Static mixing batching and raw material conveying system

Abstract

The invention discloses a static mixing burdening and raw material conveying system which comprises a first material conveying processing module, a second material conveying processing module, a third material conveying processing module and a temperature control module, and the temperature control module comprises a cold and hot all-in-one machine and a heat exchanger. The heat exchanger is connected to the first material conveying processing module, the second material conveying processing module and the third material conveying processing module. The first material conveying and processing module is provided with a first static mixer, the second material conveying and processing module is provided with a second static mixer, and by introducing the static mixers, the system can realize efficient mixing without an external power source, so that the electric energy consumption is remarkably reduced; the static mixer is simple in structure and free of quick-wear parts, and compared with traditional stirring equipment, the static mixer is lower in maintenance cost and more simplified in maintenance process; the system adopts a modular design and comprises a plurality of material conveying and processing modules and a temperature control module, flexible configuration and expansion are facilitated, and the production efficiency is improved.

Description

Technical Field

[0001] The invention relates to the technical field related to material mixing, and in particular to a static mixing batching and raw material conveying system. Background Art

[0002] In the sponge material manufacturing industry, the uniformity of raw material mixing is critical to the performance and quality of the final product. Traditional sponge material mixing systems usually use stirring equipment, such as stirring paddles or stirrers, to drive fluid movement through mechanical force to achieve uniform mixing between different components. However, this mixing method has problems such as high energy consumption, complex equipment maintenance, limited mixing efficiency, and the possibility of introducing impurities. Summary of the invention

[0003] In order to overcome at least one of the defects of the prior art, the present invention provides a static mixing batching and raw material delivery system. The system can overcome the limitations of the traditional mixing system, utilize the flow energy of the fluid itself, and achieve efficient mixing effect without the need for an external power source. This system not only reduces power consumption and equipment costs, but also simplifies the equipment maintenance process and improves production efficiency.

[0004] The technical solution adopted by the present invention to solve the problem is:

[0005] A static mixing batching and raw material conveying system, comprising: a first material conveying processing module, the first material conveying processing module comprising a first storage tank, a first mixing tank, a first intermediate tank and a first foaming machine working tank connected in sequence; a second material conveying module, the second material conveying module comprising a second storage tank and a second mixing tank connected in sequence, the second mixing tank being communicated with the first intermediate tank; a third material conveying processing module, the third material conveying processing module comprising a third storage tank, a third intermediate tank and a third foaming machine working tank connected in sequence; a temperature control module, the temperature control module comprising a hot and cold all-in-one machine and a plurality of heat exchangers connected thereto, the heat exchangers being respectively connected to the first material conveying processing module, the second material conveying module and the third material conveying processing module, for controlling the mixing temperature; wherein a first static mixer is arranged between the first mixing tank and the first intermediate tank, and a second static mixer is arranged between the second mixing tank and the first intermediate tank.

[0006] By adopting the above solution and introducing a static mixer, the system can achieve efficient mixing without an external power source, thereby significantly reducing electricity consumption; the static mixer has a simple structure and no wearing parts, and its maintenance cost is lower and the maintenance process is simpler than traditional mixing equipment; the system adopts a modular design, including multiple material conveying and processing modules and temperature control modules, which facilitates flexible configuration and expansion, thereby improving production efficiency.

[0007] Furthermore, the first static mixer and the second static mixer both include: a shell, the shell including a dispersed phase inlet, a mixing channel and a dispersed phase outlet in sequence from one end to the other end; a first rotor, the first rotor is spirally wound clockwise in the mixing channel in the shell; a second rotor, the second rotor is spirally wound counterclockwise in the mixing channel in the shell; wherein the first rotor and the second rotor are alternately arranged along the mixing channel.

[0008] By adopting the above scheme, the fluid can be guided to undergo multiple divisions, rotations and reorganizations in the flow channel, thereby achieving an efficient mixing effect; the first rotor and the second rotor are alternately arranged along the mixing flow channel, which can further enhance the mixing effect and avoid the formation of dead zones or short circuits in the flow channel.

[0009] Furthermore, a plurality of flow holes are provided on the first rotating vane and the second rotating vane, and a guide channel is extended from the flow hole toward one end of the dispersed phase outlet.

[0010] By adopting the above scheme, the setting of multiple flow holes can ensure that the raw materials are evenly distributed between the rotors, avoiding local concentrations that are too high or too low; the guide channel is the part of the flow hole that extends to one end of the dispersed phase outlet. The flow hole and the guide channel together constitute the flow path of the fluid between the rotors. Part of the fluid will pass through the flow hole, and part of the fluid will be blocked and guided by the rotor, causing changes in direction and speed. The purpose is to guide the fluid to flow more complexly between the rotors, thereby improving the mixing efficiency.

