CN215514248U - Gas-liquid mixing filling system - Google Patents
Gas-liquid mixing filling system Download PDFInfo
- Publication number
- CN215514248U CN215514248U CN202121877729.9U CN202121877729U CN215514248U CN 215514248 U CN215514248 U CN 215514248U CN 202121877729 U CN202121877729 U CN 202121877729U CN 215514248 U CN215514248 U CN 215514248U
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- mixing
- pipeline
- pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Abstract
The utility model aims to overcome the defect of insufficient dissolved gas quantity of a gas-liquid mixing and filling system in the prior art, and provides a gas-liquid mixing and filling system which comprises a gas mixing tank, a gas dissolving device, a gas inlet device and a gas-liquid circulating device, wherein the gas mixing tank is communicated with a liquid supply device, the gas inlet device at least comprises a gas inlet device I, the gas inlet device I comprises a gas inlet pipeline I, a gas pressure reducing valve A, a gas stop valve A and a gas one-way valve I, the gas-liquid mixing and filling system adopting the structure can control the dissolved gas quantity by controlling the temperature and the pressure of gas and liquid to control the dissolved gas quantity, the bubbling condition can be controlled, the consistent taste is obtained, the gas-liquid contact area is effectively increased, the gas dissolving capacity of liquid is greatly improved, the gas dissolving efficiency is improved while the gas dissolving capacity is improved, and bubble wines and beverages such as champagne with large gas content can be produced.
Description
Technical Field
The utility model relates to a gas-liquid mixing and filling system for gas-liquid mixing and filling, in particular to a device for filling foaming liquid such as soda water, champagne and the like,
background
In the wine and beverage industry, when making wine or beverage containing gas, gas such as carbon dioxide is often filled into liquid, so that the liquid can dissolve sufficient gas or gas under a certain pressure and temperature to produce gas wine or gas water. The patent No. 96232730.1, Chinese utility model named carbon dioxide mixing and filling machine, discloses a gas mixing and filling machine, which comprises a gas storage steel bottle for storing carbon dioxide, a pressure reducing valve arranged at the mouth of the gas storage steel bottle, an air inlet pipe for carbon dioxide, a high-pressure leather hose for connecting the gas storage steel bottle and the air inlet pipe, a mixing pipe for flowing liquid and mixing high-pressure carbon dioxide, a glass ball for making the liquid distribute and diffuse and facilitating the high-pressure carbon dioxide to be dissolved in the flowing liquid, a flange plate, a filling head, a bottle mouth sealing head, a bottle supporting seat and a protective door, wherein the wine liquid in the bottle flows into the mixing pipe, is distributed and diffused by the glass ball and contacts with the high-pressure carbon dioxide in the pipe to promote the high-pressure carbon dioxide to be dissolved in the flowing wine liquid and then flows into an empty bottle, after the empty bottle is filled with the wine liquid (namely, sparkling wine) mixed with carbon dioxide, the valve at the upper end of the filling head and the valve of the bottle mouth sealing head are closed, and sending the mixture into a cooling container for cooling to complete gas-liquid mixing and filling. Adopt the gas-liquid filling equipment of above-mentioned structure, adopt the glass ball to carry out the reposition of redundant personnel diffusion to liquid, make intraductal high-pressure gas fully contact with water, promote the air-water mixture, need the velocity of flow of wine liquid can produce the reposition of redundant personnel diffusion very fast with between the glass ball, and the ability of reposition of redundant personnel diffusion is limited, when filling wine or beverage that the gas content is big, makes the gaseous volume not enough, and the bubble of production is not abundant, and the gas volume and the liquid volume of filling in addition do not have the ration, make the gas content unstable, the taste is not unified.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a gas-liquid mixing and filling system aiming at the defect of insufficient dissolved gas amount of the gas-liquid mixing and filling system in the prior art.
