Beer filtering device applying cross-flow filtering technology
By combining dual cross-flow filtration technology and multi-stage ceramic filter membranes, the problem of residue residue caused by a single filter membrane in beer filtration devices is solved, achieving efficient filtration and improved stability of beer, and extending the shelf life and shelf life of beer.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-01-16
- Publication Date
- 2026-03-13
AI Technical Summary
When existing beer filtration devices use a single filter membrane, residues smaller than the pore size of the filter membrane can easily remain in the beer, resulting in poor filtration performance.
The system employs a dual cross-flow filtration technology, utilizing two sets of ceramic filter membranes for multi-stage filtration. These include a first filter membrane set and a second filter membrane set, with pore sizes of 0.2μm and smaller, respectively. The system performs coarse and fine filtration of beer through a porous support layer, a transition layer, and a separation layer, and achieves multiple circulation filtration by combining a return pipe and a one-way solenoid valve.
It improves the efficiency and effectiveness of beer filtration, ensures beer stability, extends shelf life and expiration date, and increases production efficiency.
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Figure CN223991078U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of cross-flow filtration technology, specifically a beer filtration device that applies cross-flow filtration technology. Background Technology
[0002] Cross-flow filtration has been widely used in beer and beverage production as well as liquid food. After fermentation, beer contains a large amount of yeast, fermentation byproducts and other impurities. In order to ensure the stability of beer and improve its shelf life, beer needs to be filtered to separate yeast and other impurities from the beer. Cross-flow filtration has gradually become the mainstream of modern equipment, replacing diatomaceous earth filtration and cardboard filtration.
[0003] A search revealed a hop churn device using cross-flow filtration disclosed in Chinese utility model patent CN202321694126.4. This device offers flexibility in operation through cross-flow filtration, allowing for both intermittent and continuous operation, significantly improving production efficiency. However, it can only filter beer through a single filter membrane, leaving residues smaller than the membrane pore size, resulting in poor filtration. Therefore, a beer filtration device using cross-flow filtration technology is proposed to address these issues. Summary of the Invention
[0004] To address the shortcomings of existing technologies, this utility model provides a beer filtration device that utilizes cross-flow filtration technology. This device offers advantages such as higher filtration efficiency and better filtration effect, solving the problem that during use, beer can only be filtered through a single filter membrane, resulting in residues smaller than the pore size of the filter membrane remaining in the beer and thus leading to poor filtration performance.
[0005] To achieve the above objectives, this utility model provides the following technical solution: a beer filtration device using cross-flow filtration technology, comprising a base, a raw liquid tank fixedly installed on the top of the base, a storage tank fixedly installed on the top of the base, and a filtration mechanism provided on the top of the base;
[0006] The filtration mechanism includes a first filter tank, which is mounted on the top of the base. A second filter tank is mounted on the right side of the first filter tank. A first water inlet pipe is connected to the bottom of the raw liquid tank, and a second water inlet pipe is connected to the right side of the first filter tank. A return pipe is connected to the top of the raw liquid tank, and a first diverter pipe and a second diverter pipe are connected to the bottom of the return pipe. A first filter membrane assembly is installed on the inner wall of the first filter tank, and a second filter membrane assembly is installed on the inner wall of the second filter tank.
[0007] Furthermore, a display window is fixedly installed on the front side of the raw liquid tank, and a slag discharge pipe is connected to the bottom of the raw liquid tank.
[0008] Furthermore, the side of the first water inlet pipe away from the original liquid tank is connected to the bottom of the first filter tank, and the side of the second water inlet pipe away from the first filter tank is connected to the bottom of the second filter tank.
[0009] Furthermore, the side of the return pipe away from the original liquid tank is connected to the top of the second filter tank via a second diversion pipe.
[0010] Furthermore, a scale is provided on the front side of the storage tank, an injection pipe is connected to the left side of the raw liquid tank, and a discharge pipe is connected to the right side of the storage tank.
[0011] Furthermore, both the first and second filter membrane groups are ceramic filter membranes. The first filter membrane group includes a porous support layer, a transition layer, and a separation layer. The pore size of the first filter membrane group is 0.2 μm, and the pore size of the second filter membrane group is smaller than that of the first filter membrane group.
[0012] Furthermore, a flow meter is connected to the top of the return pipe, and one-way solenoid valves are connected to the outside of the first inlet pipe, the second inlet pipe, the return pipe, the first branch pipe, and the second branch pipe. A conduit is connected to the right side of the second filter tank, and the right side of the conduit is connected to the storage tank.
[0013] Compared with the prior art, the technical solution of this application has the following beneficial effects:
[0014] 1. This beer filtration device, which uses cross-flow filtration technology, buffers the beer to be filtered in the raw liquid tank. After double cross-flow filtration, the filtered beer liquid stored in the storage tank has a better filtration effect.
