Multi-functional low-acid beverage dispensing system
By integrating a multi-functional low-acid beverage blending system, the problem of handling diverse beverage formulas in existing systems has been solved, enabling efficient and low-cost beverage production and improving product quality and production efficiency.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- THE COCA COLA CO
- Filing Date
- 2025-07-25
- Publication Date
- 2026-06-26
AI Technical Summary
Existing low-acid beverage production systems are limited in function and cannot effectively process multiple ingredients such as dairy products, coffee, tea, and plant proteins, leading to increased operating costs, increased complexity, and unstable product quality.
Design a multifunctional low-acid beverage blending system that integrates main component pretreatment, auxiliary functional component pretreatment, cooking and mixing-homogenization-emulsification-standardization production units, including balance tanks, tubular heat exchangers, homogenizers and final blending tanks, to process a variety of raw materials and additives.
It improved production efficiency, reduced operational complexity and costs, and ensured consistent product quality and efficient production.
Smart Images
Figure CN224404851U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of beverage preparation systems, and in particular to a multifunctional low-acid beverage preparation system. Background Technology
[0002] Low-acid beverages are beverages with a pH value greater than 4.6 and a water activity greater than 0.85. Such beverages must be sterilized with a sterilization value greater than 3.0 to ensure safety.
[0003] Existing low-acid beverage production systems often face challenges in efficiently processing diverse beverage formulations. Many systems are single-function and unable to handle multiple ingredients such as dairy, coffee, tea, and plant proteins. This limitation leads to increased operating costs, increased complexity, and inconsistencies in product quality.
[0004] While existing patents and technical documents describe various mixing and homogenizing equipment, they lack a comprehensive system that can fully meet the diverse needs of beverage formulations.
[0005] Therefore, there is an urgent need for an integrated system that can simplify multiple processes and ensure high quality of the final product. Utility Model Content
[0006] To address the aforementioned problems, the main objective of this invention is to provide a multifunctional low-acid beverage preparation system, which is versatile: the system can process various beverage formulations, including dairy products, coffee, tea, and plant proteins.
[0007] Another objective of this invention is to provide a multifunctional low-acid beverage preparation system that is highly efficient. By integrating mixing, homogenization, and standardization processes, this system significantly improves production efficiency.
[0008] Another objective of this invention is to provide a multifunctional low-acid beverage preparation system that is flexible, capable of handling a variety of raw materials and additives, and meeting different production needs.
[0009] Another objective of this invention is to provide a multifunctional low-acid beverage preparation system that is cost-effective, can effectively save costs, and reduce operational complexity and maintenance costs.
[0010] To achieve the above objectives, this utility model provides a multifunctional low-acid beverage preparation system, characterized in that it includes: a main component pretreatment production unit, an auxiliary functional component pretreatment production unit, a cooking production unit, and a mixing-homogenizing-emulsifying-standardizing production unit. The main component pretreatment production unit, the auxiliary functional component pretreatment production unit, the cooking production unit, and the mixing-homogenizing-emulsifying-standardizing production unit all contain a common and sequentially connected balance tank, a second tubular heat exchanger, a homogenizer, and a final preparation tank.
[0011] The multifunctional low-acid beverage blending system, wherein the main component pretreatment production unit includes: a side hopper, an oil-sauce material feed line, a vacuum high-shear mixer, a feed pump, a milk hydration tank-premixing tank, a discharge pump, a magnetic filter, a second filter, the balance tank, the second tubular heat exchanger, the homogenizer, and the final blending tank.
[0012] The vacuum high-shear mixer has a side hopper and an oil-sauce-like material feed line connected to its inlet. The outlet of the vacuum high-shear mixer is connected to the inlet of the milk hydration tank-premix tank. The outlet of the milk hydration tank-premix tank is connected in sequence to a discharge pump, a magnetic filter, a second filter, a balance tank, a second tubular heat exchanger, a homogenizer, and a final mixing tank.
[0013] The multifunctional low-acid beverage preparation system includes a first tubular heat exchanger connected in parallel between the inlet of the milk hydration tank-premix tank and the outlet of the discharge pump. The outlet of the first tubular heat exchanger is also connected to the inlet of the vacuum high-shear mixer.
[0014] The multifunctional low-acid beverage preparation system includes a second centrifugal pump and a second rotor pump connected in parallel between the balance tank and the second tubular heat exchanger.