The purpose of the utility model is realized by the following technical scheme:
a gas-liquid mixing and filling system comprises a gas mixing tank, a gas dissolving device, a gas inlet device and a gas-liquid circulating device, wherein the gas mixing tank is communicated with a liquid supply device, the gas inlet device at least comprises a first gas inlet device, a first gas pressure reducing valve A, a first gas stop valve A and a first gas one-way valve which are positioned on the first gas inlet pipeline, the first gas pressure reducing valve A is directly communicated with a gas outlet of the gas supply device, the gas dissolving device at least comprises a first gas dissolving device, the first gas dissolving device comprises a gas dissolving pipe and a microporous aerator, the microporous aerator is positioned in the gas dissolving pipe, the gas dissolving pipe is a closed container, a liquid inlet of the first gas dissolving device is positioned at the bottom of the gas dissolving pipe and is communicated with an inner cavity of the gas dissolving pipe and is communicated with the bottom of the gas mixing tank through the first liquid inlet circulating pipeline, and a gas inlet of the microporous aerator is positioned on the gas dissolving pipe or positioned outside the gas dissolving pipe on one side of the lower end of the gas dissolving pipe, the gas inlet of the microporous aerator is communicated with a gas supply device through a first gas inlet pipeline, the liquid outlet of the first gas dissolving device is positioned at the upper part of a gas dissolving pipe and is communicated with the upper part of the inner cavity of the gas mixing tank through a second gas-liquid circulation pipeline, the microporous aerator aerates the gas dissolving pipe, the first gas-liquid mixing pipeline is provided with a high-pressure liquid conveying device, the high-pressure liquid conveying device conveys high-pressure liquid to the gas dissolving pipe, the opening and closing of the first gas inlet pipeline are controlled by a gas stop valve A, and the opening and closing of the first gas-liquid circulation pipeline are controlled by a stop valve C;
the gas inlet device also comprises a second gas inlet device, the second gas inlet device comprises a backup pressure pipe, one end of the backup pressure pipe is communicated with the gas supply device through a gas pressure reducing valve B, the other end of the backup pressure pipe is communicated with the upper part of the inner cavity of the tank body of the gas mixing tank, backup pressure gas is filled into the gas mixing tank, and the backup pressure pipe is provided with the gas pressure reducing valve B, a gas stop valve B and a gas one-way valve II;
the first gas-liquid mixing pipeline is also provided with a branch pipeline I for connecting a liquid supply device, the branch pipeline I is provided with a stop valve D, one end of the branch pipeline I is communicated with the first gas-liquid mixing pipeline, the other end of the branch pipeline I is connected with the liquid supply device, the stop valve D is arranged on the liquid supply device and the first mixing pipeline, the on-off of the connected liquid is controlled through the stop valve D, and the branch pipeline I is positioned between the high-pressure conveying device and the stop valve C;
the high-pressure liquid conveying device is a high-pressure diaphragm pump or a high-pressure centrifugal pump;
the gas-liquid mixing pipeline I is also provided with a liquid flow meter, the stop valve C, the high-pressure gas conveying device and the gas flow meter are sequentially arranged from a mixed liquid outlet of the gas mixing tank to a liquid inlet of the gas dissolving device I, and the liquid outlet of the gas dissolving device I is positioned at the upper end of the gas dissolving pipe;
the gas-liquid mixing device comprises a gas-liquid mixing pipeline I, a gas-liquid mixing pipeline II and a gas-liquid mixing device II, wherein the gas-liquid mixing pipeline I is provided with a gas mixing tank;
the top of the tank body of the gas mixing tank is provided with a manual exhaust valve, a safety valve and an electric contact pressure gauge for monitoring the pressure condition in the tank body, and the electric contact pressure gauge feeds the monitored pressure back to the pressure control system;
a liquid level meter is arranged on the tank body to monitor the liquid level condition in the tank body;
a temperature sensor T for monitoring the temperature condition in the tank body is arranged on the tank body, and the monitored temperature is fed back to a temperature control system;
the refrigerating device comprises a circulating water tank and a refrigerating circulating pump, an interlayer is arranged on the tank body of the gas mixing tank, cooling liquid is arranged in the interlayer, the interlayer is communicated with the circulating water tank through a cooling pipeline, the refrigerating circulating pump is arranged on the cooling pipeline, and the refrigerating circulating pump circulates the cooling liquid in the interlayer and the liquid in the circulating water tank.
The utility model has the following beneficial effects:
the gas-liquid mixing and filling system adopting the structure can control the gas dissolving amount by controlling the temperature and the pressure of the gas and the liquid, so that the gas dissolving amount is controllable, the bubbling condition can be controlled, and the consistent taste is obtained.
