Rapid glue making system

Abstract

The utility model relates to the technical field of glue making systems, particularly provides a rapid glue making system, and aims to solve the problem that the glue making time is relatively long due to low glue mixing and dispersing efficiency of an existing glue making system. In order to achieve the purpose, the utility model provides a rapid glue making system, which comprises a glue making circulation tank, a glue making device, a glue making device and a glue making device, and is characterized in that the glue making circulation tank comprises a first tank body, and the first tank body is provided with a first port and a second port; the powder tank comprises a second tank body, and the second tank body is provided with a third port; the mixing mechanism is provided with a fourth port, a fifth port and a sixth port, the fourth port is communicated with the second port, and the fifth port is communicated with the third port; the dispersing mechanism comprises a cavity and a first rotating shaft, the cavity is provided with a seventh port and an eighth port, the seventh port is communicated with the sixth port, the eighth port is communicated with the first port, a dispersing component is arranged in the cavity, and the first rotating shaft is connected with the dispersing component, so that the dispersing component can be driven to rotate to disperse materials.

Description

Technical Field

[0001] The utility model relates to the technical field of glue making systems, and specifically provides a rapid glue making system. Background Art

[0002] In the field of battery material production, battery positive and negative electrode materials and deionized water are mixed and processed through a glue making system to obtain battery positive and negative electrode glue accordingly.

[0003] Traditional glue production systems use high-speed and low-speed paddles within the glue production tank to stir the glue liquid and disperse the rubber. However, this traditional mixing and dispersion method is probabilistic. During the mixing process, the paddles cause the particles to move randomly within the glue production tank. Due to the large internal space of the glue production tank, the rubber may become locally concentrated or stratified, resulting in uneven mixing and dispersion and low mixing and dispersion efficiency. This results in longer glue production times, lower rubber production capacity, and higher investment costs. Utility Model Content

[0004] The utility model aims to solve the above technical problem, that is, to solve the problem that the existing glue making system has low glue mixing and dispersion efficiency, thereby making the glue making time longer.

[0005] The utility model provides a rapid glue making system, which comprises:

[0006] A glue circulation tank comprises a first tank body, the first tank body having a first port and a second port, the first port and the second port being respectively communicated with the interior of the first tank body;

[0007] A powder tank comprising a second tank body, wherein the second tank body has a third port, and the third port is in communication with the interior of the second tank body;

[0008] a mixing mechanism having a fourth port, a fifth port, and a sixth port, wherein the fourth port, the fifth port, and the sixth port are respectively in communication with an interior of the mixing mechanism, the fourth port is in communication with the second port, and the fifth port is in communication with the third port;

[0009] A dispersion mechanism includes a chamber and a first rotating shaft, the chamber having a seventh port and an eighth port, the seventh port and the eighth port being respectively connected to the interior of the chamber, the seventh port being connected to the sixth port, and the eighth port being connected to the first port, a dispersion component being provided in the chamber, and the first rotating shaft being connected to the dispersion component, thereby being able to drive the dispersion component to rotate to disperse the material.

[0010] In some feasible embodiments of the above-mentioned rapid glue making system, the mixing mechanism is a venturi ejector, the venturi ejector includes a mixing pipe and a nozzle component, the mixing pipe includes an inlet pipe section and an outlet pipe section in sequence along its axial direction, the fourth port and the fifth port are respectively connected to the inlet pipe section,

[0011] The nozzle component is arranged at the fourth port and extends into the inlet pipe section along the axial direction of the mixing pipe. The fourth port is connected with the second port through the nozzle component. The inner diameter of the nozzle component gradually decreases along the axial direction of the mixing pipe. The outlet pipe section is a Venturi tube structure, and the sixth port is connected with the outlet pipe section.

[0012] In some feasible embodiments of the above-mentioned rapid glue making system, the outlet pipe section includes a contraction section, a throat section and a diffusion section in sequence along the axial direction of the mixing pipe.