[0015] The multifunctional low-acid beverage blending system, wherein the auxiliary functional component pretreatment production unit includes: an oil-sauce material feed line, an emulsifying high-shear mixing tank, a small material dissolving tank, a first filter, a first rotor pump, the balance tank, a second tubular heat exchanger, the homogenizer, and the final blending tank.
[0016] The emulsifying high-shear mixing tank is connected to the oil-sauce-like material feed pipeline, and both the emulsifying high-shear mixing tank and the small material dissolving tank are connected to the inlet of the first filter. The outlet of the first filter is connected to the inlet of the balance tank. The outlet of the balance tank is sequentially connected to the second tubular heat exchanger, the homogenizer, and the final mixing tank.
[0017] The multifunctional low-acid beverage preparation system further includes an auxiliary functional component pretreatment production unit comprising a milk hydration tank-premixing tank, a discharge pump, a magnetic filter, and a second filter. The outlet of the first filter is connected to the inlet of the milk hydration tank-premixing tank. The outlet of the milk hydration tank-premixing tank is sequentially connected to the discharge pump, the magnetic filter, and the second filter. The second filter is connected to the inlet of the balance tank.
[0018] The multifunctional low-acid beverage blending system further includes a plate heat exchanger in the auxiliary functional component pretreatment production unit, which is disposed between the first filter and the milk hydration tank-premixing tank.
[0019] The multifunctional low-acid beverage preparation system includes a first centrifugal pump and a first rotor pump connected in parallel between the first filter and the plate heat exchanger.
[0020] The multifunctional low-acid beverage preparation system, wherein the cooking production unit includes: an emulsifying high-shear mixing tank, a first filter, a first rotor pump, a plate heat exchanger, a milk hydration tank-premixing tank, a discharge pump, a first tubular heat exchanger, a magnetic filter, a second filter, the balance tank, a second centrifugal pump, a second rotor pump, a second tubular heat exchanger, the homogenizer, and the final preparation tank.
[0021] The emulsifying high-shear mixing tank is connected to the oil-sauce-like material feed pipeline. The outlet of the emulsifying high-shear mixing tank is sequentially connected to a first filter, a first rotor pump, a plate heat exchanger, a milk hydration tank-premixing tank, a discharge pump, a magnetic filter, a second filter, a balance tank, a second tubular heat exchanger, a homogenizer, and a final mixing tank.
[0022] The multifunctional low-acid beverage preparation system, wherein the mixing-homogenization-emulsification-standardization production unit includes the main component pretreatment production unit, the auxiliary functional component pretreatment production unit, and the cooking production unit.
[0023] In summary, the beneficial effects of this utility model are as follows: This utility model proposes a multifunctional low-acid beverage preparation system capable of producing low-acid ready-to-drink beverages and catering products, while improving production efficiency and product consistency. The system integrates multiple functional units and can handle various raw materials and processing steps, including dissolution, hydration, enzymatic hydrolysis, gelatinization, emulsification, homogenization, and standardization, thereby reducing operational complexity and improving product quality. Attached Figure Description
[0024] The above and / or additional aspects and advantages of this utility model will become apparent and readily understood from the description of the embodiments taken in conjunction with the following drawings, in which:
[0025] Figure 1 This is a schematic diagram of the multifunctional low-acid beverage preparation system according to the present invention. Detailed Implementation
[0026] To better understand the above-mentioned objectives, features, and advantages of this utility model, the present utility model will be further described in detail below with reference to the accompanying drawings and specific embodiments. It should be noted that, unless otherwise specified, features of the same embodiments and different embodiments of this application can be combined with each other.
[0027] Many specific details are set forth in the following description in order to provide a full understanding of the present invention. However, the present invention may also be implemented in other ways different from those described herein. Therefore, the scope of protection of the present invention is not limited to the specific embodiments disclosed below.
[0028] First, such as Figure 1 The diagram shown is a structural schematic of the multifunctional low-acid beverage preparation system of this invention. The multifunctional low-acid beverage preparation system mainly includes: a main component pretreatment production unit 100, an auxiliary functional component pretreatment production unit 200, a cooking production unit 300, and a mixing-homogenizing-emulsifying-standardizing production unit 400. The main component pretreatment production unit, auxiliary functional component pretreatment production unit, cooking production unit, and mixing-homogenizing-emulsifying-standardizing production unit contain shared functional components, such as a balance tank, a second tubular heat exchanger, a homogenizer, and a final preparation tank connected in sequence, which significantly reduces the system's footprint and energy consumption. The specific structure of the multifunctional low-acid beverage preparation system of this invention will be described in detail below.
