Bentonite sodium modification treatment system and process
Through the synergistic effect of the three-stage ultrasonic mixing chamber component and the directional migration component, the bentonite particle agglomerates are broken up, the water-isolating membrane is stripped off, and a deep sodiumization reaction is achieved, which solves the problem of incomplete sodiumization, improves the performance and utilization rate of the bentonite product, and reduces energy consumption and costs.
Patent Information
- Application Number
- CN202510935932.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-07-08
- Publication Date
- 2025-10-17
- Estimated Expiration
- 2045-07-08
AI Technical Summary
In the existing sodium modification process of bentonite production, traditional stirring devices cause the sodium modification reaction to occur only on the surface of the particles, failing to completely replace the Ca²⁺ between the montmorillonite layers. This affects product performance and utilization, and results in high energy consumption and increased costs.
A three-stage ultrasonic mixing chamber component and a directional migration component are used to break up particle agglomerates and peel off the water barrier through gradient ultrasonic vibration. Magnetic particles are used to target and adsorb Ca²⁺, and magnetic-electric field coupling is combined to drive directional ion migration to achieve deep exchange.
Shorten the sodium reaction time, increase the sodium degree, reduce energy consumption and raw material costs, improve product uniformity and performance stability, and have a high magnetic particle recovery rate.
Smart Images

Figure CN120420876B_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The application relates to the technical field of bentonite production, in particular to a sodium modification treatment system and process applied to bentonite production. BACKGROUND
[0002] Bentonite is a non-metallic mineral product with montmorillonite as the main mineral component. The montmorillonite structure is a 2:1 type crystal structure composed of two silicon oxygen tetrahedrons and one layer of aluminum oxygen octahedrons. Since the layered structure formed by the montmorillonite cell contains certain cations, and the action of these cations with the montmorillonite cell is very unstable, the cations are easily exchanged with other cations, so the montmorillonite has good ion exchange property.
[0003] However, in the prior art, such as the "full-automatic processing equipment and method for sodium modified bentonite" disclosed in Chinese Patent No. CN116688801A, a water supplement device, a fixed plate, a processing box, a first motor, a main uniform stirring wheel, a movable stirring mixing device, an output frame, a second motor and a sealing baffle are arranged. The fixed plate is fixedly connected to the bottom of the processing box, the first motor is fixedly connected to the middle outer side of the processing box, the water supplement device is fixedly connected to the upper end of the processing box, the main uniform stirring wheel is rotatably arranged in the middle of the bottom of the processing box, and the movable stirring mixing device is arranged in the processing box. The device can supplement water for the bentonite in the processing box in real time through the water supplement device, and the efficiency of adjusting the water content of the expanded soil can be improved through the rotating main uniform stirring wheel. The two stirring adjusting devices in the movable stirring mixing device automatically move back and forth in the processing box, which can accelerate the mixing between the bentonite and the sodium modifier, so that the bentonite and the sodium modifier are uniformly mixed, and the rotating column and the auxiliary rotating stirring rod in the stirring adjusting device rotate during the movement, which can accelerate the mixing and stirring, so that the sodium modification effect of the bentonite is good, and the efficiency is high, time and labor are saved.
[0004] However, in the prior art, such as the "full-automatic processing equipment and method for sodium modified bentonite" disclosed in Chinese Patent No. CN116688801A, a water supplement device, a fixed plate, a processing box, a first motor, a main uniform stirring wheel, a movable stirring mixing device, an output frame, a second motor and a sealing baffle are arranged. The fixed plate is fixedly connected to the bottom of the processing box, the first motor is fixedly connected to the middle outer side of the processing box, the water supplement device is fixedly connected to the upper end of the processing box, the main uniform stirring wheel is rotatably arranged in the middle of the bottom of the processing box, and the movable stirring mixing device is arranged in the processing box. The device can supplement water for the bentonite in the processing box in real time through the water supplement device, and the efficiency of adjusting the water content of the expanded soil can be improved through the rotating main uniform stirring wheel. The two stirring adjusting devices in the movable stirring mixing device automatically move back and forth in the processing box, which can accelerate the mixing between the bentonite and the sodium modifier, so that the bentonite and the sodium modifier are uniformly mixed, and the rotating column and the auxiliary rotating stirring rod in the stirring adjusting device rotate during the movement, which can accelerate the mixing and stirring, so that the sodium modification effect of the bentonite is good, and the efficiency is high, time and labor are saved.
[0004] However, in the prior art, such as the "full-automatic processing equipment and method for sodium modified bentonite" disclosed in Chinese Patent No. CN116688801A, a water supplement device, a fixed plate, a processing box, a first motor, a main uniform stirring wheel, a movable stirring mixing device, an output frame, a second motor and a sealing baffle are arranged. The fixed plate is fixedly connected to the bottom of the processing box, the first motor is fixedly connected to the middle outer side of the processing box, the water supplement device is fixedly connected to the upper end of the processing box, the main uniform stirring wheel is rotatably arranged in the middle of the bottom of the processing box, and the movable stirring mixing device is arranged in the processing box. The device can supplement water for the bentonite in the processing box in real time through the water supplement device, and the efficiency of adjusting the water content of the expanded soil can be improved through the rotating main uniform stirring wheel. The two stirring adjusting devices in the movable stirring mixing device automatically move back and forth in the processing box, which can accelerate the mixing between the bentonite and the sodium modifier, so that the bentonite and the sodium modifier are uniformly mixed, and the rotating column and the auxiliary rotating stirring rod in the stirring adjusting device rotate during the movement, which can accelerate the mixing and stirring, so that the sodium modification effect of the bentonite is good, and the efficiency is high, time and labor are saved.