[0013] The inner diameter of the contraction section gradually decreases along the axial direction of the mixing pipe, and the pipe section with the largest inner diameter of the contraction section is connected to the inlet pipe section.

[0014] The inner diameter of the diffusion section gradually increases along the axial direction of the mixing pipe, and the pipe section with the largest inner diameter of the diffusion section is connected to the sixth port.

[0015] The inner diameter of the throat is smaller than the minimum inner diameter of the contraction section and smaller than the minimum inner diameter of the diffusion section. Both ends of the throat are connected to the pipe section with the minimum inner diameter of the contraction section and the pipe section with the minimum inner diameter of the diffusion section respectively.

[0016] In some feasible embodiments of the above-mentioned rapid glue making system, the dispersion component includes a stator and a rotor, the stator is fixedly arranged in the chamber, the stator and the rotor are rotated together, the rotor is connected to the first rotating shaft, and the rotor can disperse the material by rotating.

[0017] In some feasible implementations of the above-mentioned rapid glue making system, a centrifugal component is further provided in the chamber, and the first rotating shaft is connected to the centrifugal component, thereby being able to drive the centrifugal component to rotate to transport materials.

[0018] In some feasible embodiments of the above-mentioned rapid glue making system, the centrifugal component includes a centrifugal impeller, the centrifugal impeller is connected to the first rotating shaft, and the centrifugal impeller can transport materials by rotating.

[0019] In some feasible implementations of the above-mentioned rapid glue making system, the glue making system further includes a pipeline cooler, and the pipeline cooler is sleeved on the pipe section between the eighth port and the first port.

[0020] In some feasible implementations of the above-mentioned rapid glue making system, the glue making circulation tank further includes a first temperature sensor, which is disposed on the first tank body and is used to detect the temperature of the material in the first tank body.

[0021] In some feasible implementations of the above-mentioned rapid glue making system, a second temperature sensor is provided on the pipe section close to the eighth port, and the second temperature sensor is used to detect the temperature of the material in the pipe section close to the eighth port.

[0022] In some feasible embodiments of the above-mentioned rapid glue making system, the glue making circulation tank also includes an anchor stirring paddle and a second rotating shaft, the second rotating shaft is connected to the anchor stirring paddle, the anchor stirring paddle is arranged in the first tank body and close to its inner bottom, and the anchor stirring paddle can stir the material by rotating.

[0023] The present invention provides a mixing mechanism and a dispersing mechanism, enabling the mixing mechanism to mix the rubber powder and solvent within the system, and the dispersing mechanism to disperse the rubber material within the system. Compared to the prior art solution of installing high-speed and low-speed dispersing paddles within the rubber storage tank, the present invention replaces the high-speed and low-speed dispersing paddles by providing the mixing mechanism and the dispersing mechanism, eliminating the need for corresponding dispersing paddles on the rubber circulation tank and reducing the investment cost of the rubber circulation tank. At the same time, the mixing mechanism and the dispersing mechanism can more efficiently mix and disperse the rubber material, reducing rubber production time and thereby increasing rubber material production capacity. BRIEF DESCRIPTION OF THE DRAWINGS

[0024] The preferred embodiments of the present invention are described below with reference to the accompanying drawings, in which:

[0025] Figure 1 This is one of the structural principle diagrams of the rapid glue making system of the utility model;

[0026] Figure 2 This is the second structural principle diagram of the rapid glue making system of the utility model, in which the dispersion mechanism and pipeline cooler are omitted;

[0027] Figure 3 This is the third structural principle diagram of the rapid glue making system of the utility model, in which the glue making circulation tank is omitted;

[0028] Figure 4 It is a cross-sectional view of the mixing mechanism of the present utility model;

[0029] Figure 5 It is a schematic structural diagram of the dispersion mechanism of the present invention, wherein the chamber is cut away;

[0030] Figure 6It is an exploded view of the guide component, the dispersion component, the centrifugal component and the first rotating shaft of the utility model.