Drawings
FIG. 1 is a schematic structural diagram of an embodiment of a gas-liquid mixing and filling system according to the present invention;
fig. 2 is a schematic structural diagram of an embodiment of an air dissolving device in the structure of the embodiment of the present invention.
Description of the reference numerals
101. A first air inlet device; 1011. A gas pressure reducing valve A; 1012. gas stop valve A; 1013. a first gas flow meter; 1014. a first gas check valve; 1015 an air inlet pipeline I;
102. a second air inlet device; 1021. a gas pressure reducing valve B; 1022. gas stop valve B; 1023. a backup pressure pipe; 1024. a second gas check valve;
103. a first air dissolving device; 1031. a microporous aerator; 1032. a gas dissolving pipe; 1033. An air inlet; 1034. a liquid inlet; 1035. a gas-liquid mixing outlet;
104. a second air dissolving device; 1041. a spiral spray head;
105. a gas-liquid circulation device; 1051. a liquid inlet circulation pipeline I; 1052. a stop valve C; 1053. a stop valve D; 1054. a high pressure diaphragm pump; 1055. A liquid flow meter; 1056. a liquid check valve; 1057. a gas-liquid circulation pipeline II;
106. a safety valve; 107. a manual exhaust valve; 108. an electric contact pressure gauge; 109. a gas mixing tank; 1091. a tank body; 1092. an electric contact pressure gauge; 1093. a manual exhaust valve; 1094 a safety valve; 1095 a temperature sensor T; 110. liquid level meter
200. An isobaric filling device; 2011. filling tubes; 2013. A stop valve A; 2014. a stop valve B;
300. a freezing device; 3011. a circulating water tank of the refrigerator; 3012. a refrigeration circulating pump;
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
The gas-liquid mixing and filling device comprises a gas mixing tank 109, a gas inlet device, a gas dissolving device, a gas-liquid circulating device 105, a filling device 200 and a refrigerating device 300, wherein a tank body 1091 of the gas mixing tank 109 is provided with a mixed liquid inlet, a standby gas inlet, a mixed liquid outlet and a gas-dissolved liquid filling port, the tank body of the gas mixing tank is preferably arranged into a double-layer interlayer, cooling liquid is arranged in the interlayer, the cooling liquid is communicated with a refrigerating machine circulating water tank 302 through a pipeline, and the cooling liquid is subjected to circulating refrigeration through a cooling liquid circulating pump 3012.
The air dissolving device at least comprises a first air dissolving device 103, the first air dissolving device 103 comprises a microporous aerator 1031 and an air dissolving pipe 1032, the microporous aerator is arranged in the air dissolving pipe, a through hole is formed in the air dissolving pipe and used for an air inlet pipe of the microporous aerator to penetrate, an air inlet 1033 of an air inlet pipe of the microporous aerator is positioned outside the air dissolving pipe, the through hole in the air dissolving pipe is in sealing connection with the air inlet pipe of the microporous aerator, a liquid inlet 1034 and a gas-liquid mixing outlet 1035 are both arranged on the air dissolving pipe and communicated with an inner cavity of the air dissolving pipe, the liquid inlet is positioned at the side lower end of the air dissolving pipe, the gas-liquid mixing port is positioned at the upper end of the air dissolving pipe and is preferably positioned at the top end of the air dissolving pipe, and the microporous aerator is communicated with the inner cavity of the air dissolving pipe through a micropore arranged on the microporous aerator.
The air inlet device comprises a first air inlet device 101 and a second air inlet device 102. The first air inlet device is used for conveying air into the first air dissolving device, and the second air inlet device is used for filling prepared pressure air into the air mixing tank 109. The first gas inlet device 101 comprises a first gas inlet pipeline 1015, one end of the first gas inlet pipeline is communicated with a gas supply device (not shown in the figure) through a gas pressure reducing valve A1011, the other end of the first gas inlet pipeline is communicated with a gas inlet 1033 of the microporous aerator, and the gas pressure reducing valve A1011, a gas stop valve A1012, a gas flow meter one 1013 and a gas one-way valve one 1014 are sequentially arranged between the gas supply device and the gas dissolving device one; and the second air inlet device comprises a backup pressure pipe 1023, one end of the backup pressure pipe is communicated with an air supply device (not shown in the figure) through a gas pressure reducing valve B1021, the other end of the backup pressure pipe is communicated with the inner cavity of the tank body of the mixed air tank, the backup pressure gas is filled into the mixed air tank, and the tank body from the air supply device to the mixed air tank on the backup pressure pipe is sequentially provided with a gas pressure reducing valve B1021, a gas stop valve B1022 and a gas check valve II 1024.
