A wastewater recycling treatment device for quartz sand production

Abstract

The present invention relates to the technical field of wastewater recycling and treatment, and discloses a wastewater reuse treatment device for quartz sand production, comprising a flocculation tank body, a primary sedimentation component and an acid-base adjustment tank, etc. The primary sedimentation component is used for preliminarily separating large-particle impurities, the acid-base adjustment tank is used for adjusting the pH of the wastewater, and the flocculation tank body is divided into a first tank body and a second tank body by a partition component, and the functions can be alternating; the inclined tube component in the tank is driven up and down by a first elevator, and the upper and lower inclined tubes thereof are staggered and gradually expanded at the ends, so that the water flow can form multi-region vortexes and turbulence, thereby realizing efficient and uniform mixing of flocculant and water body. Compared with traditional blade stirring, the device can reduce floc breakage and improve sedimentation effect. At the same time, water flow flushing the inner wall can prevent the inclined tube from being blocked, thereby reducing maintenance cost. The device is convenient for realizing efficient treatment and recycling of quartz sand production wastewater, and has both environmental protection and economic benefits.

Description

Technical Field

[0001] The present invention relates to the technical field of wastewater recycling and treatment, in particular to a wastewater recycling and treatment device for quartz sand production. Background Art

[0002] Quartz sand wastewater typically contains large amounts of solid impurities such as quartz sand particles and suspended matter. It may also carry certain acidity, alkalinity, or other pollutants due to the production process. Sedimentation treatment uses gravity to naturally settle larger suspended matter in the wastewater, removing some solid impurities and reducing the turbidity of the wastewater. Flocculation, by adding flocculants, aggregates tiny colloidal particles and suspended matter in the wastewater to form larger flocs, further enhancing solid-liquid separation and removing more fine particles and some organic pollutants that are difficult to naturally settle. The synergistic effects of sedimentation, flocculation, and neutralization can effectively remove suspended matter and adjust the pH value in quartz sand wastewater, laying the foundation for subsequent advanced treatment and reuse, ensuring that the quality of the reused water meets relevant standards and usage requirements.

[0003] In Chinese Patent No. 201820773113.9, the utility model discloses an acid-base wastewater treatment device, comprising a support frame and an intermediate water tank, wherein a water inlet pipe of the auxiliary pipe zone is installed on one side of the bottom end of the outer wall of the support frame, a condensation zone vent pipe is installed on the outer wall of the support frame and the upper end of the water inlet pipe is installed, and the top of the support frame is fixedly connected to the auxiliary pipe condensation zone. In this acid-base wastewater treatment device, after sufficient mixing and reaction, the wastewater enters the inclined tube sedimentation zone, where suspended matter in the wastewater is settled and removed, and the settled sludge is conveniently discharged outward through the sludge discharge pipe. Since the suspended particles in the wastewater are relatively light and difficult to settle, the inclined tube sedimentation zone is designed to have a longer residence time. The effluent from the inclined tube sedimentation zone enters the intermediate water tank, and the effluent from the inclined tube sedimentation tank enters the intermediate water tank. The water in the intermediate water tank is lifted by the intermediate lifting pump to the sand filter and activated carbon filter to further remove the residual suspended matter in the wastewater, thereby achieving the effect of treating the acid-base wastewater.

[0004] In view of the above-mentioned and existing related technologies, the inventors believe that the following defects often exist: the flocculants themselves have a certain viscosity. When the water flow carries the flocculants through the inclined tube and the water flow rate is slow during the sedimentation process, these floccules are easy to adhere to the inner wall of the inclined tube. The long-term adhesion accumulation will gradually affect the water flow capacity of the inclined tube and its sedimentation effect. In addition, when mixing the flocculant and the water body, the existing wastewater treatment device usually uses the rotation of the stirring blade to achieve mixing. The shear force brought by the stirring blade can easily damage the formed flocculants. Summary of the Invention

[0005] The technical problem to be solved by the present invention is that in the prior art, flocs adhere to the inner wall of the inclined tube, and long-term accumulation will affect its performance. In addition, the existing treatment device usually uses rotating blades to mix the flocculant with the water, which easily destroys the formed flocs. For this reason, we propose a wastewater reuse treatment device for quartz sand production.