[0029] Main component pretreatment production unit 100
[0030] The main component pretreatment production unit 100 mainly includes: a side hopper 1, an oil-sauce-like material feed line 2, a vacuum high-shear mixer 3, a feed pump 4, a milk hydration tank-premixing tank 5, a discharge pump 6, a first tubular heat exchanger 7, a magnetic filter 8, a second filter 18, a balance tank 15, a second centrifugal pump 16, a second rotor pump 17, a second tubular heat exchanger 19, a homogenizer 20, and a final blending tank 21.
[0031] The inlet (upstream) of the vacuum high-shear mixer 3 is connected to a side hopper 1 and an oil-saucelet material feed line 2. The side hopper is used to provide raw materials to the vacuum high-shear mixer 3, and the oil-saucelet material feed line 2 is used to add oil and / or sauce-like materials to the vacuum high-shear mixer 3. The outlet (downstream) of the vacuum high-shear mixer 3 is connected to the inlet of the milk hydration tank-premix tank 5, and a feed pump 4 is installed on the pipeline between the vacuum high-shear mixer 3 and the milk hydration tank-premix tank 5. The feed pump 4 transports the raw materials and auxiliary materials (oil and / or sauce-like materials) from the vacuum high-shear mixer 3 to the milk hydration tank-premix tank 5, which also functions as a rehydration tank for the raw materials and other auxiliary materials, as well as a mixing tank.
[0032] A discharge pump 6 is installed on the outlet pipe of the milk hydration tank-premix tank 5. Preferably, a first tubular heat exchanger 7 is connected in parallel between the inlet of the milk hydration tank-premix tank 5 and the outlet of the discharge pump 6, so that the mixture conveyed from the discharge pump 6 can enter the first tubular heat exchanger 7, and the heated mixture can re-enter the milk hydration tank-premix tank 5, or directly enter the vacuum high-shear mixer 3, and then the mixture is again conveyed to the milk hydration tank-premix tank 5 by the feed pump 4, and this cycle continues until the mixture is heated to the required temperature.
[0033] The outlet of the milk hydration tank-premixing tank 5 is sequentially connected to a discharge pump 6, a magnetic filter 8, a second filter 18, a balance tank 15, a second centrifugal pump 16, a second rotor pump 17, a second tubular heat exchanger 19, a homogenizer 20, and a final mixing tank 21. The mixture output from the milk hydration tank-premixing tank 5 is transported at high speed in the pipeline by means of the discharge pump 6. When the mixture enters the magnetic filter 8, metal contaminants in the mixture are filtered out. Then the mixture enters the first filter 18 to filter out impurities, thereby ensuring the purity of the mixture. Finally, it enters the balance tank 15 to ensure the consistency of the mixture flow rate.
[0034] A second centrifugal pump 16 and a second rotary pump 17 are connected in parallel between the balance tank 15 and the second tubular heat exchanger 19. The mixture in the balance tank 15 can be transported to the second tubular heat exchanger 19 by either the second centrifugal pump 16 or the second rotary pump 17. It should be noted that the second centrifugal pump 16 is suitable for transporting fluids that have already been uniformly mixed, while the second rotary pump 17 is suitable for further mixing the mixture while transporting it to ensure thorough mixing. In other words, the centrifugal pump is suitable for transporting low-viscosity fluids, while the rotary pump is suitable for transporting high-viscosity fluids.
[0035] After passing through the second tubular heat exchanger 19, the mixture will enter the homogenizer 20, which is used to achieve uniform dispersion of particles / materials in the mixture, and finally enter the final mixing tank 21 to make the final mixture before the sterilization process, or the mixture required for the next process.
[0036] The main component pretreatment production unit 100 is applicable to production processes such as coffee / tea powder dissolution, milk powder rehydration, lactose hydrolysis, oat flour dissolution, gelatinization, and basic emulsification, but is not limited thereto.
