Carbon material natural rubber composite reaction chamber

Abstract

The application discloses a kind of carbon material natural latex composite reaction chamber, it includes: composite reaction chamber, and carbon black slurry input pipe and natural latex input pipe are connected on composite reaction chamber;Mixing unit is arranged in composite reaction chamber, for carbon black slurry and natural latex are mixed to form mixed solution;Flow guide unit is arranged below mixing unit, for guiding mixed solution;Stirring unit is arranged below flow guide unit, for the stirring re-mixing of mixed solution;Control unit includes acquisition module, processing module and control module, control unit is arranged in composite reaction chamber, for automatically controlling the mixing unit, flow guide unit and stirring unit work.The application is mixed by setting mixing unit to carbon black slurry and natural latex is preliminarily mixed, then after stirring unit is stirred and mixed again, make carbon black be fully dispersed in natural latex, to improve the performance of rubber, and flow guide unit can refine large particle in mixed solution into small particle.

Description

Technical Field

[0001] This invention relates to the field of chemical reaction equipment technology, and in particular to a carbon-based natural latex composite reaction chamber. Background Technology

[0002] Rubber compounding is a bottleneck in rubber processing technology and a key factor in the performance of rubber products. The energy consumption of rubber compounding is enormous, accounting for almost 40% of the total energy consumption in rubber product production. Therefore, technological innovation in rubber compounding processes has attracted considerable attention in recent years, with wet compounding technology being a recent research focus. "Wet compounding" is a method of adding fillers such as carbon black and silica to rubber while it is still in its latex state (natural or synthetic latex), thoroughly mixing and dispersing it through stirring, and then producing a compound through flocculation (co-precipitation). The polymer-filler homogeneous dispersion prepared by this method is called "co-precipitated rubber." Compared with dry compounding, wet compounding has the following advantages: 1. It can significantly reduce the energy consumption of rubber compounding and lower costs (by reducing the number of compounding stages and compounding time); 2. It can significantly improve the dispersion of various reinforcing fillers in the rubber polymer, and the physical properties of the compound, such as tensile strength, elasticity, heat generation, and rolling resistance, are greatly improved; 3. It can significantly reduce dust pollution; 4. It is conducive to the realization of advanced continuous compounding processes.

[0003] However, existing compounding reaction chambers suffer from insufficient mixing. Due to the incompatibility between carbon black slurry and natural latex, existing compounding reaction chambers make it difficult to fully mix the carbon black slurry and natural latex. This results in carbon black being difficult to co-precipitate with natural latex, uneven dispersion of carbon black in natural latex, and the presence of particulate matter that is difficult to decompose. Consequently, the carbon black filling amount in the compound fluctuates greatly, and the dispersion uniformity is poor. Therefore, the compound cannot have good performance, making it difficult to promote the wet rubber compounding process and apply it on a large industrial scale. Summary of the Invention

[0004] The technical problem to be solved by the present invention is that the reaction chamber in the prior art is difficult to fully mix carbon black slurry and natural rubber latex.

[0005] To solve the above-mentioned technical problems, the present invention provides a carbon-based natural latex composite reaction chamber, comprising:

[0006] A composite reaction chamber, on which a carbon black slurry inlet pipe and a natural latex inlet pipe are connected;

[0007] A mixing unit, located in the composite reaction chamber, is used to mix carbon black slurry and natural latex to form a mixture;

[0008] A flow guiding unit is disposed below the mixing unit for guiding the mixture;

[0009] A stirring unit is located below the flow guiding unit and is used to stir and remix the mixture.

[0010] The control unit includes a data acquisition module, a processing module, and a control module. The control unit is located in the composite reaction chamber and is used to automatically control the operation of the mixing unit, the flow guiding unit, and the stirring unit.

[0011] Furthermore, the mixing unit includes:

[0012] A mixing box is located in the composite reaction chamber and is connected to the carbon black slurry input pipe and the natural latex input pipe;

[0013] A high-pressure input pump is installed on the carbon black slurry input pipe. The high-pressure input pump is used to control the flow rate and input pressure of the carbon black slurry input into the mixing tank.