[0011] Furthermore, the guide channel is provided with alternating left-hand spiral mixing sheets and right-hand spiral mixing sheets.

[0012] By adopting the above scheme, the fluid entering the guide channel from the flow hole can be divided, rotated and reorganized again, further improving the mixing effect, saving the total length of the mixing channel, and achieving a better mixing effect within a limited length.

[0013] Furthermore, staggered fins are provided in the guide channel, the fins penetrate the side wall of the guide channel, a sputtering hole is formed between the side of the fin facing the dispersed phase inlet and the side wall of the guide channel, and the sputtering hole is connected to the mixing channel.

[0014] By adopting the above scheme, the fins are arranged on the side wall of the guide channel to form a staggered structure. This design not only increases the complexity and surface area of ​​the guide channel, but also provides additional mixing opportunities. The sputtering holes allow the fluid to pass through the mixing channel and cause sputtering and collision, thereby further promoting mixing. The presence of the sputtering holes allows the fluid to enter the guide channel from the mixing channel under the guidance of the fins, and violent turbulence and mixing occur during the sputtering process. When the fluid passes through the sputtering holes, it will be hindered and guided by the fins, causing a change in direction and an increase in speed, thereby increasing the mutual collision and shear force between the fluids. This sputtering and collision effect helps to break up the clumps and stratification in the fluid, so that the fluid is more evenly distributed in the guide channel.

[0015] Furthermore, the first storage tank includes a first feeding port, a first feed inlet and a first discharge port, the first feeding port is connected to a first feed channel, and a first temperature control circuit is connected between the first feed inlet and the first discharge port; the second storage tank includes a second feeding port, a second feed inlet and a second discharge port, the second feeding port is connected to a second feed channel, and a second temperature control circuit is connected between the second feed inlet and the second discharge port.

[0016] By adopting the above scheme, the first feeding port is connected to the external device through the first feeding channel, and the second feeding port is connected to the external device through the second feeding channel for inputting raw materials into the storage tank. The first temperature control loop and the second temperature control loop are designed to control the temperature of the raw materials in the storage tank to ensure that they are kept within the appropriate temperature range during storage and transportation.

[0017] Furthermore, the first material delivery channel and the second material delivery channel both include a manual ball valve, a filter, a discharge pump, a safety overflow valve, a one-way valve, a pressure gauge and a pneumatic ball valve; the first temperature control circuit and the second temperature control circuit both include a filter, a material transfer pump, a safety overflow valve, a manual ball valve, a one-way valve, a pressure gauge, a heat exchange device and a mold temperature controller.

[0018] By adopting the above solution, the feed channel and temperature control circuit both include various equipment required for the complete process from raw material input to finished product output, ensuring the continuity and stability of the production process; the installation of safety devices such as safety relief valves and pressure gauges effectively reduces the risks that may occur in the production process; the combination of manual ball valves and pneumatic ball valves not only ensures rapid response capabilities in emergency situations, but also meets the needs of automated production lines; the reasonable selection and configuration of equipment such as filters and transfer pumps ensure the smooth flow of materials and temperature control media, and improve production efficiency.

[0019] Furthermore, the first mixing tank is provided with a first mixing outlet, the second mixing tank is provided with a second mixing outlet, a first feeding pipe is provided between the first mixing outlet and the first intermediate tank and the first foaming machine working tank, and the first static mixer is provided on the first feeding pipe; a second feeding pipe is provided between the second mixing outlet and the first intermediate tank and the first foaming machine working tank, and the second static mixer is provided on the second feeding pipe.

[0020] By adopting the above solution, through the design of two mixing tanks and one intermediate tank, the system can flexibly process a variety of materials to meet the production needs of different products; the use of static mixers significantly improves the mixing efficiency of materials and ensures the uniformity and stability of materials before foaming; the design of the entire system optimizes the process of material transmission and mixing, improves production efficiency and reduces production costs.

[0021] Furthermore, an auxiliary material replenishing pipeline is connected between the first mixing tank and the second mixing tank, and the auxiliary material replenishing pipeline includes a diaphragm pump and an auxiliary material tank.

[0022] By adopting the above solution, the design of the auxiliary material replenishment pipeline allows the system to flexibly adjust the type and amount of auxiliary materials according to production needs, thereby optimizing product performance; the use of diaphragm pumps reduces the risk of leakage and contamination, ensuring the safety and reliability of auxiliary material transportation.