[0031] List of reference numerals:

[0032] 1-Glue circulation tank; 11-First tank body; 111-First port; 112-Second port; 113-Feed port; 114-Discharge port; 115-Vent; 12-First temperature sensor; 13-Anchor stirring paddle; 14-Second rotating shaft; 15-First motor; 16-Spray head; 17-Filter component; 2-Powder tank; 21-Second tank body; 211-Third port; 3-Mixing mechanism; 31-Mixing pipe; 311-Inlet pipe section; 312-Outlet pipe section; 3121-Contraction section; 3122-Throat; 3123-Diffuser section; 313-Fourth port; 314-Fifth port; 315-Sixth port; 32-Nozzle component; 4-Dispersion mechanism; 41-Cavity; 411-Seventh port; 412-eighth port; 42-first rotating shaft; 43-dispersing component; 431-stator; 432-rotor; 44-centrifugal component; 441-centrifugal impeller; 45-guide component; 451-spiral blade; 46-third motor; 5-pipeline cooler; 51-liquid inlet; 52-liquid outlet; 6-second temperature sensor; 7-pressure sensor; 801-first valve; 802-second valve; 803-third valve; 804-fourth valve; 805-fifth valve; 806-sixth valve; 807-seventh valve; 808-eighth valve; 809-ninth valve; 810-first check valve; 811-second check valve; 812-rotary feeding valve; 8121-second motor. DETAILED DESCRIPTION

[0033] The preferred embodiments of the present invention are described below with reference to the accompanying drawings. Those skilled in the art should understand that these embodiments are only used to explain the technical principles of the present invention and are not intended to limit the scope of protection of the present invention.

[0034] It should be noted that, in the description of the present invention, terms such as "upper", "lower", "inside", and "outside" indicating directions or positional relationships are based on the directions or positional relationships shown in the accompanying drawings. This is only for the convenience of description and does not indicate or imply that the device or element must have a specific orientation, be constructed and operated in a specific orientation. Therefore, it cannot be understood as a limitation on the present invention.

[0035] In addition, it should be noted that in the description of the present invention, unless otherwise clearly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense. For example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection, a direct connection, an indirect connection through an intermediate medium, or a communication between the two components. For those skilled in the art, the specific meanings of the above terms in the present invention can be understood according to the specific circumstances. In addition, the terms "first", "second", "third", "fourth", "fifth", "sixth", "seventh", "eighth", and "ninth" are used for descriptive purposes only and are not to be understood as indicating or implying relative importance.

[0036] like Figure 1 As shown, an embodiment of the present invention provides a rapid glue making system, which includes a glue making circulation tank 1, a powder tank 2, a mixing mechanism 3 and a dispersing mechanism 4, etc.

[0037] like Figure 2As shown, the glue circulation tank 1 includes a first tank body 11, etc. The interior of the first tank body 11 is used to accommodate glue materials, including glue powder, solvent, powder liquid material and glue. The first tank body 11 has a feed port 113, a discharge port 114, a vent 115, a first port 111 and a second port 112. The feed port 113, the discharge port 114, the vent 115, the first port 111 and the second port 112 are respectively connected to the interior of the first tank body 11. The feed port 113 is located at the top of the first tank body 11 and is used to allow the solvent to pass through so that the solvent is transported into the first tank body 11. In this embodiment, the solvent is deionized water. A first valve 801 is provided at the feed port 113 so that the first valve 801 can control the opening and closing state of the feed port 113. When the first valve 801 is in the open state, the feed port 113 can transport the solvent into the first tank body 11. The discharge port 114 is located at the bottom of the first tank body 11 and is used to discharge the finished rubber material in the first tank body 11 to the outside. A second valve 802 is provided at the discharge port 114 to control the opening and closing of the discharge port 114. When the second valve 802 is open, the rubber material in the first tank body 11 can be discharged to the outside through the discharge port 114. The vent 115 is located at the top of the first tank body 11 and is used to connect the interior of the first tank body 11 with the outside to maintain air pressure balance within the first tank body 11. A filter component 17 is provided at the air inlet to filter impurities in the air to prevent impurities from contaminating the material in the first tank body 11. The first port 111 is located at the top of the first tank body 11 and is used to communicate with the eighth port 412. A sixth valve 806 is provided at the first port 111 to control the opening and closing of the first port 111. The second port 112 is located at the bottom of the first tank body 11 and is used to communicate with the fourth port 313 . A third valve 803 is provided at the second port 112 so that the third valve 803 can control the opening and closing state of the second port 112 .

