A reactor for the production of aluminosilicate

Abstract

The present invention discloses a reactor for the production of aluminum silicate, which relates to the technical field of aluminum silicate production; it includes a reaction installation member, on which a stability detection member is installed, and the stability detection member is used to detect the stability of the solution; a grading control member is installed on the stability detection member; the grading control member is used to control the precipitation of the stable solution; a clear liquid discharge member is installed on the reaction installation member; the clear liquid discharge member is used to discharge the clear liquid after precipitation; the use of the clear liquid discharge member facilitates real-time testing of the fullness of the reaction, without relying on manual use of test strips for testing, which is time-consuming and laborious, and can detect in real time whether the discharged clear liquid can continue to undergo a precipitation reaction; to solve the problems that the current reactor for the production of aluminum silicate is not convenient for real-time testing of the adequacy of the reaction, relying on manual use of test strips for testing is time-consuming and laborious, and it is not convenient to automatically control the suspension during the discharge of the precipitate.

Description

Technical Field

[0001] The present invention relates to the technical field of aluminosilicate production, and specifically to a reactor for aluminosilicate production. Background Technique

[0002] When manufacturing aluminosilicate, a reactor is required for reaction precipitation. Among them, the precipitation method is widely used. Its raw materials usually involve diluting and formulating sodium silicate and aluminum sulfate into solutions with certain concentrations, and then carrying out a neutralization reaction to generate aluminosilicate precipitation. After steps such as filtration, washing, drying, and pulverization, an aluminosilicate product is finally obtained. Currently, the reactors for aluminosilicate production usually use general reactors for reaction, which is not convenient for real-time testing of the reaction sufficiency. Relying on manual use of test strips for testing is time-consuming and laborious, and it is not convenient for reverse deduction to prevent waste, affecting economic efficiency. It is not convenient for hierarchical control to carry out precipitation work after the liquid inlet is stable, and it is not convenient to achieve continuous liquid inlet reaction precipitation. It is easy to affect the precipitation effect due to the liquid level shaking. At the same time, it is not convenient to automatically control the suspension during the discharge of the precipitate. It is difficult for manual workers outside to distinguish the amount of the precipitate, and a large amount of reaction mixture solution is easily discharged, which has a greater impact on the moisture content of the precipitate.

[0003] Therefore, we propose a reactor for aluminosilicate production. Summary of the Invention

[0004] The purpose of the present invention is to provide a reactor for aluminosilicate production to solve the problems in the above background technique that the current reactors for aluminosilicate production are not convenient for real-time testing of the reaction sufficiency, relying on manual use of test strips for testing is time-consuming and laborious, and it is not convenient to automatically control the suspension during the discharge of the precipitate.

[0005] To achieve the above purpose, the present invention provides the following technical solution: A reactor for aluminosilicate production, including a reaction installation member, on which a stability detection member is installed for detecting the stability of the solution; a hierarchical control member is installed on the stability detection member for controlling the precipitation of the stable solution; a clear liquid discharge member is installed on the reaction installation member for discharging the clear liquid after precipitation; a continuous precipitation detection member is installed on the clear liquid discharge member for detecting the precipitate; an anti-overdischarge member is installed at the bottom of the reaction installation member for preventing over-discharge; the reaction installation member includes: a reaction tank and a driving motor, the bottom of the reaction tank is provided with four support legs; the bottom of the reaction tank is of an arc structure; a driving motor is fixedly installed on the side of the reaction tank, and the output shaft of the driving motor passes through the reaction tank.

[0006] Preferably, the reaction mounting member further includes: stirring teeth and a liquid inlet pipe. The stirring teeth are fixedly mounted on the output shaft of the driving motor; two liquid inlet pipes are fixedly mounted on the top of the reaction tank, and the two liquid inlet pipes are respectively used for connecting to the external raw material pipes.

[0007] Preferably, the stability detection member includes: a detection partition plate, a discharge pipe, a ball head, a swing shaft, a stability detection plate, and a discharge solenoid valve. The detection partition plate is fixedly mounted inside the reaction tank; four discharge pipes are fixedly mounted on the reaction tank; the ball head is rotatably sleeved in the middle of the detection partition plate; the bottom of the ball head is fixedly mounted with a swing shaft, and the end of the swing shaft is an arc-shaped structure; the top of the ball head is fixedly mounted with a stability detection plate, and the stability detection plate is a "cross" shaped structure; the stability detection plate is connected to the detection partition plate by four tension springs; discharge solenoid valves are respectively installed on the four discharge pipes.