[0014] A natural latex flow detector is installed on the natural latex input pipe, and the natural latex flow detector is used to detect the flow rate of natural latex input into the mixing tank;

[0015] The acquisition module is electrically connected to the natural latex flow detector, and the control module is electrically connected to the high-pressure input pump.

[0016] Furthermore, the stirring unit includes:

[0017] A mixing tank is located within the composite reaction chamber;

[0018] A stirring shaft is installed inside the mixing tank and is used to stir the mixture at a certain speed.

[0019] The flow guiding unit includes:

[0020] A mixture flow detector is installed above the mixing tank to detect the flow rate of the mixture flowing into the mixing tank;

[0021] The acquisition module is electrically connected to the mixed liquid flow detector, and the control module is electrically connected to the stirring shaft.

[0022] Furthermore, the acquisition module is used to acquire the flow rate ΔG of natural latex flowing into the mixing tank in real time, and the control module is used to control the high-pressure input pump;

[0023] The processing module is used to set the preset flow rate value G0 of standard natural latex. The processing module is also used to set the first preset flow rate difference g1, the second preset flow rate difference g2, the third preset flow rate difference g3, and the fourth preset flow rate difference g4 of natural latex, where g1 < g2 < g3 < g4. The processing module is also used to set the first preset working condition matrix A1 (a1, b1), the second preset working condition matrix A2 (a2, b2), the third preset working condition matrix A3 (a3, b3), and the fourth preset working condition matrix A4 (a4, b4), where a1 to a4 are the first to fourth preset input flow rates, where a1 < a2 < a3 < a4, and b1 to b4 are the first to fourth preset input pressures, where b1 < b2 < b3 < b4.

[0024] The preset working condition matrix A is selected as the working condition of the high-pressure input pump based on the difference between the flow rate ΔG of the natural latex flowing into the carbon black slurry input unit and the preset value G0 of the standard natural latex flow rate.

[0025] When △G-G0≤g1, the first preset working condition matrix A1 is selected as the working condition of the high-pressure input pump;

[0026] When g1 < △G - G0 ≤ g2, the second preset working condition matrix A2 is selected as the working condition of the high-pressure input pump;

[0027] When g2 < △G - G0 ≤ g3, the third preset working condition matrix A3 is selected as the working condition of the high-pressure input pump;

[0028] When g3 < △G - G0 ≤ g4, the fourth preset working condition matrix A4 is selected as the working condition of the high-pressure input pump.

[0029] When the i-th preset working condition matrix Ai is selected as the working condition of the high-pressure input pump, the control module controls the high-pressure input pump to work with the i-th preset input flow rate ai, and the control module will also control the high-pressure input pump to work with the i-th preset input pressure bi, i = 1, 2, 3, 4.

[0030] Furthermore, the acquisition module is also used to acquire the flow rate ΔS of the mixture above the mixing tank in real time, and the control module is used to control the stirring shaft;

[0031] The acquisition module is used to set a preset value S0 for the standard mixed liquid flow rate. The acquisition module is also used to set a first preset mixed liquid flow rate difference s1, a second preset mixed liquid flow rate difference s2, a third preset mixed liquid flow rate difference s3, and a fourth preset mixed liquid flow rate difference s4, where s1 < v2 < s3 < s4. The processing module is also used to set a first preset working condition matrix W1(d1, e1), a second preset working condition matrix W2(d2, e2), a third preset working condition matrix W3(d3, e3), and a fourth preset working condition matrix W4(d4, e4), where d1 to d4 are the first to fourth preset stirring speeds, and d1 < d2 < d3 < d4, and e1 to e4 are the first to fourth preset stirring times, and e1 < e2 < e3 < e4.