[0015] 2. This beer filtration device, which utilizes cross-flow filtration technology, achieves better beer filtration results through the coordinated operation of various structures within the filtration mechanism. This improves the efficiency of subsequent processes, accelerates beer production, and ensures superior beer filtration through multi-stage filtration. Attached Figure Description
[0016] Figure 1 This is a front view schematic diagram of the present utility model;
[0017] Figure 2 This is a schematic diagram of the filtration mechanism of this utility model;
[0018] Figure 3 This is a partial cross-sectional view of the present invention.
[0019] In the diagram: 1. Base, 2. Raw material tank, 3. Storage tank, 4. Filtration mechanism, 401. First filter tank, 402. Second filter tank, 403. First water inlet pipe, 404. Second water inlet pipe, 405. Return pipe, 406. First branch pipe, 407. Second branch pipe, 408. First filter membrane group, 409. Second filter membrane group, 5. Sludge discharge pipe, 6. Flow meter, 7. Conduit. Detailed Implementation
[0020] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.
[0021] Please see Figure 1-3 A beer filtration device using cross-flow filtration technology in this embodiment includes a base 1, a raw liquid tank 2 fixedly installed on the top of the base 1, a storage tank 3 fixedly installed on the top of the base 1, and a filtration mechanism 4 provided on the top of the base 1.
[0022] The filtration mechanism 4 includes a first filter tank 401, which is mounted on the top of the base 1. A second filter tank 402 is mounted on the right side of the first filter tank 401. A first water inlet pipe 403 is connected to the bottom of the raw liquid tank 2. A second water inlet pipe 404 is connected to the right side of the first filter tank 401. A return pipe 405 is connected to the top of the raw liquid tank 2. A first diverter pipe 406 is connected to the bottom of the return pipe 405. A second diverter pipe 407 is connected to the bottom of the return pipe 405. A first filter membrane assembly 408 is installed on the inner wall of the first filter tank 401. A second filter membrane assembly 409 is installed on the inner wall of the second filter tank 402.
[0023] exist Figure 1 and Figure 2 In the middle, a display window is fixedly installed on the front side of the raw liquid tank 2, and a slag discharge pipe 5 is connected to the bottom of the raw liquid tank 2.
[0024] Specifically, after multiple filtrations, a large amount of residue is stored in the original liquid tank 2. At this time, the one-way solenoid valve is activated, and the lees are discharged through the lees discharge pipe 5.
[0025] exist Figure 1 and Figure 2 In the first water inlet pipe 403, the side away from the original liquid tank 2 is connected to the bottom of the first filter tank 401, and the side away from the first filter tank 401 is connected to the bottom of the second filter tank 402.
[0026] Specifically, by setting the first filter tank 401 and the second filter tank 402 to limit the first filter membrane group 408 and the second filter membrane group 409, the one-way solenoid valve on the first water inlet pipe 403 is activated. At this time, the beer enters the first filter tank 401 through the first water inlet pipe 403, and the first filter membrane group 403 can then perform coarse filtration of the beer through the porous support layer, transition layer and separation layer.
[0027] exist Figure 1 and Figure 3 In the middle, the side of the return pipe 405 away from the original liquid tank 2 is connected to the top of the second filter tank 402 through the second diversion pipe 407.
[0028] Specifically, the residue after double filtration is poured back to the original liquid tank 2 through the return pipe 405, which facilitates multiple filtration cycles and ensures better filtration results.
[0029] exist Figure 2 and Figure 3 In the middle, a scale is set on the front side of the storage tank 3, an injection pipe is connected to the left side of the raw liquid tank 2, and a discharge pipe is connected to the right side of the storage tank 3.
[0030] exist Figure 2 and Figure 3 In this process, both the first filter membrane group 408 and the second filter membrane group 409 are ceramic filter membranes. The first filter membrane group 408 includes a porous support layer, a transition layer and a separation layer. The pore size of the first filter membrane group 408 is 0.2 μm, and the pore size of the second filter membrane group 409 is smaller than that of the first filter membrane group 408.
[0031] Specifically, filtration is performed through a first filter membrane group 408 and a second filter membrane group 409 with different pore sizes, thereby ensuring better filtration effect.
[0032] exist Figure 2 and Figure 3 In the middle, a flow meter 6 is connected to the top of the return pipe 405. One-way solenoid valves are connected to the outside of the first inlet pipe 403, the second inlet pipe 404, the return pipe 405, the first branch pipe 406, and the second branch pipe 407. A conduit 7 is connected to the right side of the second filter tank 402, and the right side of the conduit 7 is connected to the storage tank 3.
[0033] During implementation, the following steps are performed: First, fill the original liquid tank 2 through the injection pipe. When beer filtration is required, the controller first drives the booster pump outside the first inlet pipe 403 to start. At this time, the beer enters the first filter tank 401 through the first inlet pipe 403. The first filter membrane assembly 403 then performs coarse filtration of the beer through the porous support layer, transition layer, and separation layer. At this time, some of the fermented beer flows over the upper end of the first filter membrane assembly 408 due to flow shear force. The solenoid valve is activated, and the beer enters the return pipe 405 through the first diversion pipe 406 and returns to the original liquid tank 2 through the return pipe 405. The remaining beer enters the second filter tank 402 through the second inlet pipe 404. At this time, some of the fermented beer flows over the upper end of the second filter membrane assembly 409 due to flow shear force and returns to the original liquid tank 2 through the return pipe 405. The remaining beer after secondary filtration enters the storage tank 3 through the conduit 7, thus completing the filtration process.