[0008] Preferably, the grading control member includes: a grading control cover, a lifting column, and a stability switch. The grading control cover is threadedly connected to the bottom of the detection partition plate; the lifting column is slidably inserted inside the grading control cover; the top of the lifting column is a hemispherical structure; the top of the lifting column is aligned with the swing shaft; a stability switch is fixedly mounted inside the grading control cover, and the top of the stability switch is attached to the lifting column; a spring is connected to the bottom of the lifting column, and the spring at the bottom of the lifting column is located outside the stability switch; the stability switch is electrically connected to the four discharge solenoid valves.

[0009] Preferably, the clear liquid discharge member includes: a discharge coiled pipe, a discharge check valve, a return pipe, and a return solenoid valve. The discharge coiled pipe is fixedly mounted on the reaction tank; a discharge check valve is installed at the end of the discharge coiled pipe; the discharge check valve is located inside the reaction tank; the discharge check valve is located below the detection partition plate; the discharge coiled pipe is formed by S-shaped bending; a return pipe is fixedly mounted on the side of the discharge coiled pipe; a return solenoid valve is installed on the return pipe; the return pipe is located above the detection partition plate.

[0010] Preferably, the clear liquid discharge member further includes: a port solenoid valve, a compressed gas cylinder, and a gas cylinder solenoid valve. A port solenoid valve is installed at the outlet end of the discharge coiled pipe; a compressed gas cylinder is fixedly mounted on the discharge coiled pipe; the air outlet pipe of the compressed gas cylinder is connected to the discharge coiled pipe; the air outlet pipe of the compressed gas cylinder is located on the side close to the return solenoid valve; a gas cylinder solenoid valve is installed on the air outlet pipe of the compressed gas cylinder.

[0011] Preferably, the continuous precipitation detection component includes: a support frame, an independent switch, and a precipitation isolation filter block. A circle of through holes is provided on the support frame; the support frame is fixedly installed on the discharge coiled pipe; two independent switches are fixedly installed on the support frame; the left independent switch is used to control the gas cylinder solenoid valve and the reflux solenoid valve to be normally closed, and the right independent switch is used to control the port solenoid valve to be normally open; a precipitation isolation filter block is slidably installed on the discharge coiled pipe, and the precipitation isolation filter block is located above the independent switch; a spring is provided between the precipitation isolation filter block and the support frame; the precipitation isolation filter block is provided with filter holes.

[0012] Preferably, the over-discharge prevention component includes: a precipitation discharge pipe, a stop ring, and a precipitation solenoid valve. The precipitation discharge pipe is fixedly installed at the bottom of the reaction tank; a stop ring is fixedly sleeved inside the precipitation discharge pipe; a precipitation solenoid valve is installed at the end of the precipitation discharge pipe.

[0013] Preferably, the over-discharge prevention component further includes: a monitoring installation frame, a sliding sleeve, and a reset tension spring. A monitoring installation frame is fixedly installed at the top of the precipitation discharge pipe; a circle of through holes is provided on the monitoring installation frame; a sliding sleeve is fixedly installed at the bottom of the monitoring installation frame; a reset tension spring is sleeved inside the sliding sleeve.

[0014] Preferably, the over-discharge prevention component further includes: a stop disk, a switch frame, a closed switch, and an electromagnet. A sliding shaft is provided at the top of the stop disk; the sliding shaft at the top of the stop disk is slidably installed on the sliding sleeve; the reset tension spring is connected between the sliding shaft at the top of the stop disk and the monitoring installation frame; the stop disk elastically fits the stop ring; a switch frame is fixedly installed inside the precipitation discharge pipe, and a circle of through holes is provided on the switch frame; a closed switch is fixedly installed at the top of the switch frame, and the closed switch is located below the stop disk; an electromagnet is fixedly sleeved on the switch frame; the electromagnet is used to magnetically attract the stop disk; the electromagnet is externally connected to a control switch; the closed switch is electrically connected to the precipitation solenoid valve; a circle of slot holes is provided on the stop disk.

