc surface or an inclined surface at the opposite corner of the water outlet, the water inlet of the axial flow pump is arranged at the upper part of the narrow side, a water replenishing pipe is inserted into the bent part of the water inlet pipe, the diameter of the water replenishing pipe is smaller than that of the water inlet, the water replenishing pipe is connected with a water tank, an air inlet pipe is arranged in front of the water replenishing pipe and connected with an air bottle, the air inlet pipe is of an arc structure, the inner arc surface is provided; a water outlet pipe is arranged beside the water inlet; an exhaust valve is arranged at the top end of the rectangular shell, and the height of the liquid level in the rectangular shell is guaranteed.
9. A carbonation bath system according to claim 8, wherein said inlet conduit is provided with heating means.
10. A process parameter for applying a carbonation bath system according to claim 9: it is characterized in that the temperature range of the high-temperature water tank is 40-45 ℃, and the temperature range of the low-temperature water tank is 25-38 ℃; the pressure of the carbon dioxide gas cylinder is reduced to 0.18-0.25 MPa, the temperature is heated to 28-42 ℃, and the water flow rate of the gas filling section is in a turbulent flow state; the water pressure in the carbonization generating device is 0.16-0.24 MPa, the temperature of the water entering the bath (basin) is 25-42 ℃, the carbon dioxide content of the water entering the bath is more than 1200ppm, and the pH value is 4.5-5.2.
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| CN202010568884.6A CN111659272B (en) | 2020-06-19 | 2020-06-19 | Carbonic acid bath system and carbonization generating device |
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| CN202010568884.6A CN111659272B (en) | 2020-06-19 | 2020-06-19 | Carbonic acid bath system and carbonization generating device |
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| CN111659272B CN111659272B (en) | 2024-02-23 |
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