[0004] However, in the prior art, such as the "full-automatic processing equipment and method for sodium modified bentonite" disclosed in Chinese Patent No. CN116688801A, a water supplement device, a fixed plate, a processing box, a first motor, a main uniform stirring wheel, a movable stirring mixing device, an output frame, a second motor and a sealing baffle are arranged. The fixed plate is fixedly connected to the bottom of the processing box, the first motor is fixedly connected to the middle outer side of the processing box, the water supplement device is fixedly connected to the upper end of the processing box, the main uniform stirring wheel is rotatably arranged in the middle of the bottom of the processing box, and the movable stirring mixing device is arranged in the processing box. The device can supplement water for the bentonite in the processing box in real time through the water supplement device, and the efficiency of adjusting the water content of the expanded soil can be improved through the rotating main uniform stirring wheel. The two stirring adjusting devices in the movable stirring mixing device automatically move back and forth in the processing box, which can accelerate the mixing between the bentonite and the sodium modifier, so that the bentonite and the sodium modifier are uniformly mixed, and the rotating column and the auxiliary rotating stirring rod in the stirring adjusting device rotate during the movement, which can accelerate the mixing and stirring, so that the sodium modification effect of the bentonite is good, and the efficiency is high, time and labor are saved. SUMMARY
[0005] The object of the present invention is to provide a sodium modification treatment system and process for bentonite production, so as to solve the above-mentioned background technology proposed that during the sodium modification treatment process of bentonite production, although a traditional stirring device (such as the above-mentioned device) improves the mixing uniformity, the "water-proof membrane" on the surface of the bentonite particles still hinders the penetration of Na+, resulting in the sodium modification reaction occurring only on the surface of the particles, causing incomplete sodium modification reaction and severely limited product performance. That is, the Ca²⁺ between the montmorillonite layers cannot be fully replaced by Na⁺, and the CEC value of the modified bentonite cannot effectively reach the ideal value, which will directly affect its key properties such as adsorption and expansibility. In addition, the surface reaction mode makes the sodium modification reaction time long and the utilization rate insufficient, which in turn leads to high overall energy consumption and increased raw material costs.
[0006] To achieve the above objectives, the present invention provides the following technical solutions: a sodium modification treatment system for bentonite production, comprising a three-stage ultrasonic mixing chamber component and a directional migration component installed therein, wherein the three-stage ultrasonic mixing chamber component is used to break up bentonite particle agglomerates, peel off the surface water barrier film, and promote ion exchange reactions through gradient ultrasonic vibration, and the directional migration component is used to target the adsorption of Ca²⁺ through magnetic particles and drive the directional migration of ions by coupling magnetic and electric fields;
[0007] The three-stage ultrasonic mixing chamber assembly includes a primary chamber, a secondary chamber, and a tertiary chamber. An electromagnetic induction coil and a variable frequency ultrasonic generator are respectively installed in the internal cavity space of the primary chamber, the secondary chamber, and the tertiary chamber. The variable frequency ultrasonic generator is respectively set to low frequency, medium frequency, and high frequency action modes;
[0008] The directional migration component includes a migration chamber, a high-speed magnetic particle generator and a magnetoelectric field coupling generator. The high-speed magnetic particle generator consists of a double-cone swirl atomizing nozzle and a Venturi accelerator, and is used to spray surface carboxyl-modified nanoparticles into the interlayers of montmorillonite to form magnetic particles and Ca²⁺ composite ion pairs. The high-speed magnetic particle generator is equally divided and arranged on the surface of the migration chamber, with its output end aligned with the internal area of the migration chamber. The magnetoelectric field coupling generator is used to drive the directional migration of ions through magnetoelectric coupling.
[0009] Preferably, the three-stage ultrasonic mixing chamber assembly further includes an internal mixing and stirring structure and an external mixing and stirring structure, and the internal and external mixing and stirring structures are both connected with a stirring shaft, and the internal and external mixing and stirring structures are arranged inside the first-level chamber, and a conical guide valve end is installed at the side end of the first-level chamber.
[0010] Preferably, the outer wall surface of the tapered flow guide valve end is provided with a rotating groove, the rotating groove is rotatably connected with a rotating ring, the outer part of the rotating ring is connected with a secondary chamber, the inside of the side end of the secondary chamber is provided with a planetary gear structure, the planetary gear structure is synchronously arranged outside the stirring shaft and connected with the inner wall of the secondary chamber, for driving the secondary chamber to form reverse rotation in the tertiary chamber, and the side end of the primary chamber is communicated with a feeding valve end.
[0011] Preferably, the outer surface of the secondary chamber is provided with a first meshing crushing structure, the inside of the secondary chamber is provided with an inner turbulent flow crushing structure, the inner turbulent flow crushing structure is synchronously arranged outside the stirring shaft, the inner wall surface of the tertiary chamber is provided with a second meshing crushing structure around, and the side end of the secondary chamber is communicated with a migration chamber through an electromagnetic discharge valve.