[0015] Compared with the prior art, the beneficial effects of the present invention are:

[0016] The present invention adopts a clear liquid discharge component to facilitate real-time testing of the reaction sufficiency, without relying on manual use of test strips for testing, which is time-consuming and laborious. It can directly and efficiently detect in real time whether the discharged clear liquid can continue to undergo a precipitation reaction. The structure detection is direct and efficient. At the same time, without manual control, it is convenient for the staff to timely adjust the liquid inlet speed, and at the same time, it can be used for reverse deduction to prevent waste, improve economy, reduce the possibility that the precipitate may be mixed with unreacted substances or other impurities, and improve the purity and quality of the precipitate.

[0017] The hierarchical control part can be used for hierarchical control of the discharged raw materials. When directly discharging raw materials, when the raw materials enter the inside of the reaction tank, the sediment will be impacted and floated due to the impact force, affecting the sediment quality. At the same time, the stability detection part can be used to detect the stability of the mixed solution and then conduct the discharge, which can ensure the sedimentation speed of the sediment. Excessive inlet liquid impact force will also affect the sedimentation process.

[0018] By adopting an anti-overdischarge part, it is possible to control the discharge of sediment, timely discharge the sediment, and avoid the accumulation of sediment. It can prevent the large amount of solution from being discharged due to the failure to close in time during the sediment discharge, resulting in waste. At the same time, it is easy for the excessively discharged solution to mix into the discharged sediment, resulting in too high humidity of the sediment and affecting the subsequent processing. It can be controlled directly and accurately by using the different pressures of the sediment and the solution. Brief Description of the Drawings

[0019] Figure 1 It is a schematic diagram of the overall structure of a reactor for the production of aluminum silicate according to the present invention;

[0020] Figure 2 It is a schematic diagram of the bottom structure of a reactor for the production of aluminum silicate according to the present invention;

[0021] Figure 3 It is a sectional view of the internal structure of a reactor for the production of aluminum silicate according to the present invention;

[0022] Figure 4 It is a schematic diagram of the reaction installation part structure according to the present invention;

[0023] Figure 5 According to the present invention Figure 3 The enlarged view of the structure of area B;

[0024] Figure 6 According to the present invention Figure 4 The enlarged view of the structure of area C;

[0025] Figure 7 It is a schematic diagram of the structure of the clear liquid discharge part according to the present invention;

[0026] Figure 8 According to the present invention Figure 3 The enlarged view of the structure of area D;

[0027] Figure 9 According to the present invention Figure 4 The enlarged view of the structure of area G;

[0028] Figure 10 According to the present invention Figure 4 The enlarged view of the structure of area E;

[0029] Figure 11 According to the present invention Figure 3 The enlarged view of the structure of area F.

[0030] In the figure: 1. Reaction mounting member; 101. Reaction tank; 102. Driving motor; 1021. Stirring teeth; 103. Liquid inlet pipe; 2. Stability detection member; 201. Detection partition plate; 202. Drain pipe; 203. Ball head; 2031. Swing shaft; 204. Stability detection plate; 205. Drain solenoid valve; 3. Hierarchical control member; 301. Hierarchical control cover; 302. Lifting column; 303. Stability switch; 4. Clear liquid discharge member; 401. Discharge coil pipe; 402. Discharge check valve; 403. Return pipe; 4031. Return solenoid valve; 404. Port solenoid valve; 405. Compressed gas cylinder; 406. Gas cylinder solenoid valve; 5. Continuous precipitation detection member; 501. Support frame; 502. Independent switch; 503. Precipitation isolation filter block; 6. Anti-overdischarge member; 601. Precipitation discharge pipe; 6011. Stop ring; 6012. Precipitation solenoid valve; 602. Monitoring mounting frame; 603. Sliding sleeve; 604. Reset tension spring; 605. Stop plate; 606. Switch frame; 607. Closing switch; 608. Electromagnet. Specific implementation mode

[0031] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

[0032] Embodiment 1: Please refer to Figures 1 to 11 as shown:

[0033] The present invention provides a technical solution: A reactor for producing aluminum silicate, including a reaction mounting member 1, a stability detection member 2 is installed on the reaction mounting member 1, and the stability detection member 2 is used to detect the stability of the solution; a hierarchical control member 3 is installed on the stability detection member 2; the hierarchical control member 3 is used to control the precipitation of the stable solution; a clear liquid discharge member 4 is installed on the reaction mounting member 1; the clear liquid discharge member 4 is used to discharge the clear liquid after precipitation; a continuous precipitation detection member 5 is installed on the clear liquid discharge member 4; the continuous precipitation detection member 5 is used to detect the precipitate; an anti-overdischarge member 6 is installed at the bottom of the reaction mounting member 1; the anti-overdischarge member 6 is used to prevent over-discharge; the reaction mounting member 1 includes: a reaction tank 101 and a driving motor 102, and four support legs are provided at the bottom of the reaction tank 101; the bottom of the reaction tank 101 is an arc structure; a driving motor 102 is fixedly installed on the side of the reaction tank 101, and the output shaft of the driving motor 102 passes through the reaction tank 101.

[0034] Among them, the reaction mounting member 1 further includes: stirring teeth 1021 and a liquid inlet pipe 103. The stirring teeth 1021 are fixedly installed on the output shaft of the driving motor 102; two liquid inlet pipes 103 are fixedly installed on the top of the reaction tank 101, and the two liquid inlet pipes 103 are respectively used to connect to the raw material pipes externally; the stability detection member 2 includes: a detection partition plate 201, a discharge pipe 202, a ball head 203, a swing shaft 2031, a stability detection plate 204 and a discharge solenoid valve 205. The detection partition plate 201 is fixedly installed inside the reaction tank 101; four discharge pipes 202 are fixedly installed on the reaction tank 101; the ball head 203 is rotatably sleeved in the middle of the detection partition plate 201; the swing shaft 2031 is fixedly installed at the bottom of the ball head 203, and the end of the swing shaft 2031 is an arc structure; the stability detection plate 204 is fixedly installed at the top of the ball head 203, and the stability detection plate 204 is in a "cross" shape structure; the stability detection plate 204 is connected to the detection partition plate 201 by four tension springs; discharge solenoid valves 205 are respectively installed on the four discharge pipes 202; the hierarchical control member 3 includes: a hierarchical control cover 301, a lifting column 302 and a stability switch 303. The hierarchical control cover 301 is threadedly connected to the bottom of the detection partition plate 201; the lifting column 302 is slidably inserted inside the hierarchical control cover 301; the top of the lifting column 302 is a hemispherical structure; the top of the lifting column 302 is aligned with the swing shaft 2031; the stability switch 303 is fixedly installed inside the hierarchical control cover 301, and the top of the stability switch 303 is attached to the lifting column 302; a spring is connected to the bottom of the lifting column 302, and the spring at the bottom of the lifting column 302 is located outside the stability switch 303; the stability switch 303 is electrically connected to the four discharge solenoid valves 205. The hierarchical control member 3 can be used for hierarchical control of discharging raw materials. When discharging raw materials directly, when the raw materials enter the reaction tank 101, the sediment will be impacted and floated due to the impact force, affecting the sediment quality. At the same time, the stability detection member 2 can be used to detect the stability of the mixed solution and then conduct the discharge, which can ensure the sedimentation speed of the sediment. Excessive inlet impact force will also affect the precipitation generation process. For example, during the precipitation process, if the precipitation agent is added too fast, the local reactant concentration will be too high, and the rapidly formed precipitate will accumulate locally; the energy released during the formation of this rapidly accumulated precipitate and the interaction between the precipitate particles are likely to cause impurities that are first adsorbed on the precipitate surface to be unable to leave the precipitate in time and be trapped inside the precipitate, causing coprecipitation and resulting in impure precipitate. This phenomenon is called occlusion phenomenon. When the solution shakes, the stability detection plate 204 is also driven to shake. At this time, the stability detection plate 204 will drive the ball head 203 to rotate on the detection partition plate 201, and the swing shaft 2031 will also be driven to swing. At this time, the detection partition plate 201 is no longer aligned with the lifting column 302. At this time, the discharge solenoid valve 205 is controlled to close by the stability switch 303 to avoid excessive discharge of the solution and affecting the precipitation effect.