[0038] Further, continue to refer to Figure 2 The glue circulation tank 1 further includes a first temperature sensor 12 , which is disposed at the bottom of the first tank body 11 . The first temperature sensor 12 is used to detect the temperature of the material in the first tank body 11 .

[0039] Further, continue to refer to Figure 2The rubber circulation tank 1 also includes a first motor 15, an anchor stirring paddle 13, and a second rotating shaft 14. The first motor 15 is fixedly mounted on the top of the first tank body 11. The second rotating shaft 14 is arranged in a vertical direction. The starting end of the second rotating shaft 14 is drivingly connected to the drive shaft of the first motor 15, and the end of the second rotating shaft 14 is connected to the anchor stirring paddle 13. The anchor stirring paddle 13 is arranged in the first tank body 11 and near its bottom. Driven by the first motor 15, the second rotating shaft 14 can drive the anchor stirring paddle 13 to rotate, so that the anchor stirring paddle 13 can rotate to stir the material at the bottom of the first tank body 11, thereby preventing the undissolved rubber powder at the bottom of the first tank body 11 from settling or solidifying, thereby preventing the rubber material from clumping.

[0040] Further, continue to refer to Figure 2 The glue circulation tank 1 further includes a spray head 16, which is disposed at the inner top of the first tank body 11. The water inlet of the spray head 16 is connected to the ninth valve 809, so that the ninth valve 809 can control the opening and closing of the spray head 16. When the ninth valve 809 is open, the spray head 16 can output spray water into the first tank body 11 to clean the interior of the first tank body 11. It should be noted that the number of spray heads 16 is not limited to two as shown in the figure, and can be one, three, four, five, etc.

[0041] like Figure 2 and Figure 3 As shown, the powder tank 2 includes a second tank body 21, which is used to hold rubber powder, specifically the positive and negative electrode materials of a battery. The bottom of the second tank body 21 has a third port 211, which communicates with the interior of the second tank body 21. The powder tank 2 is specifically a rubber powder metering tank. A rotary feed valve 812 is provided at the third port 211. The rotary feed valve 812 is driven by a second motor 8121 and is used to convey the rubber powder delivered from the third port 211 to the fifth port 314. It is understood that the rotary feed valve 812 is a specialized device used in powder conveying systems for unloading, metering, dust removal, quantitative conveying, mixing, and packaging. The technology behind the rotary feed valve 812 is very mature and will not be further described here.

[0042] Continue to refer Figure 2 and Figure 3The mixing mechanism 3 has a fourth port 313, a fifth port 314, and a sixth port 315, each of which is in communication with the interior of the mixing mechanism 3. The fourth port 313 is in communication with the second port 112. A fourth valve 804 is provided at the fifth port 314, enabling the fourth valve 804 to control the opening and closing of the fifth port 314. The fifth port 314 is in communication with the third port 211 via the fourth valve 804 and the rotary feeding valve 812. When the fourth valve 804 is open, the rotary feeding valve 812 drives the rubber powder in the second tank 21 to be sequentially delivered to the interior of the mixing mechanism 3 through the third port 211, the rotary feeding valve 812, the fourth valve 804, and the fifth port 314. With this arrangement, the mixing mechanism 3 can mix the solvent in the first tank 11 with the rubber powder in the second tank 21 to produce a powder-liquid material.