[0023] Furthermore, the first storage tank, the first mixing tank, the second storage tank and the second mixing tank are all provided with electronic scales for weighing, and the first storage tank and the second storage tank are also provided with maximum liquid level indicators.

[0024] By adopting the above scheme, the main function of the electronic scale is to monitor and record the weight of the material in the storage tank or mixing tank in real time, which is essential for accurately controlling the material feeding amount, monitoring material consumption and ensuring product quality; the main function of the maximum liquid level indicator is to monitor the liquid level in the storage tank. When the liquid level reaches the preset maximum point, an alarm or signal will be issued to prevent material overflow or leakage; the design of the electronic scale and the maximum liquid level indicator emphasizes accuracy, ensuring accurate monitoring of material weight and liquid level. These devices are usually connected to the central control system to realize real-time data transmission and remote monitoring. This improves the automation and intelligence level of the system and reduces the difficulty and risk of manual operation.

[0025] In summary, the static mixing batching and raw material conveying system provided by the present invention has the following technical effects:

[0026] 1. By introducing a static mixer, the system uses the fluid's own flow energy to achieve efficient mixing without relying on external power sources such as a stirring paddle or agitator. This feature significantly reduces power consumption, making the entire production process more energy-efficient. The static mixer is divided into a first static mixer and a second static mixer, which can achieve secondary mixing and achieve more uniform mixing, avoiding problems such as local uneven concentration or material stratification that may be caused by traditional mixing equipment. This helps to improve the quality and consistency of the final product and meet more stringent quality control requirements;

[0027] 2. The static mixer has a simple structure and does not contain wearing parts, such as agitator blades or bearings. Therefore, compared with traditional mixing equipment, the maintenance cost of the static mixer is lower and the maintenance process is more simplified. This not only reduces equipment downtime, but also improves the overall stability and reliability of the production line;

[0028] 3. The system adopts modular design, which allows the system to be flexibly configured and expanded according to production needs, thereby improving production efficiency;

[0029] 4. Since the static mixer does not rely on an external power source for stirring, the risk of introducing impurities due to wear or failure of the stirring equipment is reduced. This helps to maintain the cleanliness of the production environment and further ensure product quality; reducing energy consumption and reducing equipment maintenance costs not only helps to reduce production costs, but also conforms to the current trend of environmental friendliness and sustainable development. BRIEF DESCRIPTION OF THE DRAWINGS

[0030] Figure 1 A schematic diagram of the overall connection structure of the system according to an embodiment of the present invention;

[0031] Figure 2 It is a partial structural schematic diagram of a first material conveying and processing module according to an embodiment of the present invention;

[0032] Figure 3 A schematic diagram of a local structure of a system according to an embodiment of the present invention;

[0033] Figure 4 A schematic diagram of a cross-sectional structure of a static mixer according to an embodiment of the present invention;

[0034] Figure 5 A schematic diagram of a cross-sectional structure of a static mixer according to an embodiment of the present invention;

[0035] Figure 6 A schematic diagram of a cross-sectional structure of a guide channel according to an embodiment of the present invention;

[0036] Figure 7 The figure is a schematic diagram of a cross-sectional structure of a guide channel according to an embodiment of the present invention.

[0037] The meanings of the reference numerals are as follows: 1. first material conveying and processing module; 11. first storage tank; 111. first feeding port; 112. first feeding port; 113. first feeding port; 114. breathing valve; 12. first mixing tank; 121. first mixing outlet; 122. mixing circuit; 13. first intermediate tank; 14. first foaming machine working tank; 2. second material conveying module; 21. second storage tank; 22. second mixing tank; 221. second mixing outlet; 3. third material conveying and processing module; 31. third storage tank; 311. third feeding port; 32. third intermediate tank; 33. third foaming machine working tank; 4. temperature control module; 41. hot and cold all-in-one machine; 42. heat exchanger; 5. first static mixer; 51. shell; 511. dispersed phase inlet; 512. mixing channel; 513. dispersed phase outlet; 52. first a rotor; 53, a second rotor; 54, a flow hole; 55, a guide channel; 551, a left-handed spiral mixing plate; 552, a left-handed spiral mixing plate; 553, a fin; 554, a sputtering hole; 6, a second static mixer; 7, a first feed channel; 71, a tank truck; 72, a bellows; 8, a first temperature control circuit; 9, a second feed channel; 10, a second temperature control circuit; 101, a manual ball valve; 102, a filter; 10 3. Unloading pump; 104. Safety overflow valve; 105. Check valve; 106. Pressure gauge; 107. Pneumatic ball valve; 108. Transfer pump; 109. Mold temperature controller; 110. Heat exchange equipment; 200. First feeding pipeline; 300. Second feeding pipeline; 400. Auxiliary material replenishment pipeline; 401. Diaphragm pump; 402. Auxiliary material tank; 500. Electronic scale; 600. Maximum liquid level indicator; 700. Isocyanate I BC raw material barrel; 800. Fourth storage tank; 801. Pneumatic three-way ball valve; 900. Third temperature control circuit. DETAILED DESCRIPTION