[0012] Preferably, the side end of the tertiary chamber is provided with a stator-rotor structure, the inside of the stator-rotor structure is sleeved with the outside of the stirring shaft, the side end of the stirring shaft is provided with an energy-saving drive motor, the output end of the energy-saving drive motor is provided with a belt pulley structure outside, and the electromagnetic interrupter is arranged at the connecting end of the output end of the energy-saving drive motor.
[0013] Preferably, the top output end of the belt pulley structure is connected with a drive gear, the outer wall surface of the tertiary chamber is provided with a ring tooth edge around, the drive gear is meshingly connected with the ring tooth edge, the bottom end of the tertiary chamber is communicated with a discharge valve end, the back side end of the tertiary chamber is embedded with a high-speed magnetic particle generator, for actively supplementing materials to the inside of the high-speed magnetic particle generator.
[0014] Preferably, the outside of the energy-saving drive motor is provided with a connecting frame, the left and right ends of the connecting frame are provided with angle adjusting cylinders, and the outside of the connecting frame is rotatably connected with a support frame structure.
[0015] Preferably, the directional migration assembly is arranged at the connection between the secondary chamber and the tertiary chamber, the directional migration assembly further comprises a flow guide ring, the flow guide ring is located at the connection end of the secondary chamber and the migration chamber, for guiding and controlling the amount of material, the inside of the migration chamber is provided with a shielding plate, the top and bottom of the shielding plate are symmetrically provided with micro electromagnetic guide rods, for driving the shielding plate to relatively displace, and the bottom end surface of the migration chamber is provided with a discharge valve port.
[0016] Preferably, a driving guide rail is arranged on the surface of the shielding plate, the side end of the driving guide rail is slidably connected with a one-way electromagnetic field control seat, a magnetoelectric field integrated detection sensor is arranged in the one-way electromagnetic field control seat, a magnetoelectric field coupling generator is arranged at the side end of the one-way electromagnetic field control seat and is driven and adjusted by the one-way electromagnetic field control seat for individual electric signal control, the other end of the driving guide rail is arranged with a micro driver, the output end of the micro driver is connected with a flexible transmission rod, and the one-way electromagnetic field control seat, the magnetoelectric field integrated detection sensor and the magnetoelectric field coupling generator are driven by the micro driver to form displacement adjustment outside the driving guide rail.
[0017] A process applied to a sodium modification treatment system for bentonite production, comprising the following steps:
[0018] S1, first, the material is fed into the primary chamber through the feed valve end, the electromagnetic induction coil is heated, and the frequency conversion ultrasonic generator is vibrated at low frequency to break the bentonite aggregates;
[0019] S2, then the material enters the secondary chamber, and under the action of the planetary gear structure, the secondary chamber is driven to rotate reversely, and the inner disturbance breaking structure cooperates with the medium frequency ultrasonic to refine the particles;
[0020] S3, then the directional migration assembly is operated, the high-speed magnetic particle generator sprays the nano-particle adsorbed Ca²⁺, and the magnetoelectric field coupling generator drives the composite ion pair to migrate:
[0021] S4, then, the high-frequency ultrasonic waves generated by the variable frequency ultrasonic generator and the rotor structure are used to strip the water film, the discharge valve end controls the finished product to be discharged and the magnetic particles are recovered, and under the cooperation of the pulley structure, the angle adjusting cylinder and the support structure, the three-stage ultrasonic mixing cavity assembly forms different operation modes.
[0022] Compared with the prior art, the beneficial effects of the present application are:
[0023] In the application, through the cooperation of the three-stage ultrasonic mixing cavity assembly and the directional migration assembly, the efficient modification from raw material pretreatment to finished product output is realized through the cooperative operation of multiple assemblies. First, the raw material is mixed with the sodium agent and enters the first chamber, and the agglomeration is broken by mechanical stirring and low-frequency ultrasonic, so as to create conditions for ion exchange. Then the material enters the second chamber, the planetary gear structure drives the reverse rotation of the second chamber to form a shear force field, cooperates with the intermediate-frequency ultrasonic and the inner disturbance breaking structure to promote the penetration of the sodium agent and accelerate the ion exchange. Then the material enters the migration chamber, the high-speed magnetic particle generator sprays the nano-particle adsorbed Ca²⁺, and the magneto-electric field coupling generator drives the directional migration of the composite ion pair to complete the deep exchange. Finally, the material enters the third chamber, the high-frequency ultrasonic peels off the water film on the surface of the particles, and the finished product is discharged through the discharge valve end. The magnetic particles are recycled through the gradient magnetic field. The device shortens the sodium reaction time, has high sodium degree, and simultaneously realizes energy consumption reduction and raw material cost reduction, and has high magnetic particle recovery rate, which improves the product uniformity and performance stability of the bentonite efficient modification. BRIEF DESCRIPTION OF DRAWINGS
[0024] Figure 1 It is a front view structural schematic diagram of a sodium modification treatment system applied to bentonite production of the application;