[0032] The working conditions of the stirring shaft are selected based on the difference between the flow rate ΔS of the mixture above the mixing tank and the preset value G0 of the standard flow rate of the mixture.

[0033] When △S-S0≤g1, the first preset working condition matrix W1 is selected as the working condition of the stirring shaft.

[0034] When s1 < △S-S0 ≤ s2, the second preset working condition matrix W2 is selected as the working condition of the stirring shaft.

[0035] When s2<△S-S0≤s3, the third preset working condition matrix W3 is selected as the working condition of the stirring shaft;

[0036] When s3 < △S - S0 ≤ s4, the fourth preset working condition matrix W4 is selected as the working condition of the stirring shaft.

[0037] When the i-th preset working condition matrix Wi is selected as the working condition of the stirring shaft, the control module controls the stirring shaft to work at the i-th preset stirring speed di, and the control module controls the stirring time of the stirring shaft to be set to the i-th preset stirring time ei, i = 1, 2, 3, 4.

[0038] Furthermore, the mixing unit includes:

[0039] A spray head, located at the top of the mixing chamber, is used to spray carbon black slurry;

[0040] An electronic switching valve is located at the bottom of the mixing tank and is electrically connected to the control module, used to control the opening and closing of the bottom outlet of the mixing tank.

[0041] Furthermore, the flow guiding unit also includes:

[0042] A guide tube, connected below the mixing unit, is used to guide the mixture;

[0043] A flow guide tube, located below the flow guide pipe and connected to the stirring unit, is used to refine particulate matter in the mixture.

[0044] Furthermore, a mixture outlet pipe is connected to one side of the mixing tank, which is used to discharge the mixed liquid after mixing.

[0045] Furthermore, the spray head is provided with multiple jet nozzles, which are used to spray carbon black slurry into the mixing box.

[0046] Compared with the prior art, the carbon-material natural latex composite reaction chamber of this invention has the following advantages:

[0047] This invention uses a mixing unit to initially mix carbon black slurry and natural latex, followed by a stirring unit for secondary mixing, which ensures that the carbon black is fully dispersed in the natural latex, thereby improving the performance of the rubber. Furthermore, the flow guiding unit can refine large particles in the mixture into smaller particles. Attached Figure Description

[0048] Figure 1 This is a schematic diagram of the structure of the carbon material-natural latex composite reaction chamber in an embodiment of the present invention;

[0049] Figure 2 This is a schematic diagram of the mixing unit of the carbon material natural latex composite reaction chamber in an embodiment of the present invention;

[0050] Figure 3 This is a schematic diagram of the stirring unit of the carbon material natural latex composite reaction chamber in an embodiment of the present invention;

[0051] Figure 4 This is a schematic diagram of the flow guiding unit of the carbon material natural latex composite reaction chamber in an embodiment of the present invention;

[0052] Figure 5 This is a schematic diagram of the control unit structure of the carbon material natural latex composite reaction chamber in an embodiment of the present invention.

[0053] In the diagram, 1. Composite reaction chamber; 2. Mixing unit; 3. Flow guiding unit; 4. Stirring unit; 5. Control unit; 6. Carbon black slurry input pipe; 7. Natural latex input pipe; 8. High-pressure input pump; 9. Natural latex flow detector; 10. Mixing box; 11. Spray head; 12. Electronic switch valve; 13. Stirring box; 14. Stirring shaft; 15. Flow guiding pipe; 16. Mixed liquid flow detector; 17. Flow guiding cylinder; 18. Mixed liquid outflow pipe; 19. Jet nozzle. Detailed Implementation

[0054] The specific embodiments of the present invention will be described in further detail below with reference to the accompanying drawings and examples. The following examples are for illustrative purposes only and are not intended to limit the scope of the invention.

[0055] In the description of this application, it should be understood that the terms "center", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this application.

[0056] The terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance or implicitly specifying the number of technical features indicated. Therefore, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of this application, unless otherwise stated, "a plurality of" means two or more.