[0043] Furthermore, if Figure 4 As shown, the mixing mechanism 3 is a Venturi ejector, which includes a mixing pipe 31 and a nozzle assembly 32. The mixing pipe 31 includes an inlet pipe section 311 and an outlet pipe section 312 along its axial direction and in the material conveying direction. The fourth port 313 and the fifth port 314 are respectively connected to the inlet pipe section 311. The nozzle assembly 32 is disposed at the fourth port 313 and extends into the inlet pipe section 311 along the axial direction of the mixing pipe 31. The fourth port 313 is connected to the second port 112 through the nozzle assembly 32. The inner diameter of the nozzle assembly 32 gradually decreases along the axial direction of the mixing pipe 31 and in the material conveying direction. According to Bernoulli's theorem, the flow rate of the material fluid in the nozzle assembly 32 gradually increases along the conveying direction. Through the above arrangement, the solvent can be sprayed and impacted through the end of the nozzle component 32 to form a high-speed liquid flow into the inlet pipe section 311, and a low-pressure area can be formed at the inlet pipe section 311, so that the powder delivered at the fifth port 314 is sucked into the mixing pipe 31 and fully mixed with the solvent, and finally delivered to the sixth port 315 through the outlet pipe section 312.

[0044] Specifically, the outlet pipe section 312 is a venturi tube structure, and further reference is made to Figure 4The sixth port 315 is connected to the outlet pipe section 312. The outlet pipe section 312 includes, in sequence, a contraction section 3121, a throat section 3122, and a diffusion section 3123 along the axial direction of the mixing pipe 31 and in the material conveying direction. The inner diameter of the contraction section 3121 gradually decreases along the axial direction of the mixing pipe 31 and in the material conveying direction. According to Bernoulli's theorem, the flow velocity of the material fluid within the contraction section 3121 gradually increases along the conveying direction. The section with the largest inner diameter of the contraction section 3121 is connected to the inlet pipe section 311. The inner diameter of the diffusion section 3123 gradually increases along the axial direction of the mixing pipe 31 and in the material conveying direction. According to Bernoulli's theorem, the pressure of the material fluid within the diffusion section 3123 gradually increases along the conveying direction. The section with the largest inner diameter of the diffusion section 3123 is connected to the sixth port 315. The inner diameter of the throat 3122 is smaller than the minimum inner diameter of the contraction section 3121 and smaller than the minimum inner diameter of the diffusion section 3123. The two ends of the throat 3122 are respectively connected to the pipe section with the minimum inner diameter of the contraction section 3121 and the pipe section with the minimum inner diameter of the diffusion section 3123. According to Bernoulli's theorem, the flow rate of the material fluid at the throat 3122 is the largest.

[0045] The embodiment of the present invention can achieve the mixing and pushing of solvent and rubber powder by setting a venturi ejector. It is understandable that the technology of the venturi ejector is very mature and will not be described in detail here.

[0046] like Figure 3 、 Figure 5 and Figure 6 As shown, the dispersion mechanism 4 includes a chamber 41, a first rotating shaft 42, and a third motor 46. The chamber 41 has a seventh port 411 and an eighth port 412, which are respectively connected to the interior of the chamber 41. The seventh port 411 is connected to the sixth port 315, and the eighth port 412 is connected to the first port 111. The chamber 41 is provided with a dispersion component 43 and a centrifugal component 44. The dispersion component 43 and the centrifugal component 44 are respectively connected to the first rotating shaft 42 along the axial direction and in the material conveying direction. The starting end of the first rotating shaft 42 is drivingly connected to the drive shaft of the third motor 46. Under the drive of the third motor 46, the first rotating shaft 42 can simultaneously drive the dispersion component 43 and the centrifugal component 44 to rotate. In addition, compared with the solution of separately providing a shear pump and a centrifugal pump, the dispersion mechanism 43 of the present invention combines the functions of a shear pump and a centrifugal pump. The dispersion mechanism 43 of the present invention can replace the shear pump and the centrifugal pump, thereby reducing the installation space of the equipment and improving space utilization.

