System for efficiently adding carbon dioxide into deoxidized water

Through the combined system of the chiller thin plate cooler and pressure control valve, the proportion of carbon dioxide in deoxygenated water is improved, the problem of unstable carbon dioxide content in beer production is solved, and the effect of saving carbon dioxide use and stabilizing the taste of beer is achieved.

CN222331875UActive Publication Date: 2025-01-10YANJING BEER YULIN
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Patent Information

Application Number
CN202421048230.0
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-05-14
Publication Date
2025-01-10
Estimated Expiration
2034-05-14

AI Technical Summary

Technical Problem

In beer production, during the traditional deoxygenated water addition of carbon dioxide, carbon dioxide cannot be quickly integrated, resulting in unstable carbon dioxide content, affecting the foaming properties and flavor of beer, and there is a problem of a large amount of carbon dioxide waste.

Method used

The combined system of the chilled thin plate cooler and pressure control valve is adopted to cool down the high temperature deoxygenation water and squeeze into small bubbles in a narrow space. Combined with the pressure control valve, the pressure maintenance ratio is increased from the original 30%. To 95%, and evenly disperse carbon dioxide through the premixer to ensure a stable concentration.

Benefits of technology

It greatly saves the amount of carbon dioxide used, stabilizes the concentration of carbon dioxide, avoids the taste and flavor problems of beer caused by unstable concentrations, and reduces carbon dioxide waste.

✦ Generated by Eureka AI based on patent content.

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    Figure CN222331875U_ABST
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Abstract

The utility model discloses a system for efficiently adding carbon dioxide into deoxidized water, which belongs to the technical field of beer production, solves the technical problem of production waste caused by the fact that a large amount of carbon dioxide which cannot be fused into the deoxidized water enters a tank and then is discharged, and comprises a carbon dioxide tank, a deoxidizing tower, a deoxidized water tank, a chilling sheet cooler and a controller, the deoxidation tower is connected with the chilling sheet cooler through an input pipe, the input pipe is provided with a deoxidation water pump, the input pipe between the deoxidation water pump and the chilling sheet cooler is provided with a carbon dioxide pipe connected with a carbon dioxide tank, the carbon dioxide pipe is provided with a carbon dioxide regulating valve and a carbon dioxide mass flow meter, and the deoxidation water tank is connected with the chilling sheet cooler through an output pipe. And the output pipe is provided with a deoxidized water pressure control regulating valve and a deoxidized water pressure transmitter. Carbon dioxide and deoxidized water are cooled and removed through the chilling sheet cooler, pressure maintaining is conducted, the carbon dioxide fusion proportion is increased to 95% from original 30%, and the concentration is stable.
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Description

Technical Field

[0001] The utility model relates to the technical field of beer production, and more specifically, to a deoxygenated water efficient carbon dioxide adding system. Background Art

[0002] At present, in the process of producing beer, it is necessary to prepare deoxygenated water, and then mix it with the fermentation liquid in proportion to make the sake required for filling. However, the prepared deoxygenated water contains about 0.30% carbon dioxide, and it is necessary to add carbon dioxide to the prepared deoxygenated water to avoid the low proportion of carbon dioxide in the deoxygenated water. When a large amount of carbon dioxide is added during the dilution of the fermentation liquid, the carbon dioxide cannot be quickly integrated into the proportioning liquid, and a large number of bubbles are generated, which affects the accuracy of the measurement of the dilution ratio of carbon dioxide content. It will cause the following two situations to occur: First, when the carbon dioxide content is insufficient, the foaming of the beer will be reduced, the stimulation of carbon dioxide is too slight, the taste is bland, and the beer will lose its due characteristics; second, when the carbon dioxide content is too high, the killing power is too strong and the unique flavor of the beer, such as fragrance, bitterness, etc., will be diluted, and it will also cause the phenomenon of beer foam and easy explosion of bottles.