[0037] 200 auxiliary functional ingredient pretreatment production units
[0038] The auxiliary functional component pretreatment production unit 200 mainly includes: an oil-sauce-like material feed line 2, an emulsifying high-shear mixing tank 9, a small material dissolving tank 10, a first filter 11, a first centrifugal pump 12, a first rotor pump 13, a plate heat exchanger 14, a milk hydration tank-premixing tank 5, a discharge pump 6, a first tubular heat exchanger 7, a magnetic filter 8, a second filter 18, a balance tank 15, a second centrifugal pump 16, a second rotor pump 17, a second tubular heat exchanger 19, a homogenizer 20, and a final blending tank 21.
[0039] The emulsifying high-shear mixing tank 9 is connected to the oil-saucement feed line 2 and is supplied by the oil-saucement feed line 2. Both the emulsifying high-shear mixing tank 9 and the small-particle dissolving tank 10 are connected to the inlet of the first filter 11. The outlet 11 of the first filter is connected to the inlet of the plate heat exchanger 14, the inlet of the milk hydration tank-premixing tank 5, and the inlet of the balance tank 15, respectively. After thorough mixing in the emulsifying high-shear mixing tank 9, the mixture can be selectively transported to the plate heat exchanger 14 along with the salt or sugar in the small-particle dissolving tank 10 through the first filter 11. A first centrifugal pump 12 and a first rotor pump 13 are connected in parallel between the first filter 11 and the plate heat exchanger 14, and the mixture can be transported by either the first centrifugal pump 12 or the first rotor pump 13 depending on its condition. The plate heat exchanger 14 cools the mixture.
[0040] In a preferred embodiment, the outlets of the first centrifugal pump 12 and the first rotor pump 13 can also be directly connected to the milk hydration tank-premixing tank 5 via pipelines, so that the mixture output from the emulsification high-shear mixing tank 9 and the small-particle dissolving tank 10 can directly enter the milk hydration tank-premixing tank 5 through the first centrifugal pump 12 or the first rotor pump 13 without passing through the plate heat exchanger 14.
[0041] The pipeline connected to the outlet of the milk hydration tank-premix tank 5 directly adopts a part of the pipeline of the emulsification production unit 100. Therefore, the mixture will pass through the discharge pump 6, magnetic filter 8, second filter 18, balance tank 15, second tubular heat exchanger 19 and homogenizer 20 in sequence, and finally enter the final mixing tank 21 to make the final mixture before the sterilization process, or the mixture required for the next process.
[0042] In another preferred embodiment, the mixture output from the emulsifying high-shear mixing tank 9 and the small-particle dissolving tank 10, if it does not require cooling, rehydration and mixing, can be directly delivered to the balancing tank 15 without passing through the plate heat exchanger 14 or the milk hydration tank-premixing tank 5, in order to simplify the process steps.
[0043] The pipeline downstream of the balance tank 15 directly adopts a part of the pipeline of the main component pretreatment production unit 100. Therefore, the mixture will pass through the second tubular heat exchanger 19 and the homogenizer 20 in sequence, and finally enter the final blending tank 21 to make the final mixture before sterilization, or the mixture required for the next process.
[0044] The auxiliary functional component pretreatment production unit 200 is applicable to production processes such as stabilizer hydration, emulsification, and dissolution of materials such as sugar and salt, but is not limited thereto.
[0045] 300 cooking production units
[0046] The cooking production unit 300 includes: an emulsifying high-shear mixing tank 9, a first filter 11, a first rotor pump 13, a plate heat exchanger 14, a milk hydration tank-premixing tank 5, a discharge pump 6, a first tubular heat exchanger 7, a magnetic filter 8, a balancing tank 15, a second centrifugal pump 16, a second rotor pump 17, a second filter 18, a second tubular heat exchanger 19, a homogenizer 20, and a final blending tank 21.
[0047] The emulsifying high-shear mixing tank 9 is connected to the oil-saucement material feed line 2 and is fed by the oil-saucement material feed line 2. The outlet of the emulsifying high-shear mixing tank 9 is sequentially connected to a first filter 11, a first rotor pump 13, a plate heat exchanger 14, and a milk hydration tank-premixing tank 5. The mixture output from the emulsifying high-shear mixing tank 9 is first filtered by the first filter 11, then pumped by the first rotor pump 13 to the plate heat exchanger 14, cooled by the plate heat exchanger 14, and then enters the milk hydration tank-premixing tank 5.
[0048] In other words, the cooking production unit 300 actually uses a part of the auxiliary functional component pretreatment production unit 200, mainly by omitting the first centrifugal pump 12.