[0038] For better understanding and implementation, the technical solutions in the embodiments of the present invention will be clearly and completely described and discussed below in conjunction with the accompanying drawings of the present invention. Obviously, what is described here is only a part of the examples of the present invention, not all the examples. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative work are within the scope of protection of the present invention.

[0039] In order to facilitate the understanding of the embodiments of the present invention, the following will be further explained by taking specific embodiments as examples in conjunction with the drawings, and each embodiment does not constitute a limitation on the embodiments of the present invention.

[0040] In the description of the present invention, it should be noted that the terms "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside" and "outside" etc. indicate directions or positional relationships based on the directions or positional relationships shown in the accompanying drawings. They are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific direction, be constructed and operated in a specific direction. Therefore, they cannot be understood as limiting the present invention.

[0041] Unless otherwise defined, all technical and scientific terms used herein have the same meaning as those commonly understood by those skilled in the art of the present invention. The terms used in the specification of the present invention herein are only for the purpose of describing specific embodiments and are not intended to limit the present invention.

[0042] Embodiment 1 of the present invention refers to Figure 1-Figure 7 As shown, a static mixing batching and raw material conveying system is disclosed, including a first material conveying processing module 1, a second material conveying module 2, a third material conveying processing module 3 and a temperature control module 4, wherein the first material conveying processing module 1 includes a first storage tank 11, a first mixing tank 12, a first intermediate tank 13 and a first foaming machine working tank 14 connected in sequence, the second material conveying module 2 includes a second storage tank 21 and a second mixing tank 22 connected in sequence, the second mixing tank 22 is connected to the first intermediate tank 13, the third material conveying processing module 3 includes a third storage tank 31, a third intermediate tank 32 and a third foaming machine working tank 33 connected in sequence, the temperature control module 4 includes a cold and hot integrated machine 41 and a plurality of heat exchangers 42 connected thereto, The heat exchanger 42 is respectively connected to the first material conveying processing module 1, the second material conveying processing module 2 and the third material conveying processing module 3, and is used to control the mixing temperature; a first static mixer 5 is arranged between the first mixing tank 12 and the first intermediate tank 13, and a second static mixer 6 is arranged between the second mixing tank 22 and the first intermediate tank 13. By introducing the secondary mixing of the static mixer, the system can achieve efficient mixing without an external power source, thereby significantly reducing the energy consumption; the static mixer has a simple structure and no wearing parts. Compared with traditional mixing equipment, its maintenance cost is lower and the maintenance process is simpler; the system adopts a modular design, including multiple material conveying processing modules and a temperature control module 4, which is convenient for flexible configuration and expansion, and improves production efficiency.