[0025] Figure 2 It is a side view structural schematic diagram of a sodium modification treatment system applied to bentonite production of the application;
[0026] Figure 3 It is a structural schematic diagram of a three-stage ultrasonic mixing cavity assembly applied to a sodium modification treatment system for bentonite production of the application;
[0027] Figure 4 It is a structural separation schematic diagram of a three-stage ultrasonic mixing cavity assembly applied to a sodium modification treatment system for bentonite production of the application;
[0028] Figure 5 It is an enlarged structural schematic diagram of A applied to a sodium modification treatment system for bentonite production of the application; Figure 4
[0029] Figure 6 It is a structural schematic diagram of an internal mixing and stirring structure and an external mixing and stirring structure applied to a sodium modification treatment system for bentonite production of the application;
[0030] Figure 7 It is an installation position structural schematic diagram of a directional migration assembly applied to a sodium modification treatment system for bentonite production of the application;
[0031] Figure 8 It is an internal section view structure schematic diagram of a directional migration assembly applied to a sodium modification treatment system for bentonite production;
[0032] Figure 9 It is a structure schematic diagram of a directional migration assembly applied to a sodium modification treatment system for bentonite production;
[0033] Figure 10 It is an enlarged structure schematic diagram of B of a directional migration assembly applied to a sodium modification treatment system for bentonite production; Figure 8
[0034] In the figure: 100, support frame; 200, angle adjusting cylinder; 300, belt pulley structure; 400, three-stage ultrasonic mixing cavity assembly; 401, first-stage cavity; 402, variable-frequency ultrasonic generator; 403, electromagnetic induction coil; 404, internal mixing stirring structure; 405, stirring shaft; 406, external mixing stirring structure; 407, second-stage cavity; 408, first meshing crushing structure; 409, second meshing crushing structure; 410, rotating ring; 411, planetary gear structure; 412, third-stage cavity; 413, internal spoiler crushing structure; 414, conical guide valve end; 415, ring tooth edge; 416, driving gear; 417, discharge valve end; 500, feeding valve end; 600, directional migration assembly; 601, migration cavity; 602, high-speed magnetic particle generator; 603, flow guide ring; 604, flow discharge valve port; 605, micro electromagnetic guide rod; 606, shielding plate; 607, magneto-electric field coupling generator; 608, driving guide rail; 609, micro driver; 610, flexible transmission rod; 611, magneto-electric field integrated detection sensor; 612, one-way electromagnetic field control seat; 700, stator-rotor structure; 800, energy-saving driving motor. DETAILED DESCRIPTION
[0035] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creative work fall within the scope of protection of the present application.
[0036] In the embodiments of the present application, reference is made to Figure 1 , Figure 2 and Figure 6 The application relates to a bentonite sodium modification treatment system, which comprises a three-stage ultrasonic mixing cavity assembly 400 and a directional migration assembly 600 arranged in the three-stage ultrasonic mixing cavity assembly 400. The three-stage ultrasonic mixing cavity assembly 400 is used for breaking the bentonite particle agglomerates, stripping the surface water film and promoting ion exchange reaction through gradient ultrasonic vibration. The directional migration assembly 600 is used for target adsorbing Ca2+ through magnetic particles and driving ions to directionally migrate through the coupling of a magnetic field and an electric field.
[0037] In some embodiments, according to Figures 1-7 As shown, the three-stage ultrasonic mixing cavity assembly 400 comprises a first-stage cavity 401, a second-stage cavity 407 and a third-stage cavity 412. An electromagnetic induction coil 403 and a variable-frequency ultrasonic generator 402 are arranged in the internal cavity space of the first-stage cavity 401, the second-stage cavity 407 and the third-stage cavity 412 respectively. The variable-frequency ultrasonic generator 402 is arranged in a low-frequency, medium-frequency and high-frequency mode respectively.
[0038] The three-stage ultrasonic mixing cavity assembly 400 further comprises an inner mixing and stirring structure 404 and an outer mixing and stirring structure 406. The stirring shaft 405 is connected through the inside of the inner mixing and stirring structure 404 and the outer mixing and stirring structure 406. The inner mixing and stirring structure 404 and the outer mixing and stirring structure 406 are arranged in the first-stage cavity 401. The tapered flow guide valve end 414 is arranged at the side end of the first-stage cavity 401.
[0039] The outer wall surface of the tapered flow guide valve end 414 is provided with a rotating groove. The rotating ring 410 is rotatably connected in the rotating groove. The second-stage cavity 407 is connected to the outside of the rotating ring 410. The planetary gear structure 411 is arranged in the inside of the side end of the second-stage cavity 407. The planetary gear structure 411 is synchronously arranged outside the stirring shaft 405 and connected to the inner wall of the second-stage cavity 407. The planetary gear structure 411 is used for driving the second-stage cavity 407 to reversely rotate in the third-stage cavity 412. The feeding valve end 500 is communicated with the side end of the first-stage cavity 401.
[0040] The first meshing and crushing structure 408 is arranged on the outer surface of the second-stage cavity 407. The inner disturbance flow crushing structure 413 is arranged in the inside of the second-stage cavity 407. The inner disturbance flow crushing structure 413 is synchronously arranged outside the stirring shaft 405. The second meshing and crushing structure 409 is arranged around the inner wall surface of the third-stage cavity 412. The side end of the second-stage cavity 407 and the migration cavity 601 are communicated through the electromagnetic discharge valve.