[0035] Among them, the clear liquid discharge component 4 includes: a discharge coil pipe 401, a discharge check valve 402, a return pipe 403, and a return solenoid valve 4031. The discharge coil pipe 401 is fixedly installed on the reaction tank 101; a discharge check valve 402 is installed at the end of the discharge coil pipe 401; the discharge check valve 402 is located inside the reaction tank 101; the discharge check valve 402 is located below the detection partition plate 201; the discharge coil pipe 401 is formed by S-shaped bending; a return pipe 403 is fixedly installed on the side of the discharge coil pipe 401; a return solenoid valve 4031 is installed on the return pipe 403; the return pipe 403 is located above the detection partition plate 201; the clear liquid discharge component 4 further includes: a port solenoid valve 404, a compressed gas cylinder 405, and a gas cylinder solenoid valve 406. A port solenoid valve 404 is installed at the outlet end of the discharge coil pipe 401; a compressed gas cylinder 405 is fixedly installed on the discharge coil pipe 401; the air outlet pipe of the compressed gas cylinder 405 is connected to the discharge coil pipe 401; the air outlet pipe of the compressed gas cylinder 405 is located on one side close to the return solenoid valve 4031; a gas cylinder solenoid valve 406 is installed on the air outlet pipe of the compressed gas cylinder 405; the continuous precipitation detection component 5 includes: a support frame 501, an independent switch 502, and a precipitation isolation filter block 503. The precipitation isolation filter block 503 is provided with filter holes; the support frame 501 is provided with a circle of through holes; the support frame 501 is fixedly installed on the discharge coil pipe 401; two independent switches 502 are fixedly installed on the support frame 501; the left independent switch 502 is used to control the gas cylinder solenoid valve 406 and the return solenoid valve 4031 to be normally closed, and the right independent switch 502 is used to control the port solenoid valve 404 to be normally open; a precipitation isolation filter block 503 is slidably installed on the discharge coil pipe 401, and the precipitation isolation filter block 503 is located above the independent switch 502;A spring is provided between the precipitation isolation filter block 503 and the support frame 501. The use of the clear liquid discharge part 4 facilitates real-time testing of the sufficiency of the reaction. There is no need to rely on manual use of test strips for testing, which is time-consuming and laborious. It can directly and efficiently detect in real time whether the discharged clear liquid can continue to undergo a precipitation reaction. At the same time, without manual control, it is convenient for the staff to timely adjust the liquid inlet speed. At the same time, it can be pushed back to prevent waste, improve economy, and avoid the direct discharge of still-usable clear liquid. It can facilitate the reflux of the clear liquid above the detection partition plate 201 without affecting the stability of the precipitate. This structure is controlled by air pressure and also plays a role in preventing the precipitation isolation filter block 503 from being blocked, ensuring the sustainable use of this structure and making the structure more reasonable. This structure does not require cumbersome operations such as pH detection to ensure the reaction efficiency. If the precipitation is incomplete, subsequent processing of the precipitate, such as filtration, washing, drying, etc., will also be affected because the precipitate may contain unreacted substances or other impurities, thus affecting the purity and quality of the precipitate. It avoids the problem of insufficient precipitation caused by factors such as too fast feeding speed and raw material concentration. The clear liquid after precipitation under the detection partition plate 201 can be drained through the discharge coiled pipe 401. When precipitation occurs inside the discharge coiled pipe 401 due to insufficient precipitation of the solution, precipitates will filter and deposit above the precipitation isolation filter block 503. At this time, the permeability of the precipitation isolation filter block 503 will be blocked. As more precipitates block, the compressed air in the compressed gas cylinder 405 can push the liquid inside the discharge coiled pipe 401 to flow back. The solution and the precipitate can then be discharged into the detection partition plate 201 through the return pipe 403, and the precipitation mixing is carried out again to perform subsequent precipitation work.;