The gas-liquid circulation device 105 comprises a first gas-liquid circulation pipeline 1051 and a second gas-liquid circulation pipeline 1057, one end of the first gas-liquid circulation pipeline 1051 is connected with a liquid inlet 1034 of the first gas dissolving device, the other end of the first gas-liquid circulation pipeline 1051 is connected with a mixed liquid outlet of the gas mixing tank and is communicated with an inner cavity of the first gas dissolving device, and a stop valve C1052, a stop valve D1053, a high-pressure diaphragm pump 1054 serving as a high-pressure liquid conveying device and a liquid flowmeter 1055 are sequentially arranged on the first gas-liquid circulation pipeline 1051 from the mixed liquid outlet of the gas mixing tank to the first gas dissolving device 103; one end of the gas-liquid circulation pipeline II 1057 is connected with the gas-liquid mixing outlet 1035 of the gas dissolving device I, the other end is connected with the mixed liquid inlet of the gas mixing tank and is communicated with the inner cavity at the top of the tank body, and a liquid one-way valve 1056 is arranged on the gas-liquid circulation pipeline II 1057. Wherein, stop valve D1053 divides pipeline one to be the pipeline of connecting liquid through dividing pipeline one and gas-liquid mixture pipeline intercommunication, divides pipeline one, controls the liquid break-make through stop valve D1053, can connect and be used for abluent washing liquid entry, also can connect the liquid entry of filling.
In the utility model, the first gas check valve 1014 and the second gas check valve 1024 respectively permit gas to flow to the gas mixing tank, and the liquid check valve 1056 permits liquid to flow to the gas mixing tank. The gas flow meter 1013 and the liquid flow meter 1055 record the flow rates of the gas and the liquid, respectively, and perform flow rate adjustment according to the solubility of the mixed gas in the solution. Besides the high-pressure diaphragm pump, a sanitary high-pressure centrifugal pump can be used as a high-pressure liquid conveying device, liquid conveying and circulating are carried out by overcoming the internal pressure of the dissolved air pipe, and the pressure of the liquid passing through the dissolved air pipe is maintained at a set value through a gas pressure reducing valve A1011.
The top of the tank body of the gas mixing tank is provided with a manual exhaust valve 107, a safety valve 106 and an electric contact pressure gauge 108, the pressure condition in the tank body is monitored, and the monitored pressure is fed back to the pressure control system by the electric contact pressure gauge. The tank body is provided with a liquid level meter for monitoring the liquid level condition in the tank body, and the temperature sensor T1095 monitors the temperature condition in the tank body and feeds the monitored temperature back to the temperature control system.
The gas mixing and filling device is not only suitable for filling gas mixture of gas-containing wine liquid such as champagne and beer, but also suitable for gas mixture filling of gas beverage such as carbonated beverage and the like. Adopt isobaric filling device 200 during the filling, isobaric filling device 200 includes filling pipe 2011 and stop valve A2013 and stop valve B2014, and the filling liquid outlet is connected to the one end of canning pipe, is provided with stop valve A2013 on the other end, is provided with branch pipeline on the pipeline between filling pipe 2011 and stop valve A2013, is provided with stop valve B2014 on dividing the pipeline.
In the following, a 15L tank is filled with a mixture of carbon dioxide gas and wine, and an electric contact pressure gauge PS is 1MPa and a safety valve PS is 0.7 MPa. When in use, the gas and the liquid are mixed according to the following steps,
1. and filling and washing the inner cavity of the mixed gas tank body with purified water. And D, stopping valve connection of purified water, opening a manual exhaust valve 107 positioned at the top of the gas mixing tank body, starting a high-pressure diaphragm pump 1054 to inject purified water into the gas mixing tank 109, indicating that the gas mixing tank is filled with purified water when liquid flows out of the manual exhaust valve 107, closing the high-pressure diaphragm pump, and stopping filling of purified water.