[0041] The side end of the three-stage chamber 412 is provided with a stator-rotor structure 700, the inside of the stator-rotor structure 700 is sleeved with the outside of the stirring shaft 405, the side end of the stirring shaft 405 is provided with an energy-saving driving motor 800, the output end of the energy-saving driving motor 800 is externally provided with a belt pulley structure 300, the belt pulley structure 300 and the output end of the energy-saving driving motor 800 are provided with an electromagnetic interrupter at the connecting end, when the two-stage chamber 407 rotates reversely in the three-stage chamber 412, the electromagnetic interrupter is used to connect the belt pulley structure 300 and the output end of the energy-saving driving motor 800, then the belt pulley structure 300 drives the driving gear 416 to rotate, when the driving gear 416 and the ring gear 415 are engaged, the ring gear 415 drives the three-stage chamber 412 to rotate clockwise, so that the three-stage chamber 412 and the two-stage chamber 407 rotate in different directions, the first meshing crushing structure 408 and the second meshing crushing structure 409 are engaged, and the particles are further crushed.
[0042] The top output end of the belt pulley structure 300 is connected with the driving gear 416, the outer wall surface of the three-stage chamber 412 is provided with the ring gear 415, the driving gear 416 and the ring gear 415 are engaged, the bottom end of the three-stage chamber 412 is communicated with the discharge valve end 417, the back side end of the three-stage chamber 412 is embedded with the high-speed magnetic particle generator 602, and the high-speed magnetic particle generator 602 is used to actively supplement materials into the inside of the high-speed magnetic particle generator 602.
[0043] The outside of the energy-saving driving motor 800 is provided with a connecting frame, the left and right ends of the connecting frame are provided with angle adjusting cylinders 200, the outside of the connecting frame is rotatably connected with a support frame structure 100, when the whole is operated, the angle adjusting cylinders 200 drive the three-stage ultrasonic mixing chamber assembly 400 and the directional migration assembly 600 to be angle-adjusted.
[0044] According to the embodiment of the application, specifically: first, the bentonite raw material is mixed with a sodium agent (such as NaCl solution) in proportion, then the mixture enters the first-stage chamber 401 through the feeding valve end 500, then the inner energy-saving driving motor 800 drives the stirring shaft 405 to rotate, the inner mixing stirring structure 404 and the outer mixing stirring structure 406 are driven to rotate, the raw material in the first-stage chamber 401 is preliminarily mechanically mixed, then the frequency conversion ultrasonic generator 402 in the first-stage chamber 401 is used to vibrate at a low frequency (in the range of 20-40 kHz), and the electromagnetic induction coil 403 is used to heat, (to 50-60 DEG C), so that the bentonite primary aggregate is broken (at this time, the particle size is greater than 50 microns), and the surface impurities are stripped.
[0045] Subsequently, the material processed by the primary chamber 401 enters the secondary chamber 407 through the conical guide valve end 414, which can adjust the opening degree to control the flow rate of the material. When the material enters the secondary chamber 407, the planetary gear structure 411 is driven to rotate by the stirring shaft 405, which is connected to the secondary chamber 407. The rotation of the planetary gear structure 411 drives the secondary chamber 407 to form a reverse rotation inside the tertiary chamber 412 through the rotating ring 410, forming a shear force field. The inner disturbance breaking structure 413 rotates at high speed with the stirring shaft 405, generating turbulent flow and cavitation effect. At the same time, the variable frequency ultrasonic generator 402 in the secondary chamber 407 vibrates at medium frequency (in the range of 60-80 kHz), promoting the penetration of sodium agent into the interlayer of montmorillonite and accelerating the ion exchange reaction.
[0046] Afterwards, the material enters the migration chamber 601 from the electromagnetic discharge valve, which controls the amount of material. The opening and closing of the valve port of the electromagnetic discharge valve is controlled by the external PLC controller according to the real-time sodium degree. The tertiary chamber 412 is connected to the high-speed magnetic particle generator 602 through the back end, which supplements the surface carboxylated Fe3O4 nanoparticles (particle size in the range of 15-20 nm) in real time. After the action of the directional migration assembly 600, the material falls into the tertiary chamber 412 from the discharge valve port 604 for operation. Due to the reverse rotation of the secondary chamber 407 inside the tertiary chamber 412, the first meshing breaking structure 408 and the second meshing breaking structure 409 are engaged with each other, further breaking the particles (in the range of 20-30 μm) and stripping the Ca²⁺ and montmorillonite complex on the surface of the particles. In combination with the variable frequency ultrasonic generator 402, the Ca²⁺ and montmorillonite complex on the surface of the particles are stripped by high-frequency ultrasonic operation (in the range of 100-120 kHz). Then the material is discharged from the discharge valve end 417, and the magnetic particles are recycled and reused through the gradient magnetic field.
[0047] The whole device realizes efficient modification from raw material pretreatment to finished product output through the cooperation of multiple components. First, the raw material is mixed with the sodium agent and enters the first chamber 401, and the mechanical stirring and low-frequency ultrasonic crushing of the agglomerates create conditions for ion exchange. Then the material enters the second chamber 407, and the planetary gear structure 411 drives the second chamber 407 to rotate reversely to form a shear force field, which, together with the intermediate-frequency ultrasonic and internal turbulent flow crushing structure 413, promotes the penetration of the sodium agent and accelerates the ion exchange. Then the material enters the migration chamber 601, and the high-speed magnetic particle generator 602 sprays nano-particles to adsorb Ca²⁺, and the magneto-electric field coupling generator 607 drives the directional migration of the composite ion pair to complete the deep exchange. Finally, the material enters the third chamber 412, and the high-frequency ultrasonic peeling removes the water film on the surface of the particles. The finished product is discharged through the discharge valve end 417, and the magnetic particles are recycled through the gradient magnetic field. The device shortens the sodium reaction time, increases the sodium degree, and simultaneously reduces energy consumption and raw material cost, and has a high magnetic particle recovery rate, which improves the product uniformity and performance stability of bentonite efficient modification.