[0057] In the description of this application, it should be noted that, unless otherwise expressly specified and limited, the terms "installation," "connection," and "linking" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to the internal connection between two components. Those skilled in the art can understand the specific meaning of the above terms in this application based on the specific circumstances.

[0058] like Figure 1 As shown in the embodiments of this application, a carbon material natural latex composite reaction chamber is provided, including: a composite reaction chamber 1, a mixing unit 2, a flow guiding unit 3, a stirring unit 4, and a control unit 5.

[0059] Specifically, carbon black slurry input pipe 6 and natural latex input pipe 7 are respectively connected to both sides of the composite reaction chamber 1, and the carbon black slurry input pipe 6 and natural latex input pipe 7 are connected to the mixing box 10 inside the composite reaction chamber 1.

[0060] Specifically, the mixing unit 2 is disposed in the composite reaction chamber 1, specifically in the upper part of the composite reaction chamber 1. The mixing unit 2 is connected to the carbon black slurry inlet pipe 6 and the natural latex inlet pipe 7. The mixing unit 2 is used to mix the flowing carbon black slurry and natural latex to form a preliminary mixture.

[0061] Specifically, the flow guiding unit 3 is located below the mixing unit 2 and is connected to the mixing unit 2. The flow guiding unit 3 is used to guide the preliminary mixture into the stirring unit 4, and in this process, it can also refine the larger particles in the preliminary mixture to improve the mixing effect.

[0062] Specifically, the stirring unit 4 is located below the flow guiding unit 3, and the stirring unit 4 is directly connected to the flow guiding cylinder 17 in the flow guiding unit 3 above. The stirring unit 4 is used to stir the mixture after the initial mixing multiple times, so that the mixture is mixed again.

[0063] Specifically, the control unit 5 includes a data acquisition module, a processing module, and a control module. The data acquisition module is used to acquire data, the processing module is used to process data, and the control module is used to control the operation of each device. The control unit 5 is located in the composite reaction chamber 1 and is used to automatically control the specific operating parameters and operating status of the mixing unit 2, the flow guiding unit 3, and the stirring unit 4.

[0064] Specifically, the present invention uses the mixing unit 2 to initially mix carbon black slurry and natural latex, and then uses the stirring unit 4 to perform secondary mixing, so that the carbon black is fully dispersed in the natural latex, thereby improving the performance of the rubber. In addition, the flow guiding unit 3 can refine large particles in the mixture into small particles, which greatly improves the mixing of carbon black slurry and natural latex.

[0065] like Figure 2 As shown in the embodiments of this application, a carbon-based natural latex composite reaction chamber is provided, wherein the mixing unit 2 includes:

[0066] Mixing box 10 is located inside the composite reaction chamber 1 and is connected to the carbon black slurry input pipe 6 and the natural latex input pipe 7;

[0067] A high-pressure input pump 8 is installed on the carbon black slurry input pipe 6. The high-pressure input pump 8 is used to control the flow rate and input pressure of the carbon black slurry input into the mixing box 10.

[0068] Specifically, the high-pressure input pump 8 is installed on the carbon black slurry input pipe 6 outside the composite reaction chamber 1. The high-pressure input pump 8 has the function of adjusting the flow rate and pressure of the carbon black slurry, so that the carbon black slurry can enter the mixing box 10 at a certain flow rate and pressure and be mixed with the natural latex in the mixing box 10.

[0069] A natural latex flow detector 9 is installed on the natural latex input pipe 7. The natural latex flow detector 9 is used to detect the flow rate of natural latex input into the mixing tank 10.

[0070] Specifically, the natural latex flow detector 9 is installed on the natural latex input pipe 7 outside the composite reaction chamber 1, and can measure the flow rate of natural latex flowing through the natural latex input pipe 7 in real time;

[0071] The acquisition module is electrically connected to the natural latex flow detector 9, and the control module is electrically connected to the high-pressure input pump 8.