2. Filling CO to be mixed into the tank body of the gas mixing tank2The gas will discharge the washing liquid. Opening the gas pressure reducing valve B1021, regulating the pressure to 0.01MPa, opening the gas stop valve B1022, and filling CO into the gas mixing tank2Gas, open stop valve B2014, with CO2The gas pushes the purified water out of the tank body, and the purified water and the water in the tank body are dischargedWhen the tank body is out of the water, the tank body is filled with CO2A gas. All valves were closed after the water was drained.
3. And filling the liquid to be filled into the gas mixing tank. The stop valve D is connected with CO to be added2And (3) opening the manual exhaust valve 107 for the gas liquid, starting the high-pressure diaphragm pump 1054 to add the liquid, stopping pumping the liquid into the gas mixing tank when the liquid reaches 5L, and closing the manual exhaust valve 107. And starting a refrigerating machine for refrigeration to cool the liquid in the gas mixing tank body to 4 ℃.
4. After the liquid temperature in the gas mixing tank reaches 4 ℃, the high-pressure diaphragm pump is opened to send liquid into the dissolved gas pipe, meanwhile, the stop valve C1052 is opened, the gas pressure reducing valve A1011 is opened, and CO is adjusted2When the pressure reaches 0.3Mpa, the gas stop valve A1012 is opened to inflate the microporous aerator, the gas enters the gas dissolving pipe through the aerator, the gas is dissolved in the gas dissolving pipe, the liquid dissolved in the gas through aeration is called gas dissolving liquid, the liquid enters the tank body 1091 through the gas-liquid circulation pipeline II 1057, the liquid and the gas which are pre-filled in the gas mixing tank are dissolved and mixed again, then the liquid enters the gas-liquid circulation pipeline I1051 from the bottom of the tank body, the liquid is sent into the gas dissolving pipe through the high-pressure diaphragm pump to be mixed again with the gas exposed by the microporous aerator, the liquid and the gas are mixed and then enter the gas mixing tank, the gas is inflated and mixed through the circulation, and when the pressure in the tank body is equal to the pressure at the outlet of the gas pressure reducing valve A, namely 0.3Mpa, the high-pressure diaphragm pump and the gas stop valve A1011 are closed, and the gas mixing is completed.
5. Sampling and detecting CO2And (4) if the solubility does not reach the target value, properly adjusting the gas pressure reducing valve A upwards to increase the pressure, repeating the step (4) until the concentration of the liquid dissolved gas reaches the required concentration, closing all opened valves when the concentration of the liquid dissolved gas reaches the required concentration, and opening the stop valve A2013 for filling.
Preferably, a second gas dissolving device is arranged, and comprises a spiral spray nozzle 1041, and the spiral spray nozzle is arranged at one end, located in the gas mixing tank body, of the second gas-liquid circulation pipeline 1057. The gas-dissolving liquid sprayed out by the spiral nozzle is atomized by the spiral nozzle, the gas-dissolving capacity is further increased, the gas in the gas mixing tank is dissolved, the gas is dissolved for the second time, and the gas dissolving concentration is increased. Spiral spray heads are commercially available, being spray heads for sprayers.
The utility model relates to a micro-pore aerator, which is characterized in that a first air dissolving device consisting of a micro-pore aerator and an air dissolving pipe is arranged on a gas-liquid circulating pipeline for first air dissolving, the micro-pore aerator is arranged in the air dissolving pipe, micron-sized water outlet holes are formed in the micro-pore aerator and are densely distributed on the micro-pore aerator, the air can be uniformly dispersed after being sprayed out by the micro-pore aerator to achieve the micro-particle state, the micro-particle state is taken away by high-pressure liquid flowing around the micro-pore aerator and is quickly mixed with the flowing high-pressure liquid to achieve the effect of quickly dissolving air, the air dissolving efficiency is increased, and the air dissolving efficiency is increased from the original 2.5 times to 3.5-4 times at the temperature of 15.5 ℃ under the same air pressure and flow rate.