[0034] In summary, by setting up the first filter tank 401 and the second filter tank 402 to limit the movement of the first filter membrane group 408 and the second filter membrane group 409, the one-way solenoid valve on the first water inlet pipe 403 is activated. At this time, the beer enters the first filter tank 401 through the first water inlet pipe 403. The first filter membrane group 403 can then perform coarse filtration of the beer through the porous support layer, transition layer, and separation layer. At this time, some of the fermented beer liquid flows over the upper end of the first filter membrane group 408 due to the flow shear force, and the solenoid valve is activated. The liquid enters the return pipe 405 through the first branch pipe 406 and returns to the original liquid tank 2 through the return pipe 405. By setting the second filter membrane group 409, part of the liquid that has been filtered by the first filter membrane group 408 is introduced into the second filter membrane group 409 through the second water inlet pipe 403. At this time, part of the fermented beer liquid flows through the upper end of the second filter membrane group 409 under the action of flow shear force and returns to the original liquid tank 2 through the return pipe 405. The remaining liquid that has been filtered twice enters the storage tank 3 through the conduit 7, thus completing the filtration.
[0035] All electrical components mentioned in this article are connected to external controllers and 220V AC mains power. The controllers can be conventional known devices such as computers. The specific models and specifications of each device mentioned in this article need to be selected and determined according to the actual specifications of the device. The specific selection and calculation methods adopt existing technologies in this field, so they will not be described in detail here.
[0036] It should be noted that, in this document, relational terms such as "first" and "second" are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such a process, method, article, or apparatus. Without further limitations, an element defined by the phrase "comprising one..." does not exclude the presence of other identical elements in the process, method, article, or apparatus that includes said element.
[0037] Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the present invention, the scope of which is defined by the appended claims and their equivalents.
Claims
1. A beer filtering device applying cross-flow filtration technology, comprising a base (1), characterized in that: The top of the base (1) is fixedly provided with an original liquid tank (2), the top of the base (1) is fixedly provided with a storage tank (3), and the top of the base (1) is provided with a filtering mechanism (4); The filtering mechanism (4) comprises a first filtering tank (401), the top of the base (1) is provided with the first filtering tank (401), the right side of the first filtering tank (401) is provided with a second filtering tank (402), the bottom of the original liquid tank (2) is connected with a first water inlet pipe (403), the right side of the first filtering tank (401) is connected with a second water inlet pipe (404), the top of the original liquid tank (2) is connected with a reflux pipe (405), the bottom of the reflux pipe (405) is connected with a first shunt pipe (406), the bottom of the reflux pipe (405) is connected with a second shunt pipe (407), and the inner wall of the first filtering tank (401) is provided with a first filter membrane group (408).
2. A beer filtration apparatus using cross-flow filtration technology according to claim 1, characterized in that: The front side of the original liquid tank (2) is fixedly provided with a display window, and the bottom of the original liquid tank (2) is connected with a slag discharge pipe (5).
3. A beer filtration apparatus using cross-flow filtration technology according to claim 1, characterized in that: The first water inlet pipe (403) is connected with the bottom of the first filtering tank (401) away from the original liquid tank (2), and the second water inlet pipe (404) is connected with the bottom of the second filtering tank (402) away from the first filtering tank (401).
4. A beer filtration apparatus using cross-flow filtration technology according to claim 1, characterized in that: The reflux pipe (405) is connected with the top of the second filtering tank (402) away from the original liquid tank (2) through the second shunt pipe (407).
5. A beer filtration apparatus using cross-flow filtration technology according to claim 1, characterized in that: The front side of the storage tank (3) is provided with a scale, the left side of the original liquid tank (2) is connected with a pouring pipe, and the right side of the storage tank (3) is connected with a discharge pipe.
6. A beer filtration apparatus using cross-flow filtration technology according to claim 1, characterized in that: The first filter membrane group (408) and the second filter membrane group (409) are both ceramic filter membranes, the first filter membrane group (408) comprises a porous support layer, a transition layer and a separation layer, the pore size of the first filter membrane group (408) is 0.2 μm, and the pore size of the second filter membrane group (409) is smaller than that of the first filter membrane group (408).
7. A beer filtration apparatus using cross-flow filtration technology according to claim 1, characterized in that: The top of the reflux pipe (405) is connected with a flow meter (6), one-way electromagnetic valves are connected to the outside of the first water inlet pipe (403), the second water inlet pipe (404), the reflux pipe (405), the first shunt pipe (406) and the second shunt pipe (407), the right side of the second filtering tank (402) is connected with a conduit (7), and the right side of the conduit (7) is connected with the storage tank (3).
Citation Information
Patent Citations
A hop dry hopping device using cross-flow filtration
CN221028315U