[0003] In the traditional method of preparing deoxygenated water, carbon dioxide is added to the outlet pipe before the deoxygenated water enters the tank to increase the carbon dioxide content of the deoxygenated water to 0.45%-0.55%. Since the outlet pipe has no pressure and the bubbles are large, the proportion of carbon dioxide dissolved in the deoxygenated water is low, about 30%, resulting in a large amount of carbon dioxide that cannot be dissolved in the deoxygenated water being discharged after entering the tank, causing production waste. Utility Model Content

[0004] The technical problem to be solved by the utility model is aimed at the above-mentioned deficiencies of the prior art. The purpose of the utility model is to provide a system for efficiently adding carbon dioxide to deoxygenated water, which can greatly save the usage of carbon dioxide and stabilize the concentration of carbon dioxide.

[0005] The technical solution of the utility model is: a deoxygenated water efficient carbon dioxide addition system, comprising a carbon dioxide tank, a deoxygenation tower, a deoxygenated water tank, and also a chilled thin plate cooler and a controller, wherein the deoxygenation tower is connected to the inlet of the chilled thin plate cooler through an input pipe, the input pipe is provided with a deoxygenated water pump, the input pipe between the deoxygenated water pump and the inlet of the chilled thin plate cooler is provided with a carbon dioxide pipe connected to the carbon dioxide tank, the carbon dioxide pipe is provided with a carbon dioxide regulating valve and a carbon dioxide mass flow meter, the deoxygenated water tank is connected to the outlet of the chilled thin plate cooler through an output pipe, the output pipe is provided with a deoxygenated water pressure control regulating valve, the output pipe between the outlet of the chilled thin plate cooler and the deoxygenated water pressure control regulating valve is provided with a deoxygenated water pressure transmitter, and the controller is electrically connected to the deoxygenated water pump, the carbon dioxide regulating valve, the carbon dioxide mass flow meter, the deoxygenated water pressure control regulating valve, and the deoxygenated water pressure transmitter.

[0006] As a further improvement, the input pipe between the deoxygenated water pump and the carbon dioxide pipe is provided with a deoxygenated water mass flow meter, and the controller is electrically connected to the deoxygenated water mass flow meter.

[0007] Furthermore, a carbon dioxide sensor is provided on the output pipe between the deoxygenated water pressure control regulating valve and the deoxygenated water tank, and the controller is electrically connected to the carbon dioxide sensor.

[0008] Furthermore, a carbon dioxide pressure transmitter is provided on the carbon dioxide pipe between the carbon dioxide tank and the carbon dioxide regulating valve, and the controller is electrically connected to the carbon dioxide pressure transmitter.

[0009] Furthermore, the controller is any one of a PLC controller, a single-chip microcomputer, and an industrial computer.

[0010] Furthermore, a premixer is provided at the inlet of the chilled thin plate cooler.

[0011] Furthermore, the premixer includes a mixing tube, one end of which is connected to the input pipe, and the other end of which is connected to the inlet of the chilled thin plate cooler. A spherical nozzle is provided in the mixing tube, and the surface of the spherical nozzle is covered with spray holes. A joint is provided on the top of the spherical nozzle, and the joint passes through the mixing tube and is connected to the carbon dioxide tube. The joint and the mixing tube are sealed.

[0012] Beneficial Effects

[0013] Compared with the prior art, the utility model has the following advantages:

[0014] The utility model uses a chilled thin plate cooler to reduce the high-temperature deoxygenated water (78°C) to low-temperature deoxygenated water (3°C) to produce thermal expansion and contraction of carbon dioxide, and the narrow space inside the chilled thin plate cooler squeezes the carbon dioxide from large bubbles into small bubbles, and the deoxygenated water pressure control regulating valve is used to maintain the pressure inside the chilled thin plate cooler (the outlet pressure is increased to 0.2Mpa), so that the carbon dioxide integration ratio can be increased from the original 30% to 95%, which greatly saves the use of carbon dioxide, and can stabilize the concentration of carbon dioxide, avoiding the fluctuation of carbon dioxide during dilution due to the unstable concentration of carbon dioxide in deoxygenated water. BRIEF DESCRIPTION OF THE DRAWINGS

[0015] Figure 1 It is a schematic diagram of the structure of the utility model;

[0016] Figure 2 It is a schematic diagram of the structure of the premixer in the utility model.

