CN220589801U - Carbon dioxide mixing system - Google Patents
Carbon dioxide mixing system Download PDFInfo
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- CN220589801U CN220589801U CN202321984489.1U CN202321984489U CN220589801U CN 220589801 U CN220589801 U CN 220589801U CN 202321984489 U CN202321984489 U CN 202321984489U CN 220589801 U CN220589801 U CN 220589801U
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- Prior art keywords
- mixing
- carbon dioxide
- conveying
- pipeline
- communicated
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 31
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 31
- 230000003068 static effect Effects 0.000 claims abstract description 39
- 239000000463 material Substances 0.000 claims abstract description 17
- 238000013329 compounding Methods 0.000 claims 1
- 235000014171 carbonated beverage Nutrition 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 235000013361 beverage Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
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- Accessories For Mixers (AREA)
Abstract
The utility model discloses a carbon dioxide mixing system which comprises a material tank, a filling storage tank and a mixing component, wherein the material tank is communicated with the filling storage tank through a conveying pipeline, the conveying pipeline is also communicated with a conveying pump component, the mixing component comprises a Venturi mixing pipe and a static mixer, and the conveying pump component comprises a conveying pump I and a conveying pump II. The beneficial effects of the utility model are as follows: the method comprises the steps of adopting a double-delivery pump and an upgrading venturi tube to be matched with a professional sanitary static spiral mixer, introducing carbon dioxide into the venturi tube for primary mixing, sequentially mixing carbonated beverages for the second time, the third time and the fourth time through three static mixers, finally delivering the mixed carbonated beverages to a filling storage tank through a static holding mixing tube and filling qualified products, effectively improving the gas content of the carbon dioxide by 5 times, and maintaining the mixing and filling temperature above 16 ℃; effectively saves energy and improves the production efficiency of the equipment.
Description
Technical Field
The utility model relates to a mixing system, in particular to a carbon dioxide mixing system, and belongs to the technical field of mixing and filling.
Background
The carbonated beverage is popular as a beverage for a vast number of consumers, and is generally combined with ice when in use, and is prepared by filling carbon dioxide into liquid beverage, and the carbonated beverage contains a considerable amount of carbonic acid obtained by reacting carbon dioxide with water, so the carbonated beverage is called as carbonated beverage, and in hot seasons, the heat in the human body can be taken away through evaporation of heat, so the cooling effect is achieved, and therefore, in hot summer, the chilled carbonated beverage is often favored by people.
The method for producing carbonic acid in carbonated beverage is generally to fill carbon dioxide into liquid beverage to react with water to form carbonic acid, and most of carbon dioxide in the carbonic acid filling equipment is mixed by using a common venturi tube at present, so that the mixing effect is poor, the temperature of the mixed and filled product is required to be about 4-8 ℃, the energy consumption is high, and the control is not easy.
Disclosure of Invention
The present utility model aims to solve at least one of the above problems and provide a carbon dioxide mixing system.
The utility model realizes the above purpose through the following technical scheme: the carbon dioxide mixing system comprises a material tank, a filling storage tank and a mixing component, wherein the material tank is communicated with the filling storage tank through a conveying pipeline, and a conveying pump component is further communicated with the conveying pipeline;
the mixing component is communicated with the conveying pipeline and comprises a venturi mixing pipe and a static mixer, the feeding end of the venturi mixing pipe is also communicated with a carbon dioxide storage tank, the static mixer is provided with three groups, and the static mixers are connected into the conveying pipeline in series;
the conveying pump assembly comprises a conveying pump I and a conveying pump II, the conveying pump I is arranged on a conveying pipeline close to the discharge end of the material tank, and the conveying pump II is arranged on a pipe body at the middle part of the conveying pipeline.
As still further aspects of the utility model: the discharge end of the material tank is communicated with a product temperature regulator through a conveying pipeline.
As still further aspects of the utility model: one static mixer is connected to the conveying pipeline between the Venturi mixing pipe and the conveying pump II, and the other two static mixers are connected to the conveying pipeline communicated with the output end of the conveying pump II.
As still further aspects of the utility model: with the direction of delivery, the static holding mixing tube is communicated with the delivery pipeline between the filling storage tank and the terminal static mixer.
As still further aspects of the utility model: the product temperature regulator is communicated with a conveying pipeline between the Venturi mixing pipe, the other end of the diverting pipeline is communicated with the conveying pipeline connected with the output end of the static holding mixing pipe, and a second barometer and a second electromagnetic valve are arranged on the pipe body of the diverting pipeline.