The ceramic aeration head is preferably used as the microporous aerator, the microporous aerator can be tubular or spherical, and when the tubular microporous aerator is used, the microporous aerator and the dissolved air pipe are coaxially arranged and preferably occupy more than three quarters of the length of the dissolved air pipe.
The specific examples are merely illustrative of the utility model and are not intended to be limiting.
Claims (10)
1. A gas-liquid mixing and filling system comprises a gas mixing tank (109), a gas dissolving device, a gas inlet device and a gas-liquid circulating device (105), wherein the gas mixing tank is communicated with a liquid supply device, the gas inlet device at least comprises a first gas inlet device, the first gas inlet device comprises a first gas inlet pipeline, a gas pressure reducing valve A (1011), a gas stop valve A (1012) and a first gas check valve (1014), the first gas inlet device is positioned on the first gas inlet pipeline and is directly communicated with a gas outlet of the gas supply device through the gas pressure reducing valve A, the gas dissolving device at least comprises a first gas dissolving device (103), the first gas dissolving device comprises a gas dissolving pipe (1032) and a micropore aerator (1031), the micropore aerator is positioned in the gas dissolving pipe, the gas dissolving pipe is a closed container, a liquid inlet (1034) of the first gas dissolving device is positioned at the bottom of the gas dissolving pipe and is communicated with an inner cavity of the gas dissolving pipe and is communicated with the bottom of the gas mixing tank through the first liquid inlet circulating pipeline, the air inlet of micropore aerator is located gas dissolving pipe lower extreme one side and is located gas dissolving pipe or be located outside the gas dissolving pipe, the air inlet of micropore aerator passes through air inlet pipeline one and air feeder intercommunication, the liquid outlet of gas dissolving device one is located gas dissolving pipe's upper portion, and communicate through gas-liquid circulation pipeline two and gas mixing tank inner chamber upper portion, aerate to gas dissolving pipe by micropore aerator, gas-liquid mixture pipeline is last to be provided with high-pressure liquid conveyor, carry high-pressure liquid to gas dissolving pipe by high-pressure conveyor, the opening and closing of air inlet pipeline one is controlled by gas stop valve A (1012), the break-make of gas-liquid circulation pipeline one is controlled by stop valve C.
2. The gas-liquid mixing filling system according to claim 1, wherein: the air inlet unit still includes air inlet unit two, air inlet unit two is including being equipped with pressure pipe (1023), and the one end of being equipped with pressure pipe is passed through gas reducing valve B (1021) intercommunication air feeder, and the other end communicates with the upper portion of the jar body inner chamber of mixing the gas pitcher, and to filling in the gas pitcher that mixes and being equipped with pressure gas, is provided with gas reducing valve B (1021), gas stop valve B (1022), gaseous check valve two (1024) on being equipped with pressure pipe.
3. The gas-liquid mixing filling system according to claim 1, wherein: the first gas-liquid mixing pipeline is also provided with a first branch pipeline used for being connected with a liquid supply device, the first branch pipeline is provided with a stop valve D (1053), one end of the first branch pipeline is communicated with the first gas-liquid mixing pipeline, the other end of the first branch pipeline is connected with the liquid supply device, the first liquid supply device and the first mixing pipeline are provided with the stop valve D, the on-off of the liquid connected is controlled through the stop valve D (1053), and the first branch pipeline is positioned between the high-pressure conveying device and the stop valve C (1052).
4. A gas-liquid mixing and filling system according to any one of claims 1-3, wherein: the high-pressure liquid conveying device is a high-pressure diaphragm pump or a high-pressure centrifugal pump.
5. The gas-liquid mixing filling system according to claim 1, wherein: the gas-liquid mixing pipeline I on still be provided with fluidflowmeter (1055), stop valve C, high-pressure gas conveyor, gas flowmeter set gradually from mixed liquid outlet of gas mixing jar to the inlet of dissolving gas device I, the liquid outlet of dissolving gas device I is located the upper end of dissolving the trachea.
