CN215769491U - Accurate control system is filled to deoxidization water carbon dioxide - Google Patents
Accurate control system is filled to deoxidization water carbon dioxide Download PDFInfo
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- CN215769491U CN215769491U CN202121999094.XU CN202121999094U CN215769491U CN 215769491 U CN215769491 U CN 215769491U CN 202121999094 U CN202121999094 U CN 202121999094U CN 215769491 U CN215769491 U CN 215769491U
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Abstract
The utility model discloses a carbon dioxide filling accurate control system for deoxygenated water, which relates to the technical field of beer production and solves the technical problem of poor carbon dioxide filling accuracy, and comprises a deoxygenation tower and a heat exchanger, and also comprises a controller, a carbon dioxide header pipe, a first filling pipe and a second filling pipe, wherein the output end of the carbon dioxide header pipe is respectively connected with the input end of the first filling pipe and the input end of the second filling pipe, the output end of the first filling pipe is connected with the input port of the deoxygenation tower, the output end of the second filling pipe is connected with the input port of the heat exchanger, the first filling pipe is respectively provided with a first adjusting valve, a first flowmeter and a first stop valve, the second filling pipe is respectively provided with a second adjusting valve, the controller is electrically connected with the first regulating valve, the first flowmeter, the first stop valve, the second regulating valve, the second flowmeter and the second stop valve.
Description
Technical Field
The utility model relates to the technical field of beer production, in particular to a carbon dioxide filling accurate control system for deoxygenated water.
Background
Currently, deoxygenated water is required to be used during the dilution process for producing beer. The carbon dioxide is required to be filled twice in the preparation process of the deoxygenated water, the filling flow rate is artificially controlled by manually looking at scales of a float flowmeter of the glass tube and matching with a flow regulating hand valve, the change of working conditions in the water preparation process cannot be detected by the control method, and the hidden danger of unqualified products can be caused by the fact that staff careless.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem of the prior art, and aims to provide a carbon dioxide filling precision control system for deoxygenated water, which can improve the precision.
The technical scheme of the utility model is as follows: the utility model provides a deoxidized water carbon dioxide fills accurate control system, includes deoxidation tower, heat exchanger, still includes controller, carbon dioxide house steward, first filling tube, second filling tube, the output of carbon dioxide house steward is connected respectively the input of first filling tube, the input of second filling tube, the output of first filling tube is connected the input port of deoxidation tower, the output of second filling tube is connected the input port of heat exchanger, be equipped with first governing valve, first flowmeter, first stop valve on the first filling tube respectively, be equipped with second governing valve, second flowmeter, second stop valve on the second filling tube respectively, controller electric connection first governing valve, first flowmeter, first stop valve, second governing valve, second flowmeter, second stop valve.
As a further improvement, the first flowmeter and the second flowmeter are both analog quantity flowmeters with output quantities of 4-20 mA.
Further, the first regulating valve and the second regulating valve are both pneumatic regulating valves.
Further, the controller is a PLC module, a single chip microcomputer or an industrial personal computer.
Further, the first regulating valve, the first flow meter and the first stop valve are sequentially arranged on the first filling pipe, wherein the first regulating valve is close to the output end of the carbon dioxide main pipe, and the first stop valve is close to the input port of the deoxygenation tower.
Further, the second regulating valve, the second flow meter and the second stop valve are sequentially arranged on the second filling pipe, wherein the second regulating valve is close to the output end of the carbon dioxide main pipe, and the second stop valve is close to the input port of the heat exchanger.
Further, the heat exchanger comprises a shell, and a plurality of layers of heat exchange thin plates are arranged in the shell.
Furthermore, a filter is arranged on the carbon dioxide header pipe.
Advantageous effects
Compared with the prior art, the utility model has the advantages that:
according to the beer filling device, the opening degree of the first regulating valve is controlled according to the first flowmeter so as to accurately control the flow of the first filling pipe, the opening degree of the second regulating valve is controlled according to the second flowmeter so as to accurately control the flow of the second filling pipe, the flow of the first filling pipe and the flow of the second filling pipe are accurately matched according to a set proportion, and the production quality of beer can be effectively guaranteed.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
Wherein: the system comprises a deoxygenation tower 1, a heat exchanger 2, a carbon dioxide header pipe 3, a first filling pipe 4, a second filling pipe 5, a first regulating valve 6, a first flowmeter 7, a first stop valve 8, a second regulating valve 9, a second flowmeter 10 and a second stop valve 11.
Detailed Description
The utility model will be further described with reference to specific embodiments shown in the drawings.
Referring to fig. 1, a carbon dioxide filling accurate control system for deoxygenated water comprises a deoxygenation tower 1, a heat exchanger 2, a controller, a carbon dioxide header pipe 3, a first filling pipe 4 and a second filling pipe 5, wherein the output end of the carbon dioxide header pipe 3 is respectively connected with the input end of the first filling pipe 4 and the input end of the second filling pipe 5, the output end of the first filling pipe 4 is connected with the input port of the deoxygenation tower 1, the output end of the second filling pipe 5 is connected with the input port of the heat exchanger 2, the first filling pipe 4 is respectively provided with a first adjusting valve 6, a first flowmeter 7 and a first stop valve 8, the second filling pipe 5 is respectively provided with a second adjusting valve 9, the controller is electrically connected with the first regulating valve 6, the first flowmeter 7, the first stop valve 8, the second regulating valve 9, the second flowmeter 10 and the second stop valve 11. Thereby through the flow according to first flowmeter 7 control first governing valve 6's aperture accurate control first filling pipe 4, thereby control the flow of second governing valve 9's aperture accurate control second filling pipe 5 according to second flowmeter 10, realize the accurate cooperation work according to the proportion that sets for of the flow of first filling pipe 4 and the flow of second filling pipe 5, can effectively guarantee the production quality of beer.