[0043] In a specific embodiment, see Figure 1-Figure 3As shown, the first storage tank 11 is a basic polyether tank, the second storage tank 21 is a grafted polyether tank, and the third storage tank 31 is an isocyanate tank. The first storage tank 11 includes a first feeding port 111, a first feed inlet 112 and a first discharge port 113, and the second storage tank 21 includes a second feeding port, a second feed inlet and a second discharge port. The first feeding port 111 is connected to a tank truck 71 through a first feeding channel 7 for infusing raw materials into the first storage tank 11, and the second feeding port is connected to another tank truck 71 through a second feeding channel 9 for infusing raw materials into the second storage tank 21. The first feeding channel 7 is provided with a bellows 72, a manual ball valve 101, a filter 102, a manual ball valve 101, a discharge pump 103, a safety relief valve 104, a manual ball valve 101, a check valve 105, a pressure gauge 106 and a pneumatic ball valve 107 in sequence from the tank truck 71 to the first feeding port 111. Similarly, the second feeding channel 9 is provided with a bellows 72, a manual ball valve 101, a filter 102, a manual ball valve 101, a discharge pump 103, a safety overflow valve 104, a manual ball valve 101, a check valve 105, a pressure gauge 106 and a pneumatic ball valve 107 in sequence from the tank truck 71 to the second feeding port. 01, filter 102, manual ball valve 101, discharge pump 103, safety relief valve 104, manual ball valve 101, check valve 105, pressure gauge 106 and pneumatic ball valve 107; multiple manual ball valves 101 are used to manually control the opening and closing of the feeding channel, which is convenient for quickly cutting off the material flow in an emergency or daily maintenance. The filter 102 is located at the front end of the first feeding channel 7, which is used to remove impurities in the material to ensure the purity of the material and prevent clogging of the pipeline or affecting the subsequent process. The discharge pump 103 provides power to extract the material from the storage tank and transport it to the next process. The safety relief valve 104 will automatically open when the pressure in the pipeline exceeds the set value to release excess pressure and protect the pipeline and equipment from damage. The pressure gauge 106 is used to monitor the pressure in the pipeline in real time. The check valve 105 ensures that the material can only flow in one direction to prevent backflow and ensure the continuity and stability of the production process. The pneumatic ball valve 107 can control the opening and closing of the valve through a pneumatic device, which is usually used in remote control or automated production lines to improve production efficiency.

[0044] See also Figure 1-2As shown, a first temperature control circuit 8 is connected between the first feed port 112 and the first discharge port 113, and a second temperature control circuit 10 is connected between the second feed port and the second discharge port. The first temperature control circuit 8 and the second temperature control circuit 10 are designed to control the temperature of the raw materials in the storage tank to ensure that they are kept within an appropriate temperature range during storage and transportation. Specifically, the first temperature control loop 8 and the second temperature control loop 10 both include a filter 102, a material transfer pump 108, a safety relief valve 104, a manual ball valve 101, a one-way valve 105, a pressure gauge 106, a manual ball valve 101, a heat exchange device 110, a mold temperature controller 109 and a pneumatic ball valve 107. The temperature control loops both include various equipment required for the complete process from raw material input to finished product output, thereby ensuring the continuity and stability of the production process; the setting of safety devices such as the safety relief valve 104 and the pressure gauge 106 effectively reduces the risks that may occur in the production process; the combined use of the manual ball valve 101 and the pneumatic ball valve 107 not only ensures the ability to respond quickly in an emergency, but also meets the needs of an automated production line; the reasonable selection and configuration of equipment such as the filter 102 and the material transfer pump 108 ensures the smooth flow of materials and temperature control media, thereby improving production efficiency. In the first temperature control loop 8 and the second temperature control loop 10, branch pipelines are connected for communicating with the first mixing tank 12, so that the material can be transported to the mixing tank for mixing while controlling the mixing temperature. The one-way valve 105 in the second temperature control loop 10 is also connected to a pipeline communicating with the second mixing tank 22, for communicating the first mixing tank 12 and the second mixing tank 22. It should be noted that the specific flow of the material is controlled by the pneumatic ball valve 107, so the material can be controlled to flow in each specific branch.

[0045] See also Figure 2As shown, the third storage tank 31 includes a third discharge port 311, the third discharge port 311 is connected to the third intermediate tank 32, and the third discharge port 311 and the third intermediate tank 32 are sequentially provided with a filter 102, a transfer pump 108, a safety relief valve 104, a manual ball valve 101, a one-way valve 105, a pressure gauge 106 and a pneumatic ball valve 107. Similarly, the third discharge port 311 is also provided with a reflux pipeline controlled by the pneumatic ball valve 107. Optionally, the third intermediate tank 32 may also be connected to a fourth storage tank 800 or more storage tanks. In one embodiment, the third intermediate tank 32 is connected to an isocyanate IBC raw material barrel 700 via a transfer pump 108, wherein a pneumatic three-way ball valve 801 is further provided between the third intermediate tank 32 and the isocyanate IBC raw material barrel 700 for adding a loop, which is connected to the isocyanate tank, i.e., the fourth storage tank 800, so that the raw materials in the isocyanate IBC raw material barrel 700 can be controlled by the pneumatic ball valve 107 to enter the fourth storage tank 800 for temporary storage, and then transported to the third intermediate tank 32 via the pneumatic three-way ball valve 801 and the transfer pump 108. The discharge port of the third intermediate tank 32 is connected to the third foaming working tank.