6. The gas-liquid mixing filling system according to claim 1, wherein: the gas mixing device comprises a gas mixing pipeline I and a gas mixing pipeline II, and is characterized by further comprising a gas dissolving device II, wherein the gas dissolving device II comprises a spiral spray head (1041), the spiral spray head (1041) is arranged at one end, located in the gas mixing tank, of the gas-liquid mixing pipeline I, and a liquid one-way valve (1056) is arranged on the gas-liquid mixing pipeline I.
7. The gas-liquid mixing filling system according to claim 1, wherein: the top of the tank body of the gas mixing tank is provided with a manual exhaust valve (107), a safety valve (106) and an electric contact pressure gauge (108) for monitoring the pressure condition in the tank body, and the monitored pressure is fed back to the pressure control system by the electric contact pressure gauge.
8. The gas-liquid mixing filling system according to claim 1, wherein: the tank body is provided with a liquid level meter for monitoring the liquid level condition in the tank body.
9. The gas-liquid mixing filling system according to claim 1, wherein: a temperature sensor T (1095) for monitoring the temperature condition in the tank body is arranged on the tank body, and the monitored temperature is fed back to the temperature control system.
10. The gas-liquid mixing filling system according to claim 1, wherein: the refrigerating device is further provided with a refrigerating device, the refrigerating device comprises a circulating water tank (3011) and a refrigerating circulating pump (3012), an interlayer is arranged on the tank body of the gas mixing tank, cooling liquid is arranged in the interlayer, the interlayer is communicated with the circulating water tank through a cooling pipeline, the refrigerating circulating pump (3012) is arranged on the cooling pipeline, and the refrigerating circulating pump circulates the cooling liquid in the interlayer and the liquid in the circulating water tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121877729.9U CN215514248U (en) | 2021-08-12 | 2021-08-12 | Gas-liquid mixing filling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121877729.9U CN215514248U (en) | 2021-08-12 | 2021-08-12 | Gas-liquid mixing filling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215514248U true CN215514248U (en) | 2022-01-14 |
Family
ID=79790676
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121877729.9U Active CN215514248U (en) | 2021-08-12 | 2021-08-12 | Gas-liquid mixing filling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215514248U (en) |
-
2021
- 2021-08-12 CN CN202121877729.9U patent/CN215514248U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4022119A (en) | Liquid carbon dioxide carbonation apparatus | |
| CN207822314U (en) | A kind of big flow foam-generating device and foam fire-fighting equipment | |
| CA1265990A (en) | Domestic carbonator | |
| US5124088A (en) | Process and apparatus for rapidly carbonating water | |
| US3960066A (en) | Beverage preparation apparatus | |
| EP0732142A2 (en) | Control of dissolved gases in liquids | |
| EP1491491A1 (en) | Carbonator with hollow-fibre membrane module for the preparation of beverages | |
| US9980505B2 (en) | Variable pressure device for solubilizing carbon dioxide in a beverage | |
| US10477883B2 (en) | Gas injection assemblies for batch beverages having spargers | |
| KR20190089041A (en) | Manufacturing and distributing carbonated beer from beer concentrate | |
| CN101146736A (en) | Refrigerator with dispenser for carbonated water | |
| CN101175418A (en) | Method and apparatus for producing oxygen-containing reducing aqueous beverage | |
| US9248416B2 (en) | Apparatus for the pressurization and evacuation of a container | |
| US20210283558A1 (en) | Apparatuses for Mixing Gases into Liquids | |
| KR20190089042A (en) | Manufacturing and distributing carbonated beer from beer concentrate | |
| CN215514248U (en) | Gas-liquid mixing filling system | |
| US3074700A (en) | Carbonating apparatus | |
| CN112055540A (en) | Gas Liquid Absorption Device (GLAD) with replaceable gas orifice fitting and sensor | |
| US11819809B2 (en) | Gas-injected beverage apparatuses, systems, and methods | |
| KR20190086757A (en) | Manufacturing and distributing carbonated beer from beer concentrate | |
| WO2006092704A1 (en) | Refrigerated core comprising carbonating system for drinks dispenser | |
| CN214862586U (en) | Stainless steel carbonization tank | |
| CN209735373U (en) | Multifunctional gas dissolving container | |
| KR20190089043A (en) | Manufacturing and distributing carbonated beer from beer concentrate | |
| SU1271359A3 (en) | Arrangement for preparing and distributing carbonized water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |