Liquid multi-material reaction system

Abstract

The invention relates to a liquid multi-material reaction system, which comprises a first material stirring kettle, a second material stirring kettle, a reaction kettle, an emulsifying device and a finished product kettle, the first material stirring kettle and the second material stirring kettle are respectively connected with the reaction kettle, the reaction kettle and the emulsifying device are respectively connected with the finished product kettle, and the finished product kettle is connected with the emulsifying device. The first material stirring kettle is filled with a first material and is used for stirring the first material during working, and the second material stirring kettle is filled with a second material and is used for stirring the second material during working; when the reaction kettle works, a first material injected from the first material stirring kettle and a second material injected from the second material stirring kettle are stirred and reacted to form a first intermediate product. By arranging the first material stirring kettle, the second material stirring kettle, the reaction kettle, the emulsifying device and the finished product kettle, a safe and efficient production system is provided for brine reaction; and the air pressure sensor and the suction mechanism are arranged, so that furnace explosion is avoided.

Description

Technical Field

[0001] This application relates to the technical field of material reaction kettles, and particularly to a liquid multi-material reaction system. Background Art

[0002] A brine reaction kettle is a device specifically designed for processing and treating brine (an aqueous solution containing a high concentration of salts), and it has a wide range of applications in multiple industries.

[0003] At present, some brine reaction systems on the market are relatively imperfect and cannot produce the required products efficiently and safely.

[0004] Therefore, there are defects in the existing technology and improvements are needed. Summary of the Invention

[0005] This application provides a liquid multi-material reaction system to solve the problem that some brine reaction systems on the market are relatively imperfect and cannot produce the required products efficiently and safely.

[0006] In a first aspect, this application provides a liquid multi-material reaction system, including a first material stirring kettle, a second material stirring kettle, a reaction kettle, an emulsifying device, and a finished product kettle. The first material stirring kettle and the second material stirring kettle are respectively connected to the reaction kettle, and the reaction kettle and the emulsifying device are respectively connected to the finished product kettle. The first material stirring kettle contains a first material and stirs the first material during operation. The second material stirring kettle contains a second material and stirs the second material during operation. The reaction kettle stirs and reacts the first material injected from the first material stirring kettle and the second material injected from the second material stirring kettle during operation to form a first intermediate product. The emulsifying device contains a third material and stirs and performs an emulsification reaction on the third material during operation to form a second intermediate product. The finished product kettle contains a fourth material and stirs and reacts the injected first intermediate product, second intermediate product, and fourth material during operation to form a final product.

[0007] Optionally, a pressure sensor is provided on the reaction kettle, and the pressure sensor is used to detect the air pressure inside the reaction kettle.

[0008] Optionally, a longitudinal stirring tube is provided in the axial direction inside the reaction kettle, and the longitudinal stirring tube is connected to a liquid cooling mechanism outside the reaction kettle.

[0009] Optionally, a suction mechanism is further provided on the reaction kettle. The suction mechanism is connected to the reaction kettle. A pressure threshold is set inside the pressure sensor. The pressure sensor obtains the air pressure value inside the reaction kettle and compares the pressure value with the pressure threshold. When the pressure value is greater than the pressure threshold, the pressure sensor controls the suction mechanism to perform a gas pumping operation on the inside of the reaction kettle.

[0010] Optionally, the longitudinal stirring tube is integrally in the shape of a Chinese character 'Mu'.

[0011] Optionally, a heat preservation layer is provided between the inner wall and the outer wall of the reaction kettle.

[0012] Optionally, a heat preservation cavity is arranged in the heat preservation layer, and the heat preservation cavity is connected with a liquid supply module for supplying liquid to the heat preservation cavity.

[0013] Optionally, the liquid multi-material reaction system further includes a waterway cleaning module connected to the reaction kettle, and the waterway cleaning module cleans the reaction kettle by supplying high-pressure water into the reaction kettle and discharging it.

[0014] Optionally, the waterway cleaning module includes a water supply module and a liquid recovery module. The water supply module is connected to the top end of the reaction kettle, and the liquid recovery module is connected to the bottom end of the reaction kettle.

[0015] Optionally, a ring-shaped stirring tube is further connected to the bottom of the longitudinal stirring tube, and the longitudinal stirring tube is communicated with the ring-shaped stirring tube.

[0016] The above technical solutions provided by the embodiments of the present application have the following advantages compared with the prior art:

[0017] By providing the first material stirring kettle, the second material stirring kettle, the reaction kettle, the emulsifying device and the finished product kettle, the embodiments of the present application provide a safe and efficient production system for the brine reaction; by providing the air pressure sensor and the suction mechanism, it is beneficial to control the reaction in the reaction kettle under normal pressure, which is beneficial to avoiding explosion of the furnace. Description of the Drawings

[0018] The accompanying drawings herein are incorporated into the specification and constitute a part of the specification, showing embodiments consistent with the present application and used together with the specification to explain the principles of the present application.

[0019] In order to more clearly illustrate the technical solutions in the embodiments of the present application or the prior art, the following will briefly introduce the drawings required for use in the description of the embodiments or the prior art. Obviously, for those of ordinary skill in the art, other drawings can also be obtained based on these drawings without creative efforts.

[0020] One or more embodiments are exemplified by the pictures in the corresponding accompanying drawings. These exemplary descriptions do not constitute limitations on the embodiments. Elements with the same reference numerals in the drawings represent similar elements. Unless otherwise stated, the drawings in the drawings do not constitute a proportional limitation.

[0021] Figure 1Schematic diagrams of the first material stirring kettle, the second material stirring kettle, the reaction kettle, the emulsifying device, and the finished product kettle provided by the embodiments of the present application.

[0022] Figure 2 Schematic diagrams of the air pressure sensor, the suction mechanism, and a part of the reaction kettle provided by the embodiments of the present application.

[0023] Figure 3 Schematic diagram of the cleaning module provided by the embodiments of the present application.

[0024] Figure 4 Partial three-dimensional structure diagram of the liquid multi-material reaction system provided by the embodiments of the present application.

[0025] Figure 5 For Figure 4 Cross-sectional view.

[0026] Figure 6 Three-dimensional diagram of the heat exchanger provided by the embodiments of the present application.

[0027] Figure 7 Schematic diagrams of the liquid supply module and the heat exchanger provided by the embodiments of the present application.

[0028] Figure 8 Three-dimensional diagrams of the longitudinal stirring tube, the annular stirring tube, the bottom scraping structure, and the shearing structure provided by the embodiments of the present application.

[0029] Explanation of reference numerals:

[0030] 1. First material stirring kettle; 2. Second material stirring kettle; 3. Reaction kettle; 4. Emulsifying device; 5. Finished product kettle; 6. Air pressure sensor; 7. Suction mechanism; 8. Liquid recovery mechanism; 9. Condensation structure; 10. Liquid return pipeline; 11. Gas recovery pipeline; 12. Cleaning module; 13. Waterway cleaning module; 14. Gas path cleaning module; 15. Cleaning inlet; 16. Cleaning outlet; 17. Water supply module; 18. Liquid recovery module; 19. Gas supply module; 20. Gas recovery module; 21. Heat insulation layer; 23. Heat exchanger; 24. Liquid supply module; 25. Longitudinal stirring tube; 26. Annular stirring tube; 27. Bottom scraping structure; 28. Shearing structure; 29. Rate control module; 30. Low-temperature liquid module; 31. High-temperature liquid module. Detailed implementation manners

[0031] To make the objectives, technical solutions, and advantages of the embodiments of this application clearer, the following will clearly and completely describe the technical solutions in the embodiments of this application with reference to the accompanying drawings in the embodiments of this application. Obviously, the described embodiments are some, but not all, of the embodiments of this application. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of this application without creative efforts shall fall within the scope of protection of this application.

[0032] The following disclosure provides many different embodiments or examples for implementing different structures of this application. To simplify the disclosure of this application, components and settings of specific examples are described below. Of course, they are only examples and are not intended to limit this application. In addition, this application may repeat reference numerals and / or letters in different examples. This repetition is for the purpose of simplification and clarity and does not itself indicate the relationship between the various embodiments and / or settings discussed.

[0033] For ease of description, spatially relative relationship terms may be used in the text to describe the relative position relationship or movement of one element or feature shown in the figure relative to another element or feature. These relative relationship terms are, for example, "inside", "outside", "inner side", "outer side", "below", "beneath", "above", "over", "front", "rear", etc. Such spatially relative relationship terms are intended to include different orientations of the device in use or operation in addition to the orientation depicted in the figure. For example, if the device in the figure undergoes a position flip, attitude change, or motion state change, then these directional indications will also change accordingly. For example, an element described as "below" or "beneath" other elements or features will then be oriented as "above" or "over" other elements or features. Therefore, the exemplary term "below" can include both the upper and lower orientations. The device can be oriented otherwise (rotated 90 degrees or in other directions) and the spatially relative relationship descriptors used in the text are interpreted accordingly.

[0034] To solve the technical problems in the prior art, this application provides a liquid multi-material reaction system, which can provide a safe and efficient production system for brine reaction by setting up a first material stirring kettle, a second material stirring kettle, a reaction kettle, an emulsifying device, and a finished product kettle; by setting up a pressure sensor and a suction mechanism, it is beneficial to control the reaction in the reaction kettle under normal pressure and avoid furnace explosion.

[0035] Figure 1-8A liquid multi-material reaction system provided by an embodiment of the present application includes a first material stirring kettle 1, a second material stirring kettle 2, a reaction kettle 3, an emulsifying device 4 and a finished product kettle 5. The first material stirring kettle 1 and the second material stirring kettle 2 are respectively connected to the reaction kettle 3, and the reaction kettle 3 and the emulsifying device 4 are respectively connected to the finished product kettle 5. The first material stirring kettle 1 contains a first material and stirs the first material during operation. The second material stirring kettle 2 contains a second material and stirs the second material during operation. The reaction kettle 3 stirs and reacts the first material injected from the first material stirring kettle 1 and the second material injected from the second material stirring kettle 2 during operation to form a first intermediate product. The emulsifying device 4 contains a third material and stirs and emulsifies the third material during operation to form a second intermediate product. The finished product kettle 5 contains a fourth material and stirs and reacts the injected first intermediate product, second intermediate product and fourth material during operation to form a final product. The first material stirring kettle 1, the second material stirring kettle 2, the emulsifying device 4 and the finished product kettle 5 can be fed separately, avoiding the premature mixing and reaction of materials caused by feeding to one place, generating a large amount of gas resulting in an increase in air pressure and potential safety hazards, providing a safe and efficient production system for the brine reaction; the final product is discharged through the discharge port of the finished product kettle 5. The liquid materials in the present application are brine, including but not limited to this, and the specific products can be determined according to the actual situation.

[0036] Please refer to Figure 2 , a pressure sensor 6 and a suction mechanism 7 are provided on the reaction kettle 3. The pressure sensor 6 is used to detect the air pressure in the reaction kettle 3. The suction mechanism 7 is connected to the reaction kettle 3. A pressure threshold is set in the pressure sensor 6. The pressure sensor 6 obtains the air pressure value in the reaction kettle 3 and compares the air pressure value with the pressure threshold. When the air pressure value is greater than the pressure threshold, the pressure sensor 6 controls the suction mechanism 7 to perform a gas extraction operation on the inside of the reaction kettle 3. The setting of the pressure sensor 6 and the suction mechanism 7 can control the air pressure in the reaction kettle 3 in real time, avoiding the situation of explosion due to excessive air pressure in the reaction kettle 3 and improving the safety factor; at the same time, the air pressure is also maintained within a preset range to promote the full reaction of the materials and reduce the generation of more foam. Preferably, the suction mechanism 7 is a structure of an air extraction pump, including but not limited to this, and other structures for air extraction can also be used; further preferably, the suction mechanism 7 is connected to the top of the reaction kettle 3. In this way, when the suction mechanism 7 performs a gas extraction operation, it is more likely to extract the gas in the reaction kettle 3 rather than liquids such as materials, effectively achieving pressure reduction while not causing waste of materials due to the extraction of a large amount of liquid.

[0037] Please continue to refer to Figure 2, the liquid multi-material reaction system of the present application further includes a liquid recovery mechanism 8, and the liquid recovery mechanism 8 is connected to the suction mechanism 7 for recovering liquid small molecules drawn out with the gas. By setting the liquid recovery mechanism 8, the liquid small molecules drawn away by the suction mechanism 7 can flow back into the reaction kettle 3, avoiding the loss and waste of materials and improving the utilization efficiency of materials. Further, the liquid recovery mechanism 8 includes a condensation structure 9, a liquid return pipeline 10 and a gas recovery pipeline 11. The condensation structure 9 is connected to the suction mechanism 7. One end of the liquid return pipeline 10 and one end of the gas recovery pipeline 11 are respectively connected to the condensation structure 9. The other end of the liquid return pipeline 10 is connected to the reaction kettle 3. The liquid small molecules are condensed into larger liquid beads through the condensation structure 9 and flow back into the reaction kettle 3 through the liquid return pipeline 10, and the gas is transmitted to the external processing device through the gas recovery pipeline 11.

[0038] Please continue to refer to Figure 3 , the liquid multi-material reaction system of the present application further includes a cleaning module 12, and the cleaning module 12 is connected to the reaction kettle 3 for supplying high-pressure water or high-pressure gas into the reaction kettle 3 and discharging to clean the reaction kettle 3. The setting of the cleaning module 12 realizes high-intensity flushing inside the reaction kettle 3 to flush out the condensed and precipitated brine substances and other impurities, realizing the cleaning of the reaction kettle 3. Further, the cleaning module 12 includes a waterway cleaning module 13 and an airway cleaning module 14. The waterway cleaning module 13 and the airway cleaning module 14 are respectively connected to the reaction kettle 3. The waterway cleaning module 13 is used for supplying high-pressure water into the reaction kettle 3 and discharging to clean the reaction kettle 3, and the airway cleaning module 14 is used for supplying high-pressure gas into the reaction kettle 3 and discharging to clean the reaction kettle 3. It can be understood that the gas and water provided by the cleaning module 12 are both food-grade.

[0039] Please refer to Figure 4 , the cleaning module 12 includes a cleaning inlet 15 and a cleaning outlet 16. The cleaning inlet 15 is connected to the top of the reaction kettle 3, and the cleaning outlet 16 is connected to the bottom of the reaction kettle 3. The cleaning inlet 15 is arranged at the top of the reaction kettle 3, which can make the high-pressure gas or high-pressure water enter smoothly and is not easily blocked by the materials, and at the same time, there is no possibility of material backflow and damage to the cleaning module 12. Among them, the waterway cleaning module 13 includes a water supply module 17 and a liquid recovery module 18. The water supply module 17 is connected to the cleaning inlet 15, and the liquid recovery module 18 is connected to the cleaning outlet 16. The airway cleaning module 14 includes a gas supply module 19 and a gas recovery module 20. The gas supply module 19 is connected to the cleaning inlet 15, and the gas recovery module 20 is connected to the cleaning outlet 16. That is, the waterway cleaning module 13 and the airway cleaning module 14 share the cleaning inlet 15 and the cleaning outlet 16, avoiding the possibility of leakage of the reaction kettle 3 caused by setting too many pipelines.

[0040] Please refer toFigures 5-7 A heat-insulating layer 21 is provided between the inner wall and the outer wall of the reaction kettle 3. A heat-insulating cavity is arranged inside the heat-insulating layer 21. The heat-insulating cavity is connected with a heat exchanger 23, and the heat exchanger 23 is connected with a liquid supply module 24. The liquid supply module 24 is used to supply low-temperature water and / or high-temperature water to the heat exchanger 23. The heat exchanger 23 is used to inject the low-temperature water or high-temperature water provided by the liquid supply module 24 into the heat-insulating cavity, or to mix and exchange heat the simultaneously provided low-temperature water and high-temperature water and then inject them into the heat-insulating cavity, so that the injected water conforms to the reaction temperature of the material at the inner wall of the reaction kettle 3, thereby improving the reaction efficiency. Specifically, the liquid supply module 24 includes a low-temperature liquid module 30 and a high-temperature liquid module 31. The low-temperature liquid module 30 and the high-temperature liquid module 31 are respectively connected with the heat exchanger 23. The low-temperature liquid module 30 is used to provide low-temperature liquid, and the high-temperature liquid module 31 is used to provide high-temperature liquid. By providing high-temperature liquid or low-temperature liquid or mixing the two to supply to the heat-insulating cavity, it is avoided that only providing high-temperature liquid or low-temperature liquid cannot meet the temperature requirements of the material on the inner wall of the reaction kettle 3. By providing the heat-insulating layer 21 between the inner wall and the outer wall of the reaction kettle 3, and injecting water meeting the reaction required temperature into the heat-insulating cavity through the cooperation of the liquid supply module 24 and the heat exchanger 23, it is beneficial to promote the full reaction of the material located at the inner wall, and is beneficial to improving the overall reaction efficiency.

[0041] Please refer to Figure 8 Inside the reaction kettle 3, a longitudinal stirring tube 25, an annular stirring tube 26, a bottom scraping structure 27 and a shearing structure 28 which are integrally in a "mesh" shape are arranged. The longitudinal stirring tube 25 is arranged along the axial direction of the reaction kettle 3. The annular stirring tube 26 is connected to the bottom of the longitudinal stirring tube 25. The bottom scraping structure 27 is arranged at the bottom of the longitudinal stirring tube 25 and is connected with the annular stirring tube 26. The shearing structure 28 is connected to the side of the longitudinal stirring tube 25. The annular stirring tube 26 is used to drive the bottom scraping structure 27 to rotate while providing a certain stirring function. The bottom scraping structure 27 is used to scrape off the materials adhered to the bottom of the reaction kettle 3 when moving along with the longitudinal stirring tube 25. The shearing structure 28 is used to shear large pieces of materials when moving along with the longitudinal stirring tube 25. By arranging the longitudinal stirring tube 25, the reaction rate is accelerated and the reaction quality is improved; the arrangement of the bottom scraping structure 27 can scrape off the materials at the bottom of the reaction kettle 3, avoiding adhesion and residue and affecting the utilization rate of the materials; the arrangement of the shearing structure 28 can shear most of the larger reactants in the reaction kettle 3, which is beneficial to improving the quality of the intermediate products. Preferably, the shearing structure 28 is in a disc shape, and a shearing knife extends outward from its outer peripheral side. Including but not limited to this, other structures of the shearing knife structure can also be selected, and specifically can be determined according to the properties of the larger reactants.

[0042] In the present application, the longitudinal stirring tube 25 has a tubular hollow structure, specifically a serpentine tube structure arranged longitudinally, which is connected to the annular stirring tube 26. At the same time, a liquid cooling mechanism (not shown in the figure) and a rate control module 29 are provided outside the reaction kettle 3, and the longitudinal stirring tube 25 and the annular stirring tube 26 are connected to the liquid cooling mechanism outside the reaction kettle 3. The longitudinal stirring tube 25 with a serpentine tube structure arranged longitudinally occupies a relatively large area size on the rotating surface, which can better achieve the stirring function. At the same time, the liquid cooling mechanism provides coolant to the longitudinal stirring tube 25 to realize the heat exchange between the longitudinal stirring tube and the reaction cavity, so that the temperature in the reaction kettle 3 can be maintained at the temperature required for the reaction, which is beneficial to promoting the full reaction of the materials and improving the reaction efficiency. The rate control module 29 is connected to the longitudinal stirring tube 25, and the rate control module 29 is used to control the rotation rate of the longitudinal stirring tube 25.

[0043] In the above embodiments, the descriptions of the respective embodiments have their own emphases. For the parts not described in detail in a certain embodiment, reference may be made to the relevant descriptions of other embodiments.

[0044] In the description of the present application, it should be understood that the orientation or positional relationship indicated by the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc. is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present application and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus should not be construed as a limitation to the present application.

[0045] In addition, the terms "first" and "second" are only used for descriptive purposes and cannot be understood as indicating or implying relative importance or implicitly specifying the quantity of the indicated technical features. Thus, the features defined with "first" and "second" may explicitly or implicitly include one or more of such features. In the description of the present application, the meaning of "a plurality" is two or more, unless otherwise specifically defined.

[0046] In the present application, unless otherwise clearly specified and limited, the terms "installed", "connected", "connected to", "fixed", etc. should be understood in a broad sense. For example, it may be a connection, a detachable connection, or integrated; it may be a mechanical connection or an electrical connection; it may be directly connected or indirectly connected through an intermediate medium, and it may be the internal communication of two elements or the interaction relationship between two elements. For those of ordinary skill in the art, the specific meanings of the above terms in the present application can be understood according to specific circumstances.

[0047] In this application, unless otherwise clearly specified and defined, the first feature being "on" or "under" the second feature may include direct contact between the first and second features, or may include contact between the first and second features not being direct but through additional features therebetween. Moreover, the first feature being "above", "over" and "on top of" the second feature includes the first feature being directly above and obliquely above the second feature, or merely indicating that the horizontal height of the first feature is higher than that of the second feature. The first feature being "under", "beneath" and "underneath" the second feature includes the first feature being directly below and obliquely below the second feature, or merely indicating that the horizontal height of the first feature is less than that of the second feature.