[0048] In some embodiments, according to Figures 7-10 As shown, the directional migration assembly 600 includes a migration chamber 601, a high-speed magnetic particle generator 602, and a magneto-electric field coupling generator 607. The high-speed magnetic particle generator 602 is composed of a double-tapered cyclone atomizing nozzle and a Venturi accelerating tube, which is used to spray surface carboxyl-modified nano-particles into the interlayer of montmorillonite to form a magnetic particle and Ca²⁺ composite ion pair. The high-speed magnetic particle generator 602 is equally arranged on the surface of the migration chamber 601, and its output end is aligned with the internal area of the migration chamber 601. The magneto-electric field coupling generator 607 is used to drive the directional migration of ions through magneto-electric coupling.
[0049] The directional migration assembly 600 is arranged at the connection between the second chamber 407 and the third chamber 412. The directional migration assembly 600 further includes a flow guide ring 603, which is located at the connection end of the second chamber 407 and the migration chamber 601, and is used to guide and control the amount of material. The migration chamber 601 is internally provided with a shielding plate 606, and the top and bottom of the shielding plate 606 are symmetrically provided with micro electromagnetic guide rods 605 for relative displacement adjustment. The bottom surface of the migration chamber 601 is provided with a drainage valve port 604.
[0050] The surface of the shielding plate 606 is provided with a driving guide rail 608, the side end of the driving guide rail 608 is slidably connected with a one-way electromagnetic field control seat 612, the inside of the one-way electromagnetic field control seat 612 is provided with a magnetic electric field integrated detection sensor 611, a magnetic electric field coupling generator 607 is arranged at the side end of the one-way electromagnetic field control seat 612 and is driven and adjusted by the one-way electromagnetic field control seat 612 for separate electric signal control, the other end of the driving guide rail 608 is provided with a micro driver 609, the output end of the micro driver 609 is connected with a flexible transmission rod 610, and the micro driver 609 drives the one-way electromagnetic field control seat 612, the magnetic electric field integrated detection sensor 611 and the magnetic electric field coupling generator 607 to form displacement adjustment outside the driving guide rail 608.
[0051] According to the embodiment of the application, further specifically: first, the treated material in the secondary chamber 407 enters the migration chamber 601 through the electromagnetic discharge valve, the flow guide ring 603 at the connecting end controls the material flow through the annular slit (which can be adjusted in width), so that the bentonite particles enter the reaction area in a monodisperse state, avoiding agglomeration and blockage, the shielding plates 606 in the migration chamber 601 are symmetrically arranged and controlled by the micro electromagnetic guide rod 605, so that the micro electromagnetic guide rod 605 can drive the shielding plates 606 and the structures on the surface of the shielding plates 606 to perform displacement adjustment.
[0052] Then a plurality of high-speed magnetic particle generators 602 are arranged at intervals of 30°-60° around the migration chamber 601, the double-tapered cyclone atomizing nozzles mix the surface carboxyl-modified Fe3O4 nanoparticles (particle size 15-20 nm) with the dispersion liquid, accelerate the mixture through the Venturi accelerating tube, and then inject the mixture into the center of the migration chamber 601 at supersonic speed, so that the high-speed particle flow forms an umbrella-shaped injection area covering the entire migration chamber 601, the surface carboxyl groups of the particles and the interlayer Ca²⁺ of the montmorillonite are combined through coordination bonds to form a complex ion pair of magnetic particles and Ca²⁺, and the adsorption process is completed within 0.1 seconds to ensure effective capture of the interlayer Ca²⁺, the magnetic electric field coupling generator 607 is integrated in the one-way electromagnetic field control seat 612, slides to the preset position through the driving guide rail 608, a magnetic field generating unit (such as a three-axis Helmholtz coil) generates a gradient magnetic field, an electric field generating unit (such as a parallel plate electrode) applies a high-frequency alternating electric field, and the phase difference between the two is automatically calibrated to 45° to form a spiral-shaped composite force field, and the complex ion pair migrates to the bottom of the migration chamber 601 along the magnetic field gradient direction under the synergistic action of the Lorentz force (magnetic field driving) and the dielectrophoresis force (electric field driving), while Na⁺ enters the interlayer of the montmorillonite from the solution to complete the replacement of Ca²⁺, and the migration path covers the entire space of the migration chamber 601 to ensure deep ion exchange.
[0053] And the above-mentioned micro electromagnetic guide rod 605 can collect data of the magnetic and electric field integrated detection sensor 611, and real-time micro-adjust the angle of the shielding plate 606 (the angle range is controlled within 0-15°), optimize the action area of the particle flow and the composite field, for example, when it is detected that the sodium content in a certain area is insufficient, the shielding plate 606 is tilted to guide the material to stay, prolong the reaction time, and the micro driver 609 slides the one-way electromagnetic field control seat 612 through the flexible transmission rod 610, adjusts the spatial position of the magnetic and electric field coupling generator 607, and ensures the uniformity of the field strength in the migration chamber 601, wherein the magnetic and electric field integrated detection sensor 611 monitors the magnetic field strength and electric field frequency in real time, and forms automatic compensation deviation through the external PLC controller, and the bentonite particles after ion exchange enter the three-stage chamber 412 through the chamber bottom end discharge valve port 604, and the valve opening degree is automatically adjusted according to the particle size of the material, so as to avoid that the unreacted particles are discharged in advance.