As still further aspects of the utility model: a manual valve and one barometer I are arranged on the conveying pipeline between the output end of the diversion pipeline and the static holding mixing pipe.
As still further aspects of the utility model: and a first electromagnetic valve and a first other barometer are arranged on the conveying pipeline between the output end of the diversion pipeline and the filling storage tank.
As still further aspects of the utility model: the output end of the filling storage tank is connected with an output pipeline, and a flowmeter and a pressure sensor are installed on the output pipeline.
The beneficial effects of the utility model are as follows: the method comprises the steps of adopting a double-delivery pump and an upgrading venturi tube to be matched with a professional sanitary static spiral mixer, introducing carbon dioxide into the venturi tube for primary mixing, sequentially mixing carbonated beverages for the second time, the third time and the fourth time through three static mixers, finally delivering the mixed carbonated beverages to a filling storage tank through a static holding mixing tube and filling qualified products, effectively improving the gas content of the carbon dioxide by 5 times, and maintaining the mixing and filling temperature above 16 ℃; effectively saves energy and improves the production efficiency of the equipment.
Drawings
FIG. 1 is a schematic flow chart of the system of the present utility model.
In the figure: 1. the material jar, 2, the delivery pipeline, 3, the filling storage tank, 4, delivery pump one, 5, the product temperature regulator, 6, the carbon dioxide storage tank, 7, venturi mixing tube, 8, static mixer, 9, delivery pump two, 10, static holding mixing tube, 11, manual valve, 12, barometer one, 13, solenoid valve one, 14, shunt tubes, 15, barometer two, 16, solenoid valve two, 17, manometer, 18, output pipeline, 19, flowmeter, 20, pressure sensor.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Example 1
As shown in fig. 1, the carbon dioxide mixing system comprises a material tank 1, a filling material storage tank 3 and a mixing component, wherein the material tank 1 is communicated with the filling material storage tank 3 through a conveying pipeline 2, and the conveying pipeline 2 is also communicated with a conveying pump component;
the mixing component is communicated with the conveying pipeline 2 and comprises a venturi mixing pipe 7 and a static mixer 8, the feeding end of the venturi mixing pipe 7 is also communicated with a carbon dioxide storage tank 6, the static mixer 8 is provided with three groups, and the static mixers 8 are connected into the conveying pipeline 2 in series;
the conveying pump assembly comprises a conveying pump I4 and a conveying pump II 9, wherein the conveying pump I4 is arranged on a conveying pipeline 2 close to the discharge end of the material tank 1, and the conveying pump II 9 is arranged on the middle part pipe body of the conveying pipeline 2.
Example two
In addition to all the technical features in the first embodiment, the present embodiment further includes:
the discharge end of the material tank 1 is communicated with a product temperature regulator 5 through a conveying pipeline 2, so that the temperature of the product can be ensured to be kept at about 4-8 degrees in the mixing process.
One of them static mixer 8 is connected on the pipeline 2 between venturi mixing pipe 7 and delivery pump two 9, and two other static mixer 8 are connected on pipeline 2 that delivery pump two 9 output was linked together, make the product carry through two delivery pumps, and then can realize the multiple mixing to the product, can effectively improve the carbon dioxide and contain the gas multiple to 5 times.
In the conveying direction, a static holding mixing pipe 10 is communicated with the conveying pipeline 2 between the filling storage tank 3 and the tail end static mixer 8.
Example III
In addition to all the technical features in the first embodiment, the present embodiment further includes:
the conveying pipeline 2 between the product temperature regulator 5 and the Venturi mixing pipe 7 is communicated with a diversion pipeline 14, the other end of the diversion pipeline 14 is communicated with the conveying pipeline 2 connected with the output end of the static holding mixing pipe 10, and a second barometer 15 and a second electromagnetic valve 16 are arranged on the pipe body of the diversion pipeline 14, so that raw materials and carbon dioxide can be selectively supplemented into the conveying pipeline 2 according to the mixing condition to be continuously mixed, and the gas content multiple of the carbon dioxide in the raw materials is ensured.
A manual valve 11 and one of the barometers 12 are mounted on the delivery pipe 2 between the output end of the diversion pipe 14 and the static holding mixing pipe 10.
A first electromagnetic valve 13 and a first other barometer 12 are arranged on the conveying pipeline 2 between the output end of the diversion pipeline 14 and the filling storage tank 3.