[0046] In some embodiments, see Figure 3As shown, optionally, in order to ensure the temperature of the raw materials in the third intermediate tank 32, a branch is provided between the discharge port of the third intermediate tank 32 and the third foaming working tank, and the branch is a third temperature control loop 900, which is used to control the reflux of the raw materials to the third intermediate tank 32 through a pneumatic ball valve 107, and the third temperature control loop 900 is connected to the temperature control module 4. The first mixing tank 12 is provided with a first mixing outlet 121, the second mixing tank 22 is provided with a second mixing outlet 221, a first feeding pipe 200 is provided between the first mixing outlet 121 and the first intermediate tank 13 and the first foaming machine working tank 14, and a second feeding pipe 300 is provided between the second mixing outlet 221 and the first intermediate tank 13 and the first foaming machine working tank 14. In order to ensure the mixing temperature, a mixing loop 122 is provided on the first feeding pipe 200 and the second feeding pipe 300 for flowing back to the first mixing tank 12 and the second mixing tank 22, and the mixing loop 122 is connected to the temperature control module 4. Specifically, the mixing loop 122 and the third temperature control loop 900 are both provided with a heat exchanger 42, and the heat exchanger 42 is connected to the cold and hot integrated machine 41. The first static mixer 5 is arranged on the first feeding pipe 200; the second static mixer 6 is arranged on the second feeding pipe 300. Through the design of two mixing tanks and one intermediate tank, the system can flexibly process a variety of materials to meet the production needs of different products; the use of the static mixer significantly improves the mixing efficiency of the materials and ensures the uniformity and stability of the materials before foaming; the design of the entire system optimizes the process of material transmission and mixing, improves production efficiency and reduces production costs.

[0047] In some embodiments, see Figure 1 , Figure 3 As shown, an auxiliary material replenishing pipeline 400 is also connected between the first mixing tank 12 and the second mixing tank 22. The auxiliary material replenishing pipeline 400 includes a diaphragm pump 401 and an auxiliary material tank 402. The design of the auxiliary material replenishing pipeline 400 allows the system to flexibly adjust the type and amount of auxiliary materials according to production needs, thereby optimizing product performance; the use of the diaphragm pump 401 reduces the risk of leakage and contamination, and ensures the safety and reliability of auxiliary material transportation.

[0048] In some embodiments, see Figure 1-Figure 3As shown, optionally, the first storage tank 11, the first mixing tank 12, the second storage tank 21 and the second mixing tank 22 are all provided with an electronic scale 500 for weighing, and the first storage tank 11 and the second storage tank 21 are also provided with a maximum liquid level indicator 600. The main function of the electronic scale 500 is to monitor and record the weight of the material in the storage tank or the mixing tank in real time, which is essential for accurately controlling the feeding amount of the material, monitoring the material consumption and ensuring the product quality; the main function of the maximum liquid level indicator 600 is to monitor the liquid level in the storage tank. When the liquid level reaches the preset highest point, an alarm or signal will be issued to prevent the material from overflowing or leaking; the design of the electronic scale 500 and the maximum liquid level indicator 600 emphasizes accuracy, ensuring accurate monitoring of the material weight and liquid level. These devices are usually connected to a central control system to achieve real-time data transmission and remote monitoring. This improves the automation and intelligence level of the system and reduces the difficulty and risk of manual operation. A breathing valve 114 can also be set on the first storage tank 11 and the second storage tank 21.

[0049] In order to achieve static mixing, in a specific embodiment, refer to Figure 4 As shown, the first static mixer 5 and the second static mixer 6 both include a shell 51, a first rotor 52 and a second rotor 53, and the shell 51 includes a dispersed phase inlet 511, a mixing channel 512 and a dispersed phase outlet 513 from one end to the other end, the first rotor 52 is spirally wound clockwise in the mixing channel 512 in the shell 51, and the second rotor 53 is spirally wound counterclockwise in the mixing channel 512 in the shell 51; wherein, the first rotor 52 and the second rotor 53 are alternately arranged along the mixing channel 512, thereby guiding the fluid to undergo multiple divisions, rotations and recombination in the channel, thereby achieving an efficient mixing effect; the first rotor 52 and the second rotor 53 are alternately arranged along the mixing channel 512, which can further enhance the mixing effect and avoid the formation of dead zones or short circuits in the channel.