[0036] Embodiment 2. On the basis of Embodiment 1, the over-discharge prevention member 6 includes: a precipitation discharge pipe 601, a stop ring 6011, and a precipitation solenoid valve 6012. The precipitation discharge pipe 601 is fixedly installed at the bottom of the reaction tank 101; a stop ring 6011 is fixedly sleeved inside the precipitation discharge pipe 601; a precipitation solenoid valve 6012 is installed at the end of the precipitation discharge pipe 601; the over-discharge prevention member 6 further includes: a monitoring mounting bracket 602, a sliding sleeve 603, and a return spring 604. The top of the precipitation discharge pipe 601 is fixedly installed with a monitoring mounting bracket 602; a circle of through holes is provided on the monitoring mounting bracket 602; the bottom of the monitoring mounting bracket 602 is fixedly installed with a sliding sleeve 603; a return spring 604 is sleeved inside the sliding sleeve 603; the over-discharge prevention member 6 further includes: a stop disk 605, a switch bracket 606, a closing switch 607, and an electromagnet 608. A sliding shaft is provided on the top of the stop disk 605; the sliding shaft on the top of the stop disk 605 is slidably installed on the sliding sleeve 603; the return spring 604 is connected between the sliding shaft on the top of the stop disk 605 and the monitoring mounting bracket 602; the stop disk 605 elastically fits the stop ring 6011; a switch bracket 606 is fixedly installed inside the precipitation discharge pipe 601, and a circle of through holes is provided on the switch bracket 606; a closing switch 607 is fixedly installed on the top of the switch bracket 606, and the closing switch 607 is located below the stop disk 605; an electromagnet 608 is fixedly sleeved on the switch bracket 606; the electromagnet 608 is used to magnetically attract the stop disk 605; the electromagnet 608 is externally connected with a control switch; the closing switch 607 is electrically connected to the precipitation solenoid valve 6012;A ring of slot holes is provided on the stop disk 605. By using the anti-overdischarge part 6, the control of sediment discharge can be realized, and the sediment can be discharged in time, avoiding the accumulation of sediment. By using the anti-overdischarge part 6, it can also be avoided that the sediment is not closed in time during discharge, resulting in the discharge of a large amount of solution, causing waste and easily causing the discharged solution to mix into the discharged sediment, thus causing the sediment to have too high humidity and affecting the subsequent processing. It can be controlled by the different pressures of the sediment and the solution, which is direct and accurate. Since the sediment precipitates at the bottom of the reaction tank 101 and the diameter of the sediment discharge pipe 601 is limited, it is difficult to completely discharge the sediment outside the sediment discharge pipe 601 at the bottom of the reaction tank 101 during sediment discharge. It is necessary to gradually precipitate and naturally slide and then discharge again. Traditional manual observation and other methods are difficult to ensure the accuracy of sediment discharge. This structure can be automatically controlled. Because the sediment is discharged in a solid state and has a high particle size, it will push the stop disk 605 downward during sediment discharge, keeping the closed switch 607 squeezed, and controlling the sediment solenoid valve 6012 to discharge in real time. At this time, even if the electromagnet 608 is turned off after being powered on once, the sediment can still be discharged from between the stop disk 605 and the stop ring 6011. At the same time, once the sediment discharge is completed, the solution above will be discharged at this time. Since the solution is a fluid and has no particle size at this time, the moisture will flow through the slot holes on the stop disk 605, and the solution cannot push the stop disk 605. At this time, under the pull of the return spring 604, the stop disk 605 will move upward and reset, no longer squeezing the closed switch 607, and at this time, the control sediment solenoid valve 6012 will be closed.;

[0037] Working principle of this embodiment: First, place the reaction tank 101 on the ground, and introduce sodium silicate and aluminum sulfate respectively through two inlet pipes 103. As the liquid is introduced, the driving motor 102 can be started to control the mixing of the solution by the stirring teeth 1021. After the solution is mixed evenly, the driving motor 102 is turned off. At this time, the solution will continue to shake under the action of inertia, driving the stable detection plate 204 to shake as well. At this time, the stable detection plate 204 will drive the ball head 203 to rotate on the detection partition plate 201, and the swing shaft 2031 will be driven to swing. At this time, the detection partition plate 201 is no longer aligned with the lifting column 302. The top of the lifting column 302 is a hemispherical structure. When the swing shaft 2031 cannot press against the top of the lifting column 302, an upward displacement will occur. At this time, the discharge solenoid valve 205 is controlled to close by the stable switch 303, avoiding excessive discharge of the solution and affecting the precipitation effect, and is more suitable for subsequent liquid inlet in continuous precipitation work. The clarified liquid after precipitation under the detection partition plate 201 can be drained through the discharge coil pipe 401. When precipitation occurs inside the discharge coil pipe 401 because the solution is not fully precipitated, sediment will filter and deposit above the sediment isolation filter block 503. At this time, the permeability of the sediment isolation filter block 503 will be blocked. As more sediment blocks, under the action of water pressure, the sediment isolation filter block 503 will squeeze two independent switches 502. At this time, the left independent switch 502 controls the opening of the gas cylinder solenoid valve 406 and the reflux solenoid valve 4031, and the right independent switch 502 controls the closing of the port solenoid valve 404. At this time, the compressed air in the compressed gas cylinder 405 can push the liquid inside the discharge coil pipe 401 to flow back. Because the discharge check valve 402 is unidirectional, the solution and sediment can be discharged from the reflux pipe 403 into the upper part of the detection partition plate 201 to re-perform the mixing work before precipitation. When it is necessary to discharge the sediment, first control the switch externally connected to the electromagnet 608 to energize the electromagnet 608 once. At this time, the magnetic attraction of the electromagnet 608 causes the stop disk 605 to move downward. At this time, the stop disk 605 will squeeze the closed switch 607 to control the opening of the precipitation solenoid valve 6012. Because the sediment is discharged in a solid state and has a high particle size, it will push the stop disk 605 downward under the pressure during sediment discharge, keeping the closed switch 607 squeezed and controlling the real-time discharge of the precipitation solenoid valve 6012. At this time, even if the electromagnet 608 is turned off after being energized once, the sediment can still be discharged from between the stop disk 605 and the stop ring 6011 under the action of pressure. At the same time, once the sediment discharge is completed, the solution above will be discharged. Because the solution is a fluid and has no particle size at this time, the water will flow through the slot holes on the stop disk 605, and the solution cannot push the stop disk 605 downward. At this time, under the pulling of the return spring 604, the stop disk 605 will move upward to reset and no longer squeeze the closed switch 607. At this time, the precipitation solenoid valve 6012 is controlled to close, and the pulling control of the return spring 604 is used to stop the discharge and avoid excessive discharge of the solution.