[0049] The pipeline downstream of the milk hydration tank-premixing tank 5 directly adopts a part of the pipeline of the main component pretreatment production unit 100. Therefore, the mixture will pass through the discharge pump 6, magnetic filter 8, second filter 18, balance tank 15, second tubular heat exchanger 19 and homogenizer 20 in sequence, and finally enter the final blending tank 21 to make the final mixture before sterilization, or the mixture required for the next process.
[0050] The cooking production unit 300 is applicable to, but not limited to, the production process of cocoa hydration, cooking, cooling and conveying.
[0051] 400 Mixing-Homogenetic-Emulsifying-Standardized Production Units
[0052] The mixing-homogenizing-emulsifying-standardizing production unit 400 includes: a side hopper 1, an oil-saucement material feed line 2, a vacuum high-shear mixer 3, a feed pump 4, a milk hydration tank-premixing tank 5, a discharge pump 6, a first tubular heat exchanger 7, a magnetic filter 8, an emulsifying high-shear mixing tank 9, a small material dissolving tank 10, a first filter 11, a first centrifugal pump 12, a first rotor pump 13, a plate heat exchanger 14, a balance tank 15, a centrifugal pump 16, a second rotor pump 17, a second filter 18, a second tubular heat exchanger 19, a homogenizer 20, and a final mixing tank 21.
[0053] The mixing-homogenizing-emulsifying-standardizing production unit 400 is basically a simplified combination of the main component pretreatment production unit 100, the auxiliary functional component pretreatment production unit 200, and the cooking production unit 300. By sharing multiple functional components, the overall equipment is simplified, and the integrated design significantly reduces the system's footprint and energy consumption.
[0054] The mixing-homogenizing-emulsifying-standardizing production unit 400 can achieve the transfer of milk base and / or plant base through the milk hydration tank-premixing tank 5, the discharge pump 6, the magnetic filter 8, and the second filter 18; it can achieve the delivery of cocoa base, stabilizer, salt, or sugar through the emulsifying high-shear mixing tank 9, the small-particle dissolving tank 10, the first filter 11, the first centrifugal pump 12, and the first rotor pump 13; it can achieve the mixing, preheating, homogenization, and emulsification of the mixture through the balance tank 15, the second centrifugal pump 16, the second rotor pump 17, the second tubular heat exchanger 19, and the homogenizer 20; and it can achieve the standardized production of the final product through the final blending tank 21.
[0055] In summary, the beneficial effects of this utility model are as follows: This utility model proposes a multifunctional low-acid beverage preparation system capable of producing low-acid ready-to-drink beverages and catering products, while improving production efficiency and product consistency. The system integrates multiple functional units and can handle various raw materials and processing steps, including dissolution, hydration, enzymatic hydrolysis, gelatinization, emulsification, homogenization, and standardization, thereby reducing operational complexity and improving product quality.
[0056] In the description of this utility model, the term "multiple" refers to two or more. Unless otherwise explicitly defined, the terms "upper," "lower," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings, and are only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of this utility model. The terms "connection," "installation," "fixing," etc., should be interpreted broadly. For example, "connection" can be a fixed connection, a detachable connection, or an integral connection; it can be a direct connection or an indirect connection through an intermediate medium. For those skilled in the art, the specific meaning of the above terms in this utility model can be understood according to the specific circumstances.
[0057] In the description of this specification, the terms "one embodiment," "some embodiments," "specific embodiment," etc., refer to a specific feature, structure, material, or characteristic described in connection with that embodiment or example, which is included in at least one embodiment or example of the present invention. In this specification, the illustrative expressions of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials, or characteristics described may be combined in any suitable manner in one or more embodiments or examples.
[0058] The above are merely preferred embodiments of this utility model and are not intended to limit the scope of this utility model. Various modifications and variations can be made to this utility model by those skilled in the art. Any modifications, equivalent substitutions, or improvements made within the spirit and principles of this utility model should be included within the protection scope of this utility model.
Claims
1. A multi-functional low-acid beverage dispensing system, characterized by, include: The main component pretreatment production unit (100), auxiliary functional component pretreatment production unit (200), cooking production unit (300) and mixing-homogenizing-emulsifying-standardizing production unit (400) include a common and sequentially connected balance tank (15), a second tubular heat exchanger (19), a homogenizer (20) and a final blending tank (21).