[0050] In order to further improve the mixing effect, in some embodiments, refer to Figure 5 As shown, a plurality of flow holes 54 are provided on the first rotor 52 and the second rotor 53, and a guide channel 55 is extended from the flow hole 54 to one end of the dispersed phase outlet 513. The arrangement of the plurality of flow holes 54 can ensure that the raw materials are evenly distributed between the rotors to avoid excessively high or low local concentrations; the guide channel 55 is the portion of the flow hole 54 extending to one end of the dispersed phase outlet 513, and the flow holes 54 and the guide channel 55 together constitute a flow path of the fluid between the rotors. A portion of the fluid will pass through the flow holes 54, and a portion of the fluid will be blocked and guided by the rotors, causing changes in direction and speed, with the purpose of guiding the fluid to flow more complexly between the rotors, thereby improving the mixing efficiency.

[0051] For further optional information, see Figure 5 , Figure 6 As shown, the guide channel 55 is provided with left-hand spiral mixing sheets 551 and right-hand spiral mixing sheets arranged alternately, which can divide, rotate and reorganize the fluid entering the guide channel 55 from the flow hole 54, further improve the mixing effect, save the total length of the mixing channel 512, and achieve a better mixing effect within a limited length. In another embodiment, refer to Figure 5 , Figure 7 As shown, the left spiral mixing plate 551 and the right spiral mixing plate can be replaced with fins 553 arranged alternately in the guide channel 55, and the fins 553 are penetrated through the side wall of the guide channel 55. Sputtering holes 554 are formed between the side of the fin 553 facing the dispersed phase inlet 511 and the side wall of the guide channel 55, and the sputtering holes 554 are connected to the mixing channel 512. The fins 553 are penetrated through the side wall of the guide channel 55 to form a staggered structure. This design not only increases the complexity and surface area of ​​the guide channel 55, but also provides additional mixing opportunities. The sputtering holes 554 allow the fluid to pass through the mixing channel 512 and sputter and collide, thereby further promoting mixing. The presence of the sputtering holes 554 enables the fluid to enter the guide channel 55 from the mixing channel 512 under the guidance of the fins 553, and violent turbulence and mixing occur during the sputtering process. When the fluid passes through the sputtering holes 554, it will be obstructed and guided by the fins 553, causing a change in direction and an increase in speed, thereby increasing mutual collisions and shear forces between the fluids. This sputtering and collision effect helps to break up clumps and stratification in the fluid, allowing the fluid to be more evenly distributed in the guide channel 55.

[0052] In summary, the static mixing batching and raw material conveying system provided by the present invention has the following technical effects:

[0053] 1. By introducing a static mixer, the system uses the fluid's own flow energy to achieve efficient mixing without relying on an external power source, such as a stirring paddle or agitator. This feature significantly reduces power consumption, making the energy consumption of the entire production process more economical. The static mixer is divided into a first static mixer 5 and a second static mixer 6, which can achieve secondary mixing and achieve more uniform mixing, avoiding problems such as local uneven concentration or material stratification that may be caused by traditional mixing equipment. This helps to improve the quality and consistency of the final product and meet more stringent quality control requirements;

[0054] 2. The static mixer has a simple structure and does not contain wearing parts, such as agitator blades or bearings. Therefore, compared with traditional mixing equipment, the maintenance cost of the static mixer is lower and the maintenance process is more simplified. This not only reduces equipment downtime, but also improves the overall stability and reliability of the production line;

[0055] 3. The system adopts modular design, which allows the system to be flexibly configured and expanded according to production needs, thereby improving production efficiency;

[0056] 4. Since the static mixer does not rely on an external power source for stirring, the risk of introducing impurities due to wear or failure of the stirring equipment is reduced. This helps to maintain the cleanliness of the production environment and further ensure product quality; reducing energy consumption and reducing equipment maintenance costs not only helps to reduce production costs, but also conforms to the current trend of environmental friendliness and sustainable development.

[0057] The technical means disclosed in the scheme of the present invention are not limited to the technical means disclosed in the above-mentioned implementation mode, but also include technical schemes composed of any combination of the above-mentioned technical features. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the principle of the present invention, and these improvements and modifications are also regarded as the protection scope of the present invention.

Claims

1. A static mixing batching and raw material conveying system, characterized in that: include: A first material conveying and processing module (1), the first material conveying and processing module (1) comprising a first storage tank (11), a first mixing tank (12), a first intermediate tank (13) and a first foaming machine working tank (14) which are connected in sequence; A second material conveying module (2), the second material conveying module (2) comprising a second storage tank (21) and a second mixing tank (22) connected in sequence, the second mixing tank (22) being in communication with the first intermediate tank (13); A third material conveying and processing module (3), the third material conveying and processing module (3) comprising a third storage tank (31), a third intermediate tank (32) and a third foaming machine working tank (33) which are connected in sequence; A temperature control module (4), the temperature control module (4) comprising a cooling and heating integrated machine (41) and a plurality of heat exchangers (42) connected thereto, the heat exchangers (42) being respectively connected to the first material conveying and processing module (1), the second material conveying and processing module (2) and the third material conveying and processing module (3), and being used for controlling the temperature of the mixed material; A first static mixer (5) is provided between the first mixing tank (12) and the first intermediate tank (13), and a second static mixer (6) is provided between the second mixing tank (22) and the first intermediate tank (13).