[0038] It should be noted that in this text, relational terms such as first and second are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any actual relationship or order between these entities or operations. Moreover, the term "comprising", "including" or any other variant thereof is intended to cover non-exclusive inclusion, such that a process, method, article or device comprising a series of elements not only includes those elements but also includes other elements not expressly listed, or further includes elements inherent to such process, method, article or device.

[0039] Although the embodiments of the present invention have been shown and described, those of ordinary skill in the art can understand that various changes, modifications, substitutions and variations can be made to these embodiments without departing from the principles and spirit of the present invention. The scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A reactor for the production of aluminosilicate, comprising a reaction mounting member, on which a stability detection member is mounted, characterized in that: The stability detection component is used to detect the stability of the solution; a hierarchical control component is installed on the stability detection component; the hierarchical control component is used to control the precipitation of the stable solution; A supernatant discharge component is installed on the reaction installation component; the supernatant discharge component is used to discharge the supernatant after precipitation; a continuous precipitation detection component is installed on the supernatant discharge component; the continuous precipitation detection component is used to detect the precipitate; An anti-overdischarge component is installed at the bottom of the reaction installation component; the anti-overdischarge component is used to prevent over-discharge; The reaction installation component includes: a reaction tank and a driving motor. There are four support legs at the bottom of the reaction tank; the bottom of the reaction tank is an arc structure; the driving motor is fixedly installed on the side of the reaction tank, and the output shaft of the driving motor passes through the reaction tank; The stability detection component includes: a detection partition board, a discharge pipe, a ball head, a swing shaft, a stability detection board and a discharge solenoid valve. The detection partition board is fixedly installed inside the reaction tank; four discharge pipes are fixedly installed on the reaction tank; the ball head is rotatably sleeved in the middle of the detection partition board; the bottom of the ball head is fixedly installed with a swing shaft, and the end of the swing shaft is an arc structure; the top of the ball head is fixedly installed with a stability detection board, and the stability detection board is in a "cross" shape structure; the stability detection board is connected to the detection partition board by four tension springs; discharge solenoid valves are respectively installed on the four discharge pipes; the stability detection component is used to detect the stability of the mixed solution and then conduct discharge; The hierarchical control component includes: a hierarchical control cover, a lifting column and a stability switch. The hierarchical control cover is threadedly connected to the bottom of the detection partition board; the lifting column is slidably inserted inside the hierarchical control cover; the top of the lifting column is a hemispherical structure; the top of the lifting column is aligned with the swing shaft; a stability switch is fixedly installed inside the hierarchical control cover, and the top of the stability switch is attached to the lifting column; a spring is connected to the bottom of the lifting column, and the spring at the bottom of the lifting column is located outside the stability switch; the stability switch is electrically connected to the four discharge solenoid valves; when the solution shakes, it drives the stability detection board to shake, the stability detection board will drive the ball head to rotate on the detection partition board, the swing shaft is driven to swing, the detection partition board is no longer aligned with the lifting column, and the discharge solenoid valve is controlled by the stability switch to close, avoiding excessive discharge of the solution.