[0072] Specifically, in this application, natural latex first enters the mixing box 10, and then the high-pressure input pump 8 is turned on to inject carbon black slurry into the mixing box 10 at a certain flow rate and pressure, so that the carbon black slurry can be dispersed in the natural latex and mixed better.

[0073] like Figure 3 As shown in the embodiments of this application, a carbon-based natural latex composite reaction chamber is provided, wherein the stirring unit 4 includes:

[0074] The mixing tank 13 is located inside the composite reaction chamber 1;

[0075] Specifically, the mixing tank 13 is located at the bottom of the composite reaction chamber 1. The mixing of the mixture in the mixing tank 13 is the last step in the mixing process. The mixing of the mixture in the mixing tank 13 will further increase the dispersibility of the carbon black slurry in the natural latex and improve the performance of the obtained rubber.

[0076] A stirring shaft 14 is disposed inside the mixing tank 13 and is used to stir the mixture at a certain speed.

[0077] Specifically, the stirring shaft 14 is vertically arranged inside the mixing tank 13. When the mixture enters the mixing tank 13, the stirring shaft 14 is activated to stir the mixture at a certain speed to ensure that it is fully mixed.

[0078] like Figure 4 As shown, the flow guiding unit 3 includes:

[0079] A mixture flow detector 16 is disposed above the mixing tank 13 and is used to detect the flow rate of the mixture flowing into the mixing tank 13;

[0080] The acquisition module is electrically connected to the mixed liquid flow detector 16, and the control module is electrically connected to the stirring shaft 14.

[0081] In an embodiment of this application, a carbon-based natural latex composite reaction chamber is provided. The acquisition module is used to acquire the flow rate ΔG of the natural latex flowing into the mixing tank 10 in real time, and the control module is used to control the high-pressure input pump 8.

[0082] The processing module is used to set the preset flow rate value G0 of standard natural latex. The processing module is also used to set the first preset flow rate difference g1, the second preset flow rate difference g2, the third preset flow rate difference g3, and the fourth preset flow rate difference g4 of natural latex, where g1 < g2 < g3 < g4. The processing module is also used to set the first preset working condition matrix A1 (a1, b1), the second preset working condition matrix A2 (a2, b2), the third preset working condition matrix A3 (a3, b3), and the fourth preset working condition matrix A4 (a4, b4), where a1 to a4 are the first to fourth preset input flow rates, where a1 < a2 < a3 < a4, and b1 to b4 are the first to fourth preset input pressures, where b1 < b2 < b3 < b4.

[0083] The preset working condition matrix A is selected as the working condition of the high-pressure input pump 8 based on the difference between the flow rate ΔG of the natural latex flowing into the carbon black slurry input unit and the preset value G0 of the standard natural latex flow rate.

[0084] When △G-G0≤g1, the first preset working condition matrix A1 is selected as the working condition of the high-pressure input pump 8;

[0085] When g1 < △G-G0 ≤ g2, the second preset working condition matrix A2 is selected as the working condition of the high-pressure input pump 8;

[0086] When g2 < △G - G0 ≤ g3, the third preset working condition matrix A3 is selected as the working condition of the high-pressure input pump 8;

[0087] When g3 < △G - G0 ≤ g4, the fourth preset working condition matrix A4 is selected as the working condition of the high-pressure input pump 8;

[0088] When the i-th preset working condition matrix Ai is selected as the working condition of the high-pressure input pump 8, the control module controls the high-pressure input pump 8 to work with the i-th preset input flow rate ai, and the control module will also control the high-pressure input pump 8 to work with the i-th preset input pressure bi, i = 1, 2, 3, 4.

[0089] Specifically, the operating conditions of the high-pressure input pump 8 are selected based on the difference between the flow rate of natural latex flowing into the carbon black slurry input unit and the preset value of the standard natural latex flow rate, so that the carbon black slurry and natural latex are mixed in a certain proportion. Furthermore, the high-pressure input pump 8 adjusts the pumping pressure of the carbon black slurry according to the amount of natural latex, so that the carbon black slurry enters the natural latex at a certain speed, achieving a good dispersion effect and improving dispersibility.