The output end of the filling storage tank 3 is connected with an output pipeline 18, and a flowmeter 19 and a pressure sensor 20 are arranged on the output pipeline 18.
Working principle: the method comprises the steps of adopting a double-delivery pump and an upgrading venturi tube to be matched with a professional sanitary static spiral mixer, introducing carbon dioxide into the venturi tube to perform primary mixing, sequentially mixing carbonated beverages for two times, three times and four times through three static mixers, and finally delivering the mixed carbonated beverages to a filling storage tank through a static holding mixing tube and filling qualified products.
It will be evident to those skilled in the art that the utility model is not limited to the details of the foregoing illustrative embodiments, and that the present utility model may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive, the scope of the utility model being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present disclosure describes embodiments, not every embodiment is provided with a separate embodiment, and that this description is provided for clarity only, and that the disclosure is not limited to the embodiments described in detail below, and that the embodiments described in the examples may be combined as appropriate to form other embodiments that will be apparent to those skilled in the art.
Claims (8)
1. The utility model provides a carbon dioxide mixing system, includes material jar (1), filling storage tank (3) and compounding subassembly, its characterized in that: the material tank (1) is communicated with the filling storage tank (3) through a conveying pipeline (2), and a conveying pump assembly is further communicated with the conveying pipeline (2);
the mixing assembly is communicated with the conveying pipeline (2), the mixing assembly comprises a Venturi mixing pipe (7) and a static mixer (8), a carbon dioxide storage tank (6) is further communicated with the feeding end of the Venturi mixing pipe (7), three groups of static mixers (8) are arranged, and the static mixers (8) are connected into the conveying pipeline (2) in series;
the conveying pump assembly comprises a conveying pump I (4) and a conveying pump II (9), wherein the conveying pump I (4) is arranged on a conveying pipeline (2) close to the discharge end of the material tank (1), and the conveying pump II (9) is arranged on the middle part pipe body of the conveying pipeline (2).
2. A carbon dioxide mixing system as defined in claim 1, wherein: the discharge end of the material tank (1) is communicated with a product temperature regulator (5) through a conveying pipeline (2).
3. A carbon dioxide mixing system as defined in claim 1, wherein: one static mixer (8) is connected to the conveying pipeline (2) between the Venturi mixing pipe (7) and the conveying pump II (9), and the other two static mixers (8) are connected to the conveying pipeline (2) communicated with the output end of the conveying pump II (9).
4. A carbon dioxide mixing system as defined in claim 1, wherein: with the direction of delivery, the conveying pipeline (2) between the filling storage tank (3) and the terminal static mixer (8) is communicated with a static holding mixing pipe (10).
5. A carbon dioxide mixing system as claimed in claim 2, wherein: the product temperature regulator (5) and the venturi mixing tube (7) are communicated with a diversion pipeline (14) on the conveying pipeline (2), the other end of the diversion pipeline (14) is communicated with the conveying pipeline (2) connected with the output end of the static holding mixing tube (10), and a second barometer (15) and a second electromagnetic valve (16) are arranged on the tube body of the diversion pipeline (14).
6. A carbon dioxide mixing system as defined in claim 5, wherein: a manual valve (11) and one barometer I (12) are arranged on the conveying pipeline (2) between the output end of the diversion pipeline (14) and the static holding mixing pipe (10).
7. A carbon dioxide mixing system as defined in claim 5, wherein: and a first electromagnetic valve (13) and a first barometer (12) are arranged on the conveying pipeline (2) between the output end of the diversion pipeline (14) and the filling storage tank (3).
8. A carbon dioxide mixing system as defined in claim 1, wherein: the output end of the filling storage tank (3) is connected with an output pipeline (18), and a flowmeter (19) and a pressure sensor (20) are arranged on the output pipeline (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321984489.1U CN220589801U (en) | 2023-07-26 | 2023-07-26 | Carbon dioxide mixing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321984489.1U CN220589801U (en) | 2023-07-26 | 2023-07-26 | Carbon dioxide mixing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220589801U true CN220589801U (en) | 2024-03-15 |
Family
ID=90176244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321984489.1U Active CN220589801U (en) | 2023-07-26 | 2023-07-26 | Carbon dioxide mixing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220589801U (en) |
-
2023
- 2023-07-26 CN CN202321984489.1U patent/CN220589801U/en active Active
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