[0017] Among them: 1-carbon dioxide tank, 2-deoxygenation tower, 3-deoxygenation water tank, 4-quenching thin plate cooler, 5-input pipe, 6-deoxygenation water pump, 7-carbon dioxide pipe, 8-carbon dioxide regulating valve, 9-carbon dioxide mass flow meter, 10-output pipe, 11-deoxygenation water pressure control regulating valve, 12-deoxygenation water pressure transmitter, 13-deoxygenation water mass flow meter, 14-carbon dioxide sensor, 15-carbon dioxide pressure transmitter, 16-premixer, 17-mixing tube, 18-spherical nozzle, 19-spray hole, 20-connector. DETAILED DESCRIPTION

[0018] The present invention will be further described below with reference to the specific embodiments in the accompanying drawings.

[0019] See also Figure 1-2 A deoxygenated water efficient carbon dioxide addition system includes a carbon dioxide tank 1, a deoxygenation tower 2, a deoxygenated water tank 3, and a chilled thin plate cooler 4 and a controller. The deoxygenation tower 2 is connected to the inlet of the chilled thin plate cooler 4 through an input pipe 5, and the input pipe 5 is provided with a deoxygenated water pump 6. The input pipe 5 between the deoxygenated water pump 6 and the inlet of the chilled thin plate cooler 4 is provided with a carbon dioxide pipe 7 connected to the carbon dioxide tank 1. The carbon dioxide pipe 7 is provided with a carbon dioxide regulating valve 8 and a carbon dioxide mass flowmeter 9. The deoxygenated water tank 3 is connected to the outlet of the chilled thin plate cooler 4 through an output pipe 10, and the output pipe 10 is provided with a deoxygenated water pressure control regulating valve 11. The output pipe 10 between the outlet of the chilled thin plate cooler 4 and the deoxygenated water pressure control regulating valve 11 is provided with a deoxygenated water pressure transmitter 12. The controller is electrically connected to the deoxygenated water pump 6, the carbon dioxide regulating valve 8, the carbon dioxide mass flowmeter 9, the deoxygenated water pressure control regulating valve 11, and the deoxygenated water pressure transmitter 12.

[0020] By using the chilled thin plate cooler 4, the carbon dioxide is caused to expand and contract due to the drop in high-temperature deoxygenated water (78°C) to low-temperature deoxygenated water (3°C), and the narrow space inside the chilled thin plate cooler 4 squeezes the carbon dioxide from large bubbles into small bubbles. By using the deoxygenated water pressure control valve 11 to maintain the pressure inside the chilled thin plate cooler 4 (such as increasing the outlet pressure of the chilled thin plate cooler 4 to 0.2Mpa), the carbon dioxide integration ratio can be increased from the original 30% to 95%, which greatly saves the use of carbon dioxide and stabilizes the concentration of carbon dioxide, avoiding fluctuations in carbon dioxide during dilution due to unstable carbon dioxide concentration in deoxygenated water.

[0021] In one embodiment, a deoxygenated water mass flowmeter 13 is provided on the input pipe 5 between the deoxygenated water pump 6 and the carbon dioxide pipe 7, and the controller is electrically connected to the deoxygenated water mass flowmeter 13. The controller can control the opening of the carbon dioxide regulating valve 8 according to the deoxygenated water flow detected by the deoxygenated water mass flowmeter 13 to match the carbon dioxide flow.

[0022] In one embodiment, a carbon dioxide sensor 14 is provided in the output pipe 10 between the deoxygenated water pressure control valve 11 and the deoxygenated water tank 3, and a controller is electrically connected to the carbon dioxide sensor 14. The controller can control the opening of the carbon dioxide regulating valve 8 according to the data fed back by the carbon dioxide sensor 14 to stabilize the concentration of carbon dioxide.

[0023] The carbon dioxide pipe 7 between the carbon dioxide tank 1 and the carbon dioxide regulating valve 8 is provided with a carbon dioxide pressure transmitter 15, and the controller is electrically connected to the carbon dioxide pressure transmitter 15. The carbon dioxide amount in the carbon dioxide tank 1 can be detected in real time by the carbon dioxide pressure transmitter 15, and an alarm is given in time when the carbon dioxide amount is less than the set amount.

[0024] The controller is any one of a PLC controller, a single chip microcomputer, and an industrial computer.