[0047] Further, continue to refer to Figure 5 and Figure 6As shown, the dispersing component 43 includes a stator 431 and a rotor 432. The stator 431 is fixedly disposed within the chamber 41 and rotates in conjunction with the rotor 432. The rotor 432 is connected to the first rotating shaft 42 and can disperse the material by rotation. Specifically, the stator 431 is formed with a plurality of first shearing teeth spaced apart along its circumference, and the rotor 432 is formed with a plurality of second shearing teeth spaced apart along its circumference. During the rotation of the rotor 432 relative to the stator 431, the walls of the second shearing teeth can be aligned with or offset from the walls of the first shearing teeth. The second shearing teeth and the first shearing teeth are used to mix, shear, and disperse the powder and liquid materials. The centrifugal component 44 includes a centrifugal impeller 441, which is connected to the first rotating shaft 42 and can convey the material by rotation.

[0048] Further, continue to refer to Figure 5 and Figure 6 There are multiple dispersing components 43, and the multiple dispersing components 43 are arranged along the axial direction of the first rotating shaft 42. In this embodiment, there are two dispersing components 43. It should be noted that the number of dispersing components 43 is not limited to the two shown in the figure, and can be one, three, four, etc. The appropriate number of dispersing components 43 can be selected based on the mixing and shear dispersion requirements of the powder and liquid materials in actual applications.

[0049] Further, continue to refer to Figure 5 and Figure 6 A guide component 45 is provided in the seventh port 411. The guide component 45 includes a spiral blade 451. The spiral blade 451 can guide the material into the chamber 41 by rotating. The spiral blade 451 is mounted at the end of the first rotating shaft 42, so that the first rotating shaft 42 can drive the spiral blade 451 to rotate. By disposing the guide component 45 at the seventh port 411, the spiral blade 451 can guide the powder and liquid material into the chamber 41 and stir the powder and liquid material at the seventh port 411 to a certain extent, thereby preventing the powder and liquid material from being blocked at the seventh port 411 during transportation.

[0050] Further, continue to refer to Figure 5 The seventh port 411 is opened along the axial direction of the first rotating shaft 42, and the eighth port 412 is opened along the radial direction of the first rotating shaft 42 and is arranged corresponding to the centrifugal impeller 441. In the embodiment of the utility model, by arranging the eighth port 412 and the centrifugal impeller 441 correspondingly, when the centrifugal impeller 441 rotates at a high speed, the powder and liquid materials will be thrown outward in the radial direction of the centrifugal impeller 441 after contacting the centrifugal impeller 441 under the action of centrifugal force, thereby being accelerated and transported to the glue circulation tank 1 through the eighth port 412.

[0051] The operating principle of the dispersing mechanism 4 of the present embodiment is as follows: First, the third motor 46 is activated, so that its drive shaft, via the first rotating shaft 42, simultaneously drives the rotor 432 of the dispersing component 43 and the centrifugal impeller 441 of the centrifugal component 44 to rotate. Then, the powder and liquid material enters the chamber 41 through the seventh port 411. The high-speed rotation of the centrifugal impeller 441 creates a low-pressure zone at its center, which draws the powder and liquid material into the impeller 441, allowing the material to be transported through the dispersing component 43 to the centrifugal component 44. This enables the dispersing mechanism 4 to achieve self-absorption of the powder and liquid material. As the powder and liquid material passes through the dispersing component 43, the rotor 432 rotates relative to the stator 431, causing the material to be mixed, sheared, and dispersed. Subsequently, when the powder and liquid material reaches the centrifugal component 44, the high-speed rotation of the centrifugal impeller 441 ejects the material radially outward, accelerating its transport to the glue circulation tank 1.

[0052] The present invention provides a mixing mechanism 3 and a dispersing mechanism 4, enabling the mixing mechanism 3 to mix the rubber powder and solvent within the system, and enabling the dispersing mechanism 4 to disperse the rubber material within the system. Compared to the prior art solution of installing high-speed and low-speed dispersing paddles within the rubber storage tank, the present invention replaces the high-speed and low-speed dispersing paddles by providing the mixing mechanism 3 and the dispersing mechanism 4, thereby eliminating the need for corresponding dispersing paddles on the rubber circulation tank 1 and reducing the investment cost of the rubber circulation tank 1. At the same time, the mixing mechanism 3 and the dispersing mechanism 4 can more efficiently mix and disperse the rubber material, reducing rubber production time and thereby increasing rubber material production capacity.