[0048] In the description of this specification, the description with reference to terms such as "one embodiment", "some embodiments", "example", "specific example", or "some examples", etc. means that the specific features, structures, materials or characteristics described in connection with the embodiment or example are included in at least one embodiment or example of this application. In this specification, the schematic representations of the above terms should not be understood as necessarily referring to the same embodiment or example. Moreover, the specific features, structures, materials or characteristics described can be combined in any one or more embodiments or examples in a suitable manner. In addition, those skilled in the art can combine and combine the different embodiments or examples described in this specification.

[0049] Obviously, those skilled in the art can make various changes and modifications to this application without departing from the spirit and scope of this application. Thus, provided that these modifications and variations of this application fall within the scope of the claims of this application and their equivalent technologies, this application is also intended to include these changes and modifications.

[0050] As described above, this is the specific implementation manner of this application, but the protection scope of this application is not limited thereto. Any person skilled in the art within the technical scope disclosed by this application can easily think of various equivalent modifications or substitutions, and these modifications or substitutions should all be covered by the protection scope of this application. Therefore, the protection scope of this application shall be subject to the protection scope of the claims.

Claims

1. A liquid multi-material reaction system, characterized in that: It includes a first material stirring kettle, a second material stirring kettle, a reaction kettle, an emulsifying device and a finished product kettle. The first material stirring kettle and the second material stirring kettle are respectively connected to the reaction kettle, and the reaction kettle and the emulsifying device are respectively connected to the finished product kettle. The first material stirring kettle contains a first material and stirs the first material during operation. The second material stirring kettle contains a second material and stirs the second material during operation. The reaction kettle stirs and reacts the first material injected from the first material stirring kettle and the second material injected from the second material stirring kettle during operation to form a first intermediate product. The emulsifying device contains a third material and stirs and performs an emulsification reaction on the third material during operation to form a second intermediate product. The finished product kettle contains a fourth material and stirs and reacts the injected first intermediate product, second intermediate product and fourth material during operation to form a final product.

2. The liquid multi-material reaction system according to claim 1, wherein: A pressure sensor is provided on the reaction kettle, and the pressure sensor is used to detect the air pressure inside the reaction kettle.

3. The liquid multi-material reaction system according to claim 1, characterized in that: A longitudinal stirring pipe is provided in the axial direction inside the reaction kettle, and the longitudinal stirring pipe is connected to a liquid cooling mechanism outside the reaction kettle.

4. The liquid multi-material reaction system according to claim 2, wherein: A suction mechanism is further provided on the reaction kettle. The suction mechanism is connected to the reaction kettle. A pressure threshold is set inside the pressure sensor. The pressure sensor obtains the air pressure value inside the reaction kettle and compares the air pressure value with the pressure threshold. When the air pressure value is greater than the pressure threshold, the pressure sensor controls the suction mechanism to perform a pumping operation on the inside of the reaction kettle.

5. The liquid multi-material reaction system according to claim 3, wherein: The longitudinal stirring pipe is integrally in the shape of the Chinese character "mu".

6. The liquid multi-material reaction system according to claim 1, characterized in that: A heat preservation layer is provided between the inner wall and the outer wall of the reaction kettle.

7. The liquid multi-material reaction system according to claim 6, characterized in that: A heat preservation cavity is provided inside the heat preservation layer, and the heat preservation cavity is connected to a liquid supply module, and the liquid supply module is used to supply liquid to the heat preservation cavity.

8. The liquid multi-material reaction system according to claim 1, wherein: The liquid multi-material reaction system further includes a waterway cleaning module. The waterway cleaning module is connected to the reaction kettle, and the waterway cleaning module cleans the reaction kettle by supplying a high-pressure water body into the reaction kettle for cleaning and discharging.

9. The liquid multi-material reaction system according to claim 8, wherein: The waterway cleaning module includes a water supply module and a liquid recovery module. The water supply module is connected to the top of the reaction kettle, and the liquid recovery module is connected to the bottom of the reaction kettle.

10. The liquid multi-material reaction system according to claim 3, characterized in that: A ring-shaped stirring pipe is further connected to the bottom of the longitudinal stirring pipe, and the longitudinal stirring pipe is communicated with the ring-shaped stirring pipe.

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