The first flowmeter 7 and the second flowmeter 10 are both analog quantity flowmeters with output quantities of 4-20mA, the first regulating valve 6 and the second regulating valve 9 are both pneumatic regulating valves, and the controller is a PLC module or a single chip microcomputer or an industrial personal computer.
A first regulating valve 6, a first flow meter 7 and a first cut-off valve 8 are sequentially arranged on the first filling pipe 4, wherein the first regulating valve 6 is close to the output end of the carbon dioxide header pipe 3, and the first cut-off valve 8 is close to the input port of the deoxygenator column 1.
A second regulating valve 9, a second flow meter 10 and a second stop valve 11 are arranged in this order on the second filling pipe 5, wherein the second regulating valve 9 is close to the outlet of the carbon dioxide manifold 3 and the second stop valve 11 is close to the inlet of the heat exchanger 2.
The heat exchanger 2 comprises a shell, a plurality of layers of heat exchange thin plates are arranged in the shell, the plurality of layers of heat exchange thin plates are vertically arranged in the shell, deoxygenated water in the deoxygenation tower 1 is injected into the heat exchanger 2, carbon dioxide bubbles are reduced by filling carbon dioxide gas into the heat exchange thin plates through the characteristics of the thin plates, the contact area between the deoxygenated water and the carbon dioxide is increased, the carbon dioxide is better dissolved into the deoxygenated water, and the consumption of the carbon dioxide is reduced.
The carbon dioxide main pipe 3 is provided with a filter 12 for filtering impurities such as dust in the carbon dioxide gas.
The above is only a preferred embodiment of the present invention, and it should be noted that it is obvious to those skilled in the art that several variations and modifications can be made without departing from the structure of the present invention, which will not affect the effect of the implementation of the present invention and the utility of the patent.
Claims (8)
1. A deoxygenated water carbon dioxide filling accurate control system comprises a deoxygenated tower (1) and a heat exchanger (2), and is characterized by further comprising a controller, a carbon dioxide header pipe (3), a first filling pipe (4) and a second filling pipe (5), wherein the output end of the carbon dioxide header pipe (3) is respectively connected with the input end of the first filling pipe (4) and the input end of the second filling pipe (5), the output end of the first filling pipe (4) is connected with the input port of the deoxygenated tower (1), the output end of the second filling pipe (5) is connected with the input port of the heat exchanger (2), the first filling pipe (4) is respectively provided with a first adjusting valve (6), a first flowmeter (7) and a first stop valve (8), the second filling pipe (5) is respectively provided with a second adjusting valve (9), a second flowmeter (10) and a second stop valve (11), the controller is electrically connected with the first regulating valve (6), the first flow meter (7), the first stop valve (8), the second regulating valve (9), the second flow meter (10) and the second stop valve (11).
2. The deoxygenated water carbon dioxide filling precision control system according to claim 1, wherein the first flow meter (7) and the second flow meter (10) are both analog quantity flow meters with output quantity of 4-20 mA.
3. The system for accurately controlling the carbon dioxide filling of deoxygenated water according to claim 1, wherein said first regulating valve (6) and said second regulating valve (9) are pneumatic regulating valves.
4. The system for accurately controlling carbon dioxide filling of deoxygenated water according to claim 1, wherein the controller is a PLC module, a single chip microcomputer or an industrial personal computer.
5. A deoxygenated water carbon dioxide filling precision control system according to claim 1, characterized in that the first regulating valve (6), the first flow meter (7) and the first cut-off valve (8) are sequentially arranged on the first filling pipe (4), wherein the first regulating valve (6) is close to the output end of the carbon dioxide main pipe (3), and the first cut-off valve (8) is close to the input port of the deoxygenating tower (1).
6. The deoxygenated water carbon dioxide filling precision control system of claim 1, characterized in that the second regulating valve (9), the second flow meter (10) and the second stop valve (11) are sequentially arranged on the second filling pipe (5), wherein the second regulating valve (9) is close to the output end of the carbon dioxide header pipe (3), and the second stop valve (11) is close to the input end of the heat exchanger (2).
7. The system for accurately controlling the carbon dioxide filling of deoxygenated water according to claim 1, wherein said heat exchanger (2) comprises a housing, and a plurality of layers of heat exchange thin plates are arranged in said housing.
8. The system for accurately controlling the carbon dioxide filling of deoxygenated water according to claim 1, characterized in that said carbon dioxide main pipe (3) is provided with a filter (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121999094.XU CN215769491U (en) | 2021-08-24 | 2021-08-24 | Accurate control system is filled to deoxidization water carbon dioxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121999094.XU CN215769491U (en) | 2021-08-24 | 2021-08-24 | Accurate control system is filled to deoxidization water carbon dioxide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215769491U true CN215769491U (en) | 2022-02-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121999094.XU Active CN215769491U (en) | 2021-08-24 | 2021-08-24 | Accurate control system is filled to deoxidization water carbon dioxide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215769491U (en) |
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2021
- 2021-08-24 CN CN202121999094.XU patent/CN215769491U/en active Active
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