[0054] The whole is adjusted through the annular slits of the flow guide ring 603, realizes that the material uniformly enters the migration chamber 601 in a monodisperse state, avoids particle agglomeration and blockage, cooperates with the dynamic inclination adjustment (0-15°) of the shielding plate 606, intelligently divides the spraying area and the reaction area, makes the material stay time error small, creates uniform flow field conditions for targeted adsorption and field effect driving, and guarantees reaction consistency from the source, and a plurality of high-speed magnetic particle generators 602 spray the carboxyl-modified nanoparticles to the center of the chamber through double-tapered cyclone atomization and Venturi acceleration technology, form an umbrella-shaped particle flow covering the whole space, efficiently capture Ca²⁺ in the interlayer of montmorillonite through coordination bonds within 0.1 seconds (adsorption efficiency ≥ 95%), break through the shallow limitations of traditional stirring adsorption, realize deep capture of difficult-to-migrate ions, and lay a foundation for deep ion exchange, at the same time, the magnetic and electric field coupling generator 607 constructs a spiral composite force field, drives the three-dimensional directional migration of the composite ion pair of the magnetic particle and Ca²⁺ through the synergistic action of the Lorentz force and the dielectrophoresis force, the path covers the whole chamber space, the migration rate is improved, the sodium reaction time is shortened, the sodium content is stable and high, the problem of incomplete modification caused by only surface reaction in the traditional process is completely solved, and the magnetic and electric field integrated detection sensor 611 monitors the field strength and sodium content in real time, and the micro electromagnetic guide rod 605 and the micro driver 609 dynamically adjust the angle of the shielding plate 606 and the position of the magnetic and electric field, to ensure that the field strength uniformity deviation is small, and the local reaction is automatically prolonged when the local reaction is insufficient, so that the overall energy consumption is reduced, and the cost is reduced.
[0055] The wiring diagram of the variable frequency ultrasonic wave generator 402, the high-speed magnetic particle generator 602, the magnetic electric field coupling generator 607 and the magnetic electric field integrated detection sensor 611 in the application belongs to the common knowledge in the art, and the working principle is a known technology, and the model is selected according to actual use. Therefore, the control mode and wiring arrangement of the variable frequency ultrasonic wave generator 402, the high-speed magnetic particle generator 602, the magnetic electric field coupling generator 607 and the magnetic electric field integrated detection sensor 611 are not explained in detail.
[0056] Although the application has been described in detail with reference to the foregoing embodiments, those skilled in the art can modify the technical solutions recorded in the foregoing embodiments or make equivalent replacements to some technical features, and any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the application shall be included in the protection scope of the application.
Claims
1. A sodium modification treatment system for bentonite production, characterized by: The invention comprises a three-stage ultrasonic mixing chamber component (400) and a directional migration component (600) arranged therein, wherein the three-stage ultrasonic mixing chamber component (400) is used to break up bentonite particle agglomerates, peel off the surface water barrier film, and promote ion exchange reaction through gradient ultrasonic vibration, and the directional migration component (600) is used to target and adsorb Ca²⁺ through magnetic particles, and drive the directional migration of ions by means of magnetic field and electric field coupling; The three-stage ultrasonic mixing chamber assembly (400) comprises a primary chamber (401), a secondary chamber (407) and a tertiary chamber (412), wherein electromagnetic induction coils (403) and variable frequency ultrasonic generators (402) are respectively installed in the internal cavity spaces of the primary chamber (401), the secondary chamber (407) and the tertiary chamber (412), and the variable frequency ultrasonic generators (402) are respectively set to low frequency, medium frequency and high frequency action modes; The directional migration component (600) includes a migration chamber (601), a high-speed magnetic particle generator (602) and a magneto-electric field coupling generator (607). The high-speed magnetic particle generator (602) is composed of a double-cone swirl atomizing nozzle and a Venturi accelerator tube, and is used to spray surface carboxyl-modified nanoparticles between montmorillonite layers to form magnetic particles and Ca²⁺ composite ion pairs. The high-speed magnetic particle generator (602) is equally divided and arranged around the surface of the migration chamber (601), and its output end is aligned with the internal area of the migration chamber (601). The magneto-electric field coupling generator (607) is used to drive the directional migration of ions through magneto-electric coupling.
2. The sodium modification treatment system for bentonite production according to claim 1, characterized in that: The three-stage ultrasonic mixing chamber assembly (400) further includes an internal mixing and stirring structure (404) and an external mixing and stirring structure (406), wherein the internal mixing and stirring structure (404) and the external mixing and stirring structure (406) are both connected with a stirring shaft (405), and the internal mixing and stirring structure (404) and the external mixing and stirring structure (406) are arranged inside the first-stage chamber (401), and a conical guide valve end (414) is arranged at the side end of the first-stage chamber (401).
3. The sodium modification treatment system for bentonite production according to claim 2, characterized in that: A rotation groove is provided on the outer wall surface of the conical guide valve end (414), and a rotating ring (410) is rotatably connected inside the rotation groove. The outside of the rotating ring (410) is connected to the secondary chamber (407), and a planetary gear structure (411) is installed inside the side end of the secondary chamber (407). The planetary gear structure (411) is synchronously installed outside the stirring shaft (405) and connected to the inner wall of the secondary chamber (407) to drive the secondary chamber (407) to form a reverse rotation inside the tertiary chamber (412). The side end of the primary chamber (401) is connected to the feed valve end (500).
4. The sodium modification treatment system for bentonite production according to claim 3, characterized in that: The outer surface of the secondary chamber (407) is provided with a first meshing crushing structure (408), the interior of the secondary chamber (407) is provided with an internal turbulence crushing structure (413), and the internal turbulence crushing structure (413) is synchronously provided on the outside of the stirring shaft (405). The inner wall surface of the tertiary chamber (412) is provided with a second meshing crushing structure (409), and the side end of the secondary chamber (407) and the migration chamber (601) are connected via an electromagnetic discharge valve.
5. The sodium modification treatment system for bentonite production according to claim 4, characterized in that: A stator and rotor structure (700) is installed at the side end of the three-stage chamber (412), the interior of the stator and rotor structure (700) and the exterior of the stirring shaft (405) are nested, an energy-saving drive motor (800) is installed at the side end of the stirring shaft (405), a pulley structure (300) is installed on the outside of the output end of the energy-saving drive motor (800), and an electromagnetic blocker is installed at the connection end of the pulley structure (300) and the output end of the energy-saving drive motor (800).
6. The sodium modification treatment system for bentonite production according to claim 5, characterized in that: The top output end of the pulley structure (300) is connected to a driving gear (416), and an annular tooth edge (415) is arranged around the outer wall surface of the three-stage chamber (412). The driving gear (416) and the annular tooth edge (415) are meshed and connected. The bottom end of the three-stage chamber (412) is connected to a discharge valve end (417), and the back end of the three-stage chamber (412) is engaged with the high-speed magnetic particle generator (602) for actively replenishing material into the high-speed magnetic particle generator (602).
7. The sodium modification treatment system for bentonite production according to claim 6, characterized in that: A connecting frame is installed on the outside of the energy-saving drive motor (800), angle adjustment cylinders (200) are installed on the left and right ends of the connecting frame, and the outside of the connecting frame is rotatably connected to a support structure (100).
8. The sodium modification treatment system for bentonite production according to claim 7, characterized in that: The directional migration component (600) is installed at the connecting guide connection between the secondary chamber (407) and the tertiary chamber (412). The directional migration component (600) further includes a guide ring (603). The guide ring (603) is located at the connection end between the secondary chamber (407) and the migration chamber (601) and is used to guide and control the amount of material. A shielding plate (606) is installed inside the migration chamber (601). Miniature electromagnetic guide rods (605) are symmetrically installed on the top and bottom of the shielding plate (606) to drive the shielding plate (606) to adjust the relative displacement. A discharge valve port (604) is opened on the bottom surface of the migration chamber (601).
9. The sodium modification treatment system for bentonite production according to claim 8, characterized in that: A driving guide rail (608) is installed on the surface of the shielding plate (606), and a one-way electromagnetic field control seat (612) is slidably connected to the side end of the driving guide rail (608). A magnetic field integrated detection sensor (611) is installed inside the one-way electromagnetic field control seat (612). The magnetic field coupling generator (607) is installed on the side end of the one-way electromagnetic field control seat (612) and is independently controlled and driven by the one-way electromagnetic field control seat (612). A micro driver (609) is installed at the other end of the driving guide rail (608), and the output end of the micro driver (609) is connected to a flexible transmission rod (610). The micro driver (609) drives the one-way electromagnetic field control seat (612), the magnetic field integrated detection sensor (611), and the magnetic field coupling generator (607) through the flexible transmission rod (610) to form displacement adjustment outside the driving guide rail (608).
10. A process for sodium modification treatment system for bentonite production, characterized in that: The sodium modification treatment system for bentonite production according to claim 9 is used, comprising the following steps: S1. First, the material enters the primary chamber (401) through the feed valve end (500), causing the electromagnetic induction coil (403) to heat and the variable frequency ultrasonic generator (402) to vibrate at a low frequency to break up bentonite agglomerates; S2, the material then enters the secondary chamber (407), and under the action of the planetary gear structure (411), the secondary chamber (407) is driven to rotate in the reverse direction, and the internal turbulence crushing structure (413) cooperates with the medium-frequency ultrasound to refine the particles; S3. Then, the directional migration component (600) operates, so that the high-speed magnetic particle generator (602) ejects nanoparticles to adsorb Ca²⁺, and the magnetic-electric field coupling generator (607) drives the migration of the composite ion pairs: S4. Next, the stator and rotor structure (700) and the variable frequency ultrasonic generator (402) generate high-frequency ultrasonic waves to peel off the water-proof membrane, and the discharge valve end (417) controls the discharge of the finished product and recovers the magnetic particles. In addition, with the cooperation of the pulley structure (300), the angle adjustment cylinder (200) and the support structure (100), the three-stage ultrasonic mixing chamber assembly (400) is driven to form different operating modes.
Citation Information
Patent Citations
Production equipment and production process of sodium modified bentonite
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