2. A static mixing batching and raw material delivery system according to claim 1, characterized in that: The first static mixer (5) and the second static mixer (6) both comprise: A shell (51), wherein the shell (51) comprises, from one end to the other end, a dispersed phase inlet (511), a mixing channel (512) and a dispersed phase outlet (513); A first rotating blade (52), the first rotating blade (52) spirally encircling the mixing flow channel (512) in the housing (51) in a clockwise direction; A second rotating blade (53), the second rotating blade (53) spirally surrounds the mixing flow channel (512) in the housing (51) in a counterclockwise direction; Wherein, the first rotary vanes (52) and the second rotary vanes (53) are alternately arranged along the mixing flow channel (512).

3. A static mixing batching and raw material delivery system according to claim 2, characterized in that: A plurality of flow holes (54) are provided on the first rotating blade (52) and the second rotating blade (53), and a guide channel (55) is extended from the flow hole (54) toward one end of the dispersed phase outlet (513).

4. A static mixing batching and raw material delivery system according to claim 3, characterized in that: The guide channel (55) is provided with left-hand spiral mixing sheets (551) and right-hand spiral mixing sheets which are arranged alternately.

5. A static mixing batching and raw material delivery system according to claim 3, characterized in that: The guide channel (55) is provided with staggered fins (553), the fins (553) are penetrated through the side wall of the guide channel (55), and a sputtering hole (554) is formed between the side of the fin (553) facing the dispersed phase inlet (511) and the side wall of the guide channel (55), and the sputtering hole (554) is connected to the mixing channel (512).

6. A static mixing batching and raw material delivery system according to any one of claims 1 to 5, characterized in that: The first storage tank (11) comprises a first feeding port (111), a first feed inlet (112) and a first discharge port (113); the first feeding port (111) is connected to a first feed channel (7); a first temperature control circuit (8) is connected between the first feed inlet (112) and the first discharge port (113); the second storage tank (21) comprises a second feeding port, a second feed inlet and a second discharge port; the second feeding port is connected to a second feed channel (9); a second temperature control circuit (10) is connected between the second feed inlet and the second discharge port.

7. A static mixing batching and raw material delivery system according to claim 6, characterized in that: The first material delivery channel (7) and the second material delivery channel (9) both comprise a manual ball valve (101), a filter (102), a discharge pump (103), a safety relief valve (104), a one-way valve (105), a pressure gauge (106) and a pneumatic ball valve (107); the first temperature control circuit (8) and the second temperature control circuit (10) both comprise a filter (102), a material transfer pump (108), a safety relief valve (104), a manual ball valve (101), a one-way valve (105), a pressure gauge (106), a heat exchange device (110) and a mold temperature controller (109).

8. A static mixing batching and raw material delivery system according to any one of claims 1 to 5, characterized in that: The first mixing tank (12) is provided with a first mixing outlet (121), the second mixing tank (22) is provided with a second mixing outlet (221), a first feeding pipe (200) is provided between the first mixing outlet (121) and the first intermediate tank (13) and the first foaming machine working tank (14), and the first static mixer (5) is provided on the first feeding pipe (200); a second feeding pipe (300) is provided between the second mixing outlet (221) and the first intermediate tank (13) and the first foaming machine working tank (14), and the second static mixer (6) is provided on the second feeding pipe (300).

9. A static mixing batching and raw material delivery system according to any one of claims 1 to 5, characterized in that: An auxiliary material replenishment pipeline (400) is also connected between the first mixing tank (12) and the second mixing tank (22), and the auxiliary material replenishment pipeline (400) includes a diaphragm pump (401) and an auxiliary material tank (402).

10. A static mixing batching and raw material delivery system according to any one of claims 1 to 5, characterized in that: The first storage tank (11), the first mixing tank (12), the second storage tank (21) and the second mixing tank (22) are all provided with an electronic scale (500) for weighing, and the first storage tank (11) and the second storage tank (21) are also provided with a maximum liquid level indicator (600).

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