[0025] Furthermore, a premixer 16 is provided at the inlet of the chilled sheet cooler 4. The premixer 16 includes a mixing tube 17, one end of which is connected to the input tube 5, and the other end of which is connected to the inlet of the chilled sheet cooler 4. A spherical nozzle 18 is provided in the mixing tube 17, and the surface of the spherical nozzle 18 is covered with spray holes 19. A joint 20 is provided at the top of the spherical nozzle 18, and the joint 20 passes through the mixing tube 17 and is connected to the carbon dioxide tube 7. The joint 20 and the mixing tube 17 are sealed. Carbon dioxide is sprayed out from the spray holes 19 of the spherical nozzle 18, and can be more evenly dispersed into the deoxygenated water to ensure the integration ratio of carbon dioxide.

[0026] The above are only preferred implementations of the utility model. It should be pointed out that for those skilled in the art, several modifications and improvements can be made without departing from the structure of the utility model, which will not affect the effect of the implementation of the utility model and the practicality of the patent.

Claims

1. A system for efficiently adding carbon dioxide to deoxygenated water, comprising a carbon dioxide tank (1), a deoxygenation tower (2), and a deoxygenated water tank (3), characterized in that: The deoxidation tower (2) is connected to the inlet of the chilled thin plate cooler (4) via an inlet pipe (5), the inlet pipe (5) is provided with a deoxidation water pump (6), the inlet pipe (5) between the deoxidation water pump (6) and the inlet of the chilled thin plate cooler (4) is provided with a carbon dioxide pipe (7) connected to the carbon dioxide tank (1), the carbon dioxide pipe (7) is provided with a carbon dioxide regulating valve (8) and a carbon dioxide mass flow meter (9), the deoxidation water tank (3) is connected to the inlet of the chilled thin plate cooler (4), and the deoxidation tower (2) is connected to the inlet of the chilled thin plate cooler (4) via an inlet pipe (5). The outlet of the chilled thin plate cooler (4) is connected via an output pipe (10), the output pipe (10) is provided with a deoxygenated water pressure control regulating valve (11), the output pipe (10) between the outlet of the chilled thin plate cooler (4) and the deoxygenated water pressure control regulating valve (11) is provided with a deoxygenated water pressure transmitter (12), and the controller is electrically connected to the deoxygenated water pump (6), the carbon dioxide regulating valve (8), the carbon dioxide mass flow meter (9), the deoxygenated water pressure control regulating valve (11), and the deoxygenated water pressure transmitter (12).

2. A deoxygenated water efficient carbon dioxide addition system according to claim 1, characterized in that: The input pipe (5) between the deoxygenated water pump (6) and the carbon dioxide pipe (7) is provided with a deoxygenated water mass flow meter (13), and the controller is electrically connected to the deoxygenated water mass flow meter (13).

3. A deoxygenated water efficient carbon dioxide addition system according to claim 1, characterized in that: The output pipe (10) between the deoxygenated water pressure control regulating valve (11) and the deoxygenated water tank (3) is provided with a carbon dioxide sensor (14), and the controller is electrically connected to the carbon dioxide sensor (14).

4. A deoxygenated water efficient carbon dioxide addition system according to claim 1, characterized in that: The carbon dioxide pipe (7) between the carbon dioxide tank (1) and the carbon dioxide regulating valve (8) is provided with a carbon dioxide pressure transmitter (15), and the controller is electrically connected to the carbon dioxide pressure transmitter (15).

5. A deoxygenated water efficient carbon dioxide addition system according to claim 1, characterized in that: The controller is any one of a PLC controller, a single chip microcomputer and an industrial computer.

6. A deoxygenated water efficient carbon dioxide addition system according to any one of claims 1 to 5, characterized in that: The inlet of the chilled thin plate cooler (4) is provided with a pre-mixer (16).

7. A deoxygenated water efficient carbon dioxide addition system according to claim 6, characterized in that: The premixer (16) comprises a mixing tube (17), one end of which is connected to the input tube (5), and the other end of which is connected to the inlet of the chilled thin plate cooler (4). A spherical nozzle (18) is arranged in the mixing tube (17), and the surface of the spherical nozzle (18) is covered with spray holes (19). A joint (20) is arranged on the top of the spherical nozzle (18), and the joint (20) passes through the mixing tube (17) and is connected to the carbon dioxide tube (7). The joint (20) and the mixing tube (17) are sealed.