2. The reactor for producing aluminosilicate according to claim 1, wherein: The reaction installation component further includes: stirring teeth and a liquid inlet pipe. Stirring teeth are fixedly installed on the output shaft of the driving motor; two liquid inlet pipes are fixedly installed on the top of the reaction tank, and the two liquid inlet pipes are respectively used to connect to the raw material pipes externally.

3. A reactor for producing aluminum silicate according to claim 1, characterized in that: The supernatant discharge component includes: a discharge coil pipe, a discharge check valve, a return pipe and a return solenoid valve. The discharge coil pipe is fixedly installed on the reaction tank; a discharge check valve is installed at the end of the discharge coil pipe; the discharge check valve is located inside the reaction tank; the discharge check valve is located below the detection partition board; the discharge coil pipe is formed by S-shaped bending; a return pipe is fixedly installed on the side of the discharge coil pipe; a return solenoid valve is installed on the return pipe; the return pipe is located above the detection partition board.

4. A reactor for producing aluminum silicate according to claim 3, characterized in that: The supernatant discharge component further includes: a port solenoid valve, a compressed gas cylinder and a gas cylinder solenoid valve. A port solenoid valve is installed at the outlet end of the discharge coil pipe; a compressed gas cylinder is fixedly installed on the discharge coil pipe; the air outlet pipe of the compressed gas cylinder is connected to the discharge coil pipe; the air outlet pipe of the compressed gas cylinder is located on one side close to the return solenoid valve; a gas cylinder solenoid valve is installed on the air outlet pipe of the compressed gas cylinder.

5. A reactor for producing aluminum silicate according to claim 4, characterized in that: The continuous precipitation detection component includes: a support frame, an independent switch, and a precipitation isolation filter block. A circle of through holes is provided on the support frame; the support frame is fixedly installed on the discharge coil pipe; two independent switches are fixedly installed on the support frame; the left independent switch is used to control the gas cylinder solenoid valve and the reflux solenoid valve to be normally closed, and the right independent switch is used to control the port solenoid valve to be normally open; a precipitation isolation filter block is slidably installed on the discharge coil pipe, and the precipitation isolation filter block is located above the independent switch; a spring is provided between the precipitation isolation filter block and the support frame; the precipitation isolation filter block is provided with filter holes.

6. The reactor for producing aluminum silicate according to claim 1, wherein: The anti-overdischarge component includes: a precipitation discharge pipe, a stop ring, and a precipitation solenoid valve. The precipitation discharge pipe is fixedly installed at the bottom of the reaction tank; a stop ring is fixedly sleeved inside the precipitation discharge pipe; a precipitation solenoid valve is installed at the end of the precipitation discharge pipe.

7. A reactor for producing aluminum silicate according to claim 6, characterized in that: The anti-overdischarge component further includes: a monitoring installation frame, a sliding sleeve, and a reset tension spring. A monitoring installation frame is fixedly installed at the top of the precipitation discharge pipe; a circle of through holes is provided on the monitoring installation frame; a sliding sleeve is fixedly installed at the bottom of the monitoring installation frame; a reset tension spring is sleeved inside the sliding sleeve.

8. A reactor for producing aluminum silicate according to claim 7, characterized in that: The anti-overdischarge component further includes: a stop disk, a switch frame, a closed switch, and an electromagnet. A sliding shaft is provided at the top of the stop disk; the sliding shaft at the top of the stop disk is slidably installed on the sliding sleeve; the reset tension spring is connected between the sliding shaft at the top of the stop disk and the monitoring installation frame; the stop disk elastically fits the stop ring; a switch frame is fixedly installed inside the precipitation discharge pipe, and a circle of through holes is provided on the switch frame; a closed switch is fixedly installed at the top of the switch frame, and the closed switch is located below the stop disk; an electromagnet is fixedly sleeved on the switch frame; the electromagnet is used to magnetically attract the stop disk; the electromagnet is externally connected with a control switch; the closed switch is electrically connected to the precipitation solenoid valve; a circle of slot holes is provided on the stop disk.

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