[0090] In an embodiment of this application, a carbon material natural latex composite reaction chamber is provided. The acquisition module is also used to acquire the flow rate ΔS of the mixed liquid above the mixing tank 13 in real time, and the control module is used to control the stirring shaft 14.

[0091] The acquisition module is used to set a preset value S0 for the standard mixed liquid flow rate. The acquisition module is also used to set a first preset mixed liquid flow rate difference s1, a second preset mixed liquid flow rate difference s2, a third preset mixed liquid flow rate difference s3, and a fourth preset mixed liquid flow rate difference s4, where s1 < v2 < s3 < s4. The processing module is also used to set a first preset working condition matrix W1(d1, e1), a second preset working condition matrix W2(d2, e2), a third preset working condition matrix W3(d3, e3), and a fourth preset working condition matrix W4(d4, e4), where d1 to d4 are the first to fourth preset stirring speeds, and d1 < d2 < d3 < d4, and e1 to e4 are the first to fourth preset stirring times, and e1 < e2 < e3 < e4.

[0092] The working conditions of the stirring shaft 14 are selected based on the difference between the flow rate ΔS of the mixture above the mixing tank 13 and the preset value G0 of the standard mixture flow rate.

[0093] When △S-S0≤g1, the first preset working condition matrix W1 is selected as the working condition of the stirring shaft 14.

[0094] When s1 < △S-S0 ≤ s2, the second preset working condition matrix W2 is selected as the working condition of the stirring shaft 14.

[0095] When s2 < △S - S0 ≤ s3, the third preset working condition matrix W3 is selected as the working condition of the stirring shaft 14.

[0096] When s3 < △S - S0 ≤ s4, the fourth preset working condition matrix W4 is selected as the working condition of the stirring shaft 14.

[0097] When the i-th preset working condition matrix Wi is selected as the working condition of the stirring shaft 14, the control module controls the stirring shaft 14 to work at the i-th preset stirring speed di, and the control module controls the stirring time of the stirring shaft 14 to be set to the i-th preset stirring time ei, i = 1, 2, 3, 4.

[0098] Specifically, the working conditions of the stirring shaft 14 are selected based on the difference between the flow rate of the mixed liquid above the mixing tank 13 and the preset value of the standard mixed liquid flow rate. This allows the stirring shaft 14 to set its operating parameters according to the amount of mixed liquid, so as to fully stir the mixed liquid at the optimal stirring speed and stirring time, ensuring that the mixed liquid is fully mixed.

[0099] In an embodiment of this application, a carbon-based natural latex composite reaction chamber is provided, wherein the mixing unit 2 includes:

[0100] Spray head 11 is located at the top inside the mixing box 10 and is used to spray carbon black slurry;

[0101] An electronic switching valve 12 is located at the bottom of the mixing tank 10 and is electrically connected to the control module for controlling the opening and closing of the bottom outlet of the mixing tank 10.

[0102] Specifically, the bottom outlet of the mixing tank 10 is normally closed. When the carbon black slurry is sprayed into the natural latex through the spray head 11 and mixed in the mixing tank 10, the control module controls the electronic switch valve 12 to open the bottom outlet of the mixing tank 10, allowing the mixture to enter the next process.

[0103] In an embodiment of this application, a carbon-based natural latex composite reaction chamber is provided, wherein the flow guiding unit 3 further includes:

[0104] The guide pipe 15 is connected below the mixing unit 2 and is used to guide the mixture.

[0105] The guide tube 17 is located below the guide pipe 15 and is connected to the stirring unit 4, and is used to refine the particulate matter in the mixture.