[0053] like Figure 3 As shown, a first check valve 810 and a fifth valve 805 are sequentially provided on the pipe section between the first port 111 and the eighth port 412. The primary function of the first check valve 810 is to allow material fluid to flow from the eighth port 412 to the first port 111, while preventing material fluid from flowing in the opposite direction. The fifth valve 805 is used to control the open and closed state of the pipe section between the eighth port 412 and the first port 111.

[0054] Continue to refer Figure 3 A second temperature sensor 6 is provided on the pipe section near the eighth port 412 , and the second temperature sensor 6 is used to detect the temperature of the material in the pipe section near the eighth port 412 . Specifically, the second temperature sensor 6 is provided on the pipe section between the eighth port 412 and the first check valve 810 .

[0055] Continue to refer Figure 3A pressure sensor 7 is further provided on the pipe section near the eighth port 412, and the pressure sensor 7 is used to detect the material pressure in the pipe section near the eighth port 412. Specifically, the pressure sensor 7 is provided on the pipe section between the eighth port 412 and the first check valve 810.

[0056] Continue to refer Figure 3 The glue making system further includes a pipe cooler 5, which is sleeved on the pipe section between the eighth port 412 and the first port 111. Specifically, the pipe section cooler is provided on the pipe section between the fifth valve 805 and the first port 111.

[0057] Further, continue to refer to Figure 3 The pipe cooler 5 includes a liquid inlet 51 and a liquid outlet 52. A seventh valve 807 is provided at the liquid inlet 51 so that the seventh valve 807 can control the opening and closing state of the liquid inlet 51. A second check valve 811 and an eighth valve 808 are provided at the liquid outlet 52 in sequence so that the eighth valve 808 can control the opening and closing state of the liquid outlet 52. The main function of the second check valve 811 is to allow the coolant to flow from the liquid inlet 51 to the liquid outlet 52, while preventing the coolant from flowing in the opposite direction. By providing the pipe cooler 5, the embodiment of the utility model can reduce the temperature of the material in the glue making system and prevent the material temperature from being too high.

[0058] The process flow of the rapid glue making system of the embodiment of the utility model is as follows:

[0059] S101, according to the formulation requirements of the rubber material, corresponding solvent and rubber powder are added to the rubber circulation tank 1 and the powder tank 2 respectively in proportion;

[0060] S102, opening the third valve 803, the fifth valve 805 and the sixth valve 806 respectively;

[0061] S103, starting the dispersion mechanism 4, and driving the centrifugal component 44 of the dispersion mechanism 4, causing the solvent to circulate in the system pipeline;

[0062] S104, opening the fourth valve 804 and starting the rotary feeding valve 812, the rubber powder is fed to the mixing mechanism 3 under the action of the rotary feeding valve 812, and the rubber powder and the solvent are mixed in the mixing mechanism 3 to obtain a powder-liquid material;

[0063] S105, the powder material is transported from the mixing mechanism 3 to the dispersing mechanism 4, and is quickly dispersed by the dispersing components 43 of the dispersing mechanism 4, thereby forming a uniform rubber material, which is then transported to the rubber circulation tank 1 for continued circulation of the rubber material;

[0064] S106 , after the rubber material circulates multiple times in the rubber making system, the finished rubber material is discharged through the discharge port 114 of the rubber making circulation tank 1 .

[0065] Thus far, the technical solutions of the present invention have been described in conjunction with the preferred embodiments shown in the accompanying drawings. However, it is readily understood by those skilled in the art that the scope of protection of the present invention is obviously not limited to these specific embodiments. Without departing from the principles of the present invention, those skilled in the art may make equivalent changes or substitutions to the relevant technical features, and the technical solutions after such changes or substitutions will fall within the scope of protection of the present invention.