2. The multi-functional low-acid beverage dispensing system of claim 1, wherein, The main component pretreatment production unit (100) includes: a side hopper (1), an oil-saucement material feed line (2), a vacuum high-shear mixer (3), a feed pump (4), a milk hydration tank-premixing tank (5), a discharge pump (6), a magnetic filter (8), a second filter (18), the balance tank (15), the second tubular heat exchanger (19), the homogenizer (20), and the final blending tank (21). The vacuum high shear mixer (3) is connected to a side hopper (1) and an oil-sauce-like material feed line (2) at its inlet. The vacuum high shear mixer (3) is connected to the inlet of a milk hydration tank-premix tank (5). The outlet of the milk hydration tank-premix tank is connected in sequence to a discharge pump (6), a magnetic filter (8), a second filter (18), a balance tank (15), a second tubular heat exchanger (19), a homogenizer (20), and a final mixing tank (21).
3. The multi-functional low-acid beverage dispensing system of claim 2, wherein, A first tubular heat exchanger (7) is provided in parallel between the inlet of the milk hydration tank-premix tank (5) and the outlet of the discharge pump (6). The outlet of the first tubular heat exchanger (7) is also connected to the inlet of the vacuum high shear mixer (3).
4. The multi-functional low-acid beverage dispensing system of claim 2, wherein, A second centrifugal pump (16) and a second rotor pump (17) are connected in parallel between the balance tank (15) and the second tubular heat exchanger (19).
5. The multi-functional low-acid beverage dispensing system of claim 1, wherein, The auxiliary functional component pretreatment production unit (200) includes: an oil-saucement material feed line (2), an emulsifying high-shear mixing tank (9), a small-particle dissolving tank (10), a first filter (11), a first rotor pump (13), the balance tank (15), the second tubular heat exchanger (19), the homogenizer (20), and the final blending tank (21). The emulsifying high-shear mixing tank (9) is connected to the oil-sauce-like material feed line (2), and the emulsifying high-shear mixing tank (9) and the small material dissolving tank (10) are both connected to the inlet of the first filter (11). The outlet of the first filter (11) is connected to the inlet of the balance tank (15). The outlet of the balance tank (15) is sequentially connected to the second tubular heat exchanger (19), the homogenizer (20), and the final mixing tank (21).
6. The multi-functional low-acid beverage dispensing system of claim 5, wherein, The auxiliary functional component pretreatment production unit (200) further includes a milk hydration tank-premixing tank (5), a discharge pump (6), a magnetic filter (8), and a second filter (18). The outlet of the first filter (11) is connected to the inlet of the milk hydration tank-premixing tank (5). The outlet of the milk hydration tank-premixing tank (5) is sequentially connected to the discharge pump (6), the magnetic filter (8), and the second filter (18). The second filter (18) is connected to the inlet of the balance tank (15).
7. The multi-functional low-acid beverage dispensing system of claim 6, wherein, The auxiliary functional component pretreatment production unit (200) also includes a plate heat exchanger (14), which is disposed between the first filter (11) and the milk hydration tank-premixing tank (5).
8. The multi-functional low-acid beverage dispensing system of claim 7, wherein, A first centrifugal pump (12) and a first rotor pump (13) are connected in parallel between the first filter (11) and the plate heat exchanger (14).
9. The multi-functional low-acid beverage dispensing system of claim 1, wherein, The cooking production unit (300) includes: an emulsifying high-shear mixing tank (9), a first filter (11), a first rotor pump (13), a plate heat exchanger (14), a milk hydration tank-premixing tank (5), a discharge pump (6), a first tubular heat exchanger (7), a magnetic filter (8), a second filter (18), the balance tank (15), a second centrifugal pump (16), a second rotor pump (17), a second tubular heat exchanger (19), a homogenizer (20), and a final blending tank (21). The emulsifying high-shear mixing tank (9) is connected to the oil-sauce-like material feed line (2). The outlet of the emulsifying high-shear mixing tank (9) is sequentially connected to a first filter (11), a first rotor pump (13), a plate heat exchanger (14), a milk hydration tank-premixing tank (5), a discharge pump (6), a magnetic filter (8), a second filter (18), a balance tank (15), a second tubular heat exchanger (19), a homogenizer (20), and a final mixing tank (21).
10. The multi-functional low-acid beverage dispensing system of any one of claims 1-9, wherein, The mixing-homogenizing-emulsifying-standardizing production unit (400) includes the main component pretreatment production unit (100), the auxiliary functional component pretreatment production unit (200), and the cooking production unit (300).