[0106] Specifically, the guide tube 17 has a conical structure, resembling a funnel. Due to the large cross-section of the guide tube 15 and the slow flow rate, larger solid particles in the mixture will move downwards. When they move downwards into the guide tube 17, the cross-section becomes smaller, and the upward flow rate of the mixture increases, causing the solid particles to be swept up and move upwards. This process is repeated until they dissolve into smaller particles. This prevents excessive large solid particles from entering the mixing tank 13 and forming sediment that could block the inlet of the mixing tank 13. As a result, the solid particles in the mixture entering the mixing tank 13 are smaller, thus eliminating sedimentation problems during operation.

[0107] In an embodiment of this application, a carbon material natural latex composite reaction chamber is provided. A mixing tank 13 is connected to a mixed liquid outlet pipe 18 on one side, which is used to discharge the mixed liquid after stirring.

[0108] In an embodiment of this application, a carbon material natural latex composite reaction chamber is provided, wherein the spray head 11 is provided with a plurality of jet nozzles 19, which are used to spray carbon black slurry into the mixing box 10.

[0109] In summary, this invention provides a carbon-based natural latex composite reaction chamber, comprising: a composite reaction chamber 1, with a carbon black slurry input pipe 6 and a natural latex input pipe 7 connected to the composite reaction chamber 1; a mixing unit 2, disposed within the composite reaction chamber 1, for mixing the carbon black slurry and natural latex to form a mixture; a flow guiding unit 3, disposed below the mixing unit 2, for guiding the mixture; a stirring unit 4, disposed below the flow guiding unit 3, for stirring and remixing the mixture; and a control unit 5, including a data acquisition module, a processing module, and a control module, disposed within the composite reaction chamber 1, for automatically controlling the operation of the mixing unit 2, the flow guiding unit 3, and the stirring unit 4. This invention uses the mixing unit 2 to initially mix the carbon black slurry and natural latex, followed by a secondary stirring and mixing by the stirring unit 4, to ensure that the carbon black is fully dispersed in the natural latex, thereby improving the rubber's performance. Furthermore, the flow guiding unit 3 can refine large particles in the mixture into smaller particles.

[0110] Finally, it should be noted that those skilled in the art can obviously make various modifications and variations to this invention without departing from its spirit and scope. Therefore, if these modifications and variations fall within the scope of the claims and their equivalents, this invention also intends to include these modifications and variations.

[0111] The above description is merely one embodiment of the present invention, and should not be construed as limiting the scope of the invention. Any structural changes made based on the present invention, as long as they do not depart from the essence of the invention, should be considered as falling within the protection scope of the present invention and subject to its restrictions. Those skilled in the art will clearly understand that, for the sake of convenience and brevity, the specific working process and related descriptions of the system described above can be referred to the corresponding processes in the foregoing method embodiments, and will not be repeated here.

[0112] The term "comprising" or any other similar term is intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus / device that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent in such process, method, article, or apparatus / device.

[0113] The technical solutions of the present invention have been described above with reference to the accompanying drawings and further embodiments. However, it will be 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 can make equivalent changes or substitutions to the relevant technical features, and the technical solutions after such changes or substitutions will all fall within the scope of protection of the present invention.

[0114] The above description is merely a preferred embodiment of the present invention and is not intended to limit the scope of protection of the present invention.