Claims

1. A rapid glue making system, characterized in that: The glue making system comprises: A glue circulation tank comprises a first tank body, the first tank body having a first port and a second port, the first port and the second port being respectively communicated with the interior of the first tank body; A powder tank comprising a second tank body, wherein the second tank body has a third port, and the third port is in communication with the interior of the second tank body; a mixing mechanism having a fourth port, a fifth port, and a sixth port, wherein the fourth port, the fifth port, and the sixth port are respectively in communication with an interior of the mixing mechanism, the fourth port is in communication with the second port, and the fifth port is in communication with the third port; A dispersion mechanism includes a chamber and a first rotating shaft, the chamber having a seventh port and an eighth port, the seventh port and the eighth port being respectively connected to the interior of the chamber, the seventh port being connected to the sixth port, and the eighth port being connected to the first port, a dispersion component being provided in the chamber, and the first rotating shaft being connected to the dispersion component, thereby being able to drive the dispersion component to rotate to disperse the material.

2. The rapid glue making system according to claim 1, characterized in that: The mixing mechanism is a venturi ejector, which includes a mixing pipe and a nozzle component. The mixing pipe includes an inlet pipe section and an outlet pipe section in sequence along its axial direction. The fourth port and the fifth port are respectively connected to the inlet pipe section. The nozzle component is arranged at the fourth port and extends into the inlet pipe section along the axial direction of the mixing pipe. The fourth port is connected with the second port through the nozzle component. The inner diameter of the nozzle component gradually decreases along the axial direction of the mixing pipe. The outlet pipe section is a Venturi tube structure, and the sixth port is connected with the outlet pipe section.

3. The rapid glue making system according to claim 2, characterized in that: The outlet pipe section includes a contraction section, a throat section and a diffusion section in sequence along the axial direction of the mixing pipe. The inner diameter of the contraction section gradually decreases along the axial direction of the mixing pipe, and the pipe section with the largest inner diameter of the contraction section is connected to the inlet pipe section. The inner diameter of the diffusion section gradually increases along the axial direction of the mixing pipe, and the pipe section with the largest inner diameter of the diffusion section is connected to the sixth port. The inner diameter of the throat is smaller than the minimum inner diameter of the contraction section and smaller than the minimum inner diameter of the diffusion section. Both ends of the throat are connected to the pipe section with the minimum inner diameter of the contraction section and the pipe section with the minimum inner diameter of the diffusion section respectively.

4. The rapid glue making system according to claim 1, characterized in that: The dispersing component includes a stator and a rotor. The stator is fixedly disposed in the chamber. The stator and the rotor are rotationally matched. The rotor is connected to the first rotating shaft. The rotor can disperse the material by rotating.

5. The rapid glue making system according to claim 1, characterized in that: A centrifugal component is also provided in the chamber, and the first rotating shaft is connected to the centrifugal component, so as to drive the centrifugal component to rotate to transport materials.

6. The rapid glue making system according to claim 5, characterized in that: The centrifugal component includes a centrifugal impeller, which is connected to the first rotating shaft and can transport materials by rotating.

7. The rapid glue making system according to claim 1, characterized in that: The glue making system further includes a pipeline cooler, which is sleeved on the pipe section between the eighth port and the first port.

8. The rapid glue making system according to claim 1, characterized in that: The glue making circulation tank further includes a first temperature sensor, which is arranged on the first tank body and is used to detect the temperature of the material in the first tank body.

9. The rapid glue making system according to claim 1, characterized in that: A second temperature sensor is provided on the pipe section close to the eighth port, and the second temperature sensor is used to detect the temperature of the material in the pipe section close to the eighth port.

10. The rapid glue making system according to claim 1, characterized in that: The glue-making circulation tank also includes an anchor stirring paddle and a second rotating shaft, the second rotating shaft is connected to the anchor stirring paddle, the anchor stirring paddle is arranged in the first tank body and close to the inner bottom thereof, and the anchor stirring paddle can stir the material by rotating.

Images