Claims

1. A carbon material natural rubber latex composite reaction chamber, characterized by, The device comprises: a composite reaction chamber, to which a carbon black slurry input pipe and a natural latex input pipe are connected; a mixing unit arranged in the composite reaction chamber, for mixing carbon black slurry and natural latex to form a mixed liquid; a flow guiding unit arranged below the mixing unit, for guiding the mixed liquid; a stirring unit arranged below the flow guiding unit, for stirring and remixing the mixed liquid; a control unit comprising a collection module, a processing module and a control module, arranged in the composite reaction chamber, for automatically controlling the mixing unit, the flow guiding unit and the stirring unit to work; the mixing unit comprises: a mixing box arranged in the composite reaction chamber and connected to the carbon black slurry input pipe and the natural latex input pipe; a high-pressure input pump arranged on the carbon black slurry input pipe, for controlling the flow rate and input pressure of the carbon black slurry input into the mixing box; a natural latex flow rate detector arranged on the natural latex input pipe, for detecting the flow rate of the natural latex input into the mixing box; the collection module is electrically connected to the natural latex flow rate detector, and the control module is electrically connected to the high-pressure input pump; the collection module is used to collect the flow rate △G of the natural latex flowing into the mixing box in real time, and the control module is used to control the high-pressure input pump; the processing module is used to set a standard natural latex flow rate preset value G0, and is also used to set a first preset natural latex flow rate difference value g1, a second preset natural latex flow rate difference value g2, a third preset natural latex flow rate difference value g3 and a fourth preset natural latex flow rate difference value g4, and g1 According to the difference between the flow rate △G of the natural latex flowing into the mixing box and the standard natural latex flow rate preset value G0, a preset working condition matrix A is selected as the working condition of the high-pressure input pump; when △G-G0≤g1, the first preset working condition matrix A1 is selected as the working condition of the high-pressure input pump; when g1 when g2 when g3 when g3 When the i-th preset working condition matrix Ai is selected as the working condition of the high-pressure input pump, the control module controls the high-pressure input pump to work at the i-th preset input flow rate ai, and the control module also controls the high-pressure input pump to work at the i-th preset input pressure bi, i=1, 2, 3, 4.

2. The carbon material natural latex composite reaction chamber according to claim 1, characterized in that, The stirring unit comprises: a stirring box arranged in the composite reaction chamber; a stirring shaft arranged in the stirring box and used for stirring the mixed solution at a rotating speed; The flow guiding unit comprises: a mixed solution flow rate detector arranged above the stirring box and used for detecting the flow rate of the mixed solution flowing into the stirring box; The control module is electrically connected with the stirring shaft.

3. The carbon material natural latex composite reaction chamber according to claim 2, characterized in that, The control module is used for controlling the stirring shaft. The processing module is used for setting a standard mixed solution flow rate preset value S0, and is also used for setting a first preset mixed solution flow rate difference value s1, a second preset mixed solution flow rate difference value s2, a third preset mixed solution flow rate difference value s3 and a fourth preset mixed solution flow rate difference value s4, and s1 According to the difference between the mixed solution flow rate △S above the stirring box and the standard mixed solution flow rate preset value S0, a preset working condition matrix W is selected as the working condition of the stirring shaft; When △S-S0≤s1, the first preset working condition matrix W1 is selected as the working condition of the stirring shaft; When s1 When s2 When s3 When s3 4. The carbon material natural latex composite reaction chamber according to claim 1, characterized in that, When the i-th preset working condition matrix Wi is selected as the working condition of the stirring shaft, the control module controls the stirring shaft to work at the i-th preset stirring rotating speed di, and the control module controls the stirring time of the stirring shaft to be set as the i-th preset stirring time ei, i=1, 2, 3, 4. The mixing unit comprises: a spraying head arranged at the top of the mixing box and used for spraying the carbon black slurry; 5. The carbon material natural latex composite reaction chamber according to claim 1, characterized in that, an electronic switch valve arranged at the bottom of the mixing box and electrically connected with the control module, and used for controlling the opening and closing of the outlet at the bottom of the mixing box. The flow guiding unit further comprises: a flow guiding pipe connected below the mixing unit and used for guiding the mixed solution; A flow guide cylinder is arranged below the flow guide pipe and connected with the stirring unit, and is used for refining the particulate matters in the mixed solution. 6.The carbon material natural rubber composite reaction chamber according to claim 2, characterized in that, One side of the stirring box is connected with a mixed solution outlet pipe, and the mixed solution outlet pipe is used for discharging the mixed solution after stirring. 7.The carbon material natural rubber composite reaction chamber according to claim 4, characterized in that, A plurality of jet ports are arranged on the spray head, and the jet ports are used for spraying the carbon black slurry into the mixing box.

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