[0006] In order to achieve the above-mentioned purpose, the present application adopts the following technical scheme: a wastewater reuse treatment device for quartz sand production, comprising: a flocculation tank body, a support frame is installed inside the flocculation tank body, a first elevator is installed at the bottom of the support frame, an inclined pipe assembly is installed at the output end of the first elevator, the inclined pipe assembly includes an upper fixed layer, and the upper fixed layer is fixedly connected to the output end of the first elevator, and the upper fixed layer is slidably connected to the interior of the flocculation tank body, a plurality of upper inclined pipes are evenly arranged inside the upper fixed layer, a lower fixed layer is provided at the bottom of the upper fixed layer, a buffer layer cavity is formed by the enclosure between the lower fixed layer and the upper fixed layer, two groups of connecting blocks are symmetrically provided on the sides of the buffer layer cavity, and the top end of the connecting block is fixedly connected to the upper fixed layer, and the bottom end of the connecting block is fixedly connected to the lower fixed layer, a plurality of lower inclined pipes are evenly arranged inside the lower fixed layer, and the lower inclined pipes and the upper inclined pipes are staggered;

[0007] A partition assembly is provided in the middle of the flocculation tank body, and the partition assembly divides the interior of the flocculation tank body into two parts, a first tank body and a second tank body, of equal volume; a primary sedimentation assembly is provided on one side of the flocculation tank body, and an acid-base regulating tank is provided on the other side of the flocculation tank body; a first water pipe is fixedly connected to the top of the primary sedimentation assembly, two groups of second water pipes are fixedly connected to the output end of the first water pipe, and a valve is installed at the connection between the two groups of second water pipes, and one group of the second water pipes is connected to the first tank body, and the other group of the second water pipes is connected to the second tank body;

[0008] A flocculant dispenser is installed on the top of the flocculation tank body, and two groups of dosing ports are installed at the bottom of the flocculant dispenser, one group of dosing ports is connected to the first tank body, and the other group of dosing ports is connected to the second tank body.

[0009] Preferably, the end of the upper inclined tube close to the buffer layer cavity is configured to be gradually expanded, and the end of the lower inclined tube close to the buffer layer cavity is also configured to be gradually expanded.

[0010] Preferably, an overflow assembly is further provided inside the flocculation tank body, and the overflow assembly includes a second elevator, the second elevator is fixedly connected to the bottom of the support frame, and the output end of the second elevator is fixedly connected to the overflow pipe.

[0011] Preferably, a plurality of overflow holes are evenly opened on the side of the overflow pipe, and a water suction hose is fixedly connected to the end of the overflow pipe, and the water suction hose is communicated with the overflow pipe.

[0012] Preferably, the top end of the water suction hose is fixedly connected to a third water supply pipeline, and the output end of the third water supply pipeline is connected to the acid-base regulating tank.

[0013] Preferably, the partition assembly includes a partition plate, which is fixedly connected to the middle position inside the flocculation tank body. A water outlet is provided at the bottom of the partition plate, and the first tank body is connected to the second tank body through the water outlet.

[0014] Preferably, a servo motor is installed inside the partition plate, and an output end of the servo motor is fixedly connected to a transmission connecting rod, and the transmission connecting rod is rotatably connected to the inside of the partition plate.

[0015] Preferably, the bottom end of the transmission connecting rod is fixedly connected with a screw rod, the interior of the water outlet is slidably connected with a sealing plate, the screw rod is inserted into the interior of the sealing plate, and the screw rod and the sealing plate are threadedly connected.

[0016] Preferably, the primary sedimentation assembly includes a sedimentation tank, a buffer tube is coaxially arranged inside the sedimentation tank, a side of the buffer tube is connected to a water inlet pipe, and a mud discharge pipe is fixedly connected to the side of the interior of the sedimentation tank.

[0017] Preferably, an overflow trough is fixedly connected to the top of the sedimentation tank, and the overflow trough is communicated with the first water pipe.

[0018] Technical effects and advantages of the present invention:

[0019] The present invention is provided with two tank bodies with the same structure inside the flocculation tank body, and the mixing and sedimentation functions of the two tank bodies can be performed alternately. In the flocculation mixing link, a liftable inclined tube assembly structure is utilized, and the upper inclined tube and the lower inclined tube are designed with staggered and gradually expanded internal shapes. Multi-region and multi-directional vortexes and turbulence are generated through up and down movement. Compared with traditional blade stirring, it can achieve more uniform and efficient mixing of flocculant and water, and reduce floc breakage due to the soft three-dimensional flow field, thereby ensuring the sedimentation effect. At the same time, the water flow movement can also flush the inner wall of the inclined tube to prevent floc clogging and reduce maintenance costs. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] The disclosure of the present invention is illustrated with reference to the accompanying drawings. It should be understood that the drawings are for illustrative purposes only and are not intended to limit the scope of protection of the present invention. In the drawings, the same reference numerals are used to refer to the same components:

[0021] Figure 1 It is a schematic diagram of the overall three-dimensional structure of the present invention;

[0022] Figure 2 It is a schematic diagram of the three-dimensional structure of the flocculation tank body of the present invention;

[0023] Figure 3 It is a schematic diagram of the three-dimensional structure of the interior of the flocculation tank body of the present invention;

[0024] Figure 4 Schematic diagram of the cross-sectional structure of the inclined tube assembly of the present invention;

[0025] Figure 5 Schematic diagram of the three-dimensional structure of the overflow component of the present invention;

[0026] Figure 6 Schematic diagram of the cross-sectional structure of the separation component part of the present invention;

[0027] Figure 7 for Figure 6 Schematic diagram of the enlarged structure at A in the middle;

[0028] Figure 8 Schematic diagram of the internal structure of the primary precipitation component of the present invention;

[0029] Figure 9 It is a schematic diagram of the three-dimensional structure of the second water supply pipe and the flocculant dispenser of the present invention.

[0030] Legend: 1. Flocculation tank body; 2. Overflow assembly; 3. First elevator; 4. Inclined pipe assembly; 5. Partition assembly; 6. Support frame; 7. Primary sedimentation assembly; 8. Flocculant dispenser; 9. First water pipe; 10. Valve; 11. Second water pipe; 12. Acid-base regulating tank; 201. Second elevator; 202. Overflow pipe; 203. Overflow hole; 204. Suction hose; 205. Third water pipe Pipeline; 401, upper fixed layer; 402, upper inclined pipe; 403, connecting block; 404, lower fixed layer; 405, lower inclined pipe; 406, buffer layer cavity; 501, partition plate; 502, servo motor; 503, transmission connecting rod; 504, water outlet; 505, sealing plate; 506, screw; 701, sedimentation tank; 702, buffer pipe; 703, water inlet pipe; 704, mud discharge pipe; 705, overflow trough. DETAILED DESCRIPTION

[0031] It is easy to understand that according to the technical solution of the present invention, without changing the essential spirit of the present invention, a person skilled in the art can propose a variety of interchangeable structural modes and implementation modes. Therefore, the following specific embodiments and drawings are only exemplary descriptions of the technical solution of the present invention and should not be regarded as the entire invention or as a limitation or restriction of the technical solution of the present invention.

[0032] Reference Figure 1 and Figure 8 As shown, the present invention provides a technical solution: a wastewater reuse treatment device for quartz sand production, including a primary sedimentation component 7, the primary sedimentation component 7 includes a sedimentation tank 701, a buffer pipe 702 is coaxially arranged inside the sedimentation tank 701, the side of the buffer pipe 702 is connected to a water inlet pipe 703, a mud discharge pipe 704 is fixedly connected to the side of the inside of the sedimentation tank 701, and an overflow trough 705 is fixedly connected to the top of the sedimentation tank 701, and the overflow trough 705 is connected to the first water supply pipe 9.

[0033] The wastewater generated during the production of quartz sand enters the interior of the buffer pipe 702 through the water inlet pipe 703 and flows downward along the buffer pipe 702 into the interior of the sedimentation tank 701. The buffer pipe 702 is used to weaken the impact of the incoming water flow on the sediment settled at the bottom. Under the action of gravity, some large particles of sediment and other impurities in the wastewater settle at the bottom of the sedimentation tank 701 and are discharged to the outside through the mud discharge pipe 704. The water after the preliminary sedimentation treatment enters the interior of the overflow trough 705 and is transported to the interior of the flocculation tank body 1 through the first water supply pipe 9 for subsequent flocculation treatment.

[0034] See also Figure 2 、 Figure 3 、 Figure 4 and Figure 9 As shown, a partition component 5 is provided in the middle position of the flocculation tank body 1, and the partition component 5 divides the interior of the flocculation tank body 1 into two parts, a first tank body and a second tank body, of equal volume. A primary sedimentation component 7 is provided on one side of the flocculation tank body 1, and an acid-base regulating tank 12 is provided on the other side of the flocculation tank body 1. A first water pipe 9 is fixedly connected to the top of the primary sedimentation component 7, and two groups of second water pipes 11 are fixedly connected to the output end of the first water pipe 9, and a valve 10 is installed at the connection between the two groups of second water pipes 11, and one group of the second water pipes 11 is connected to the first tank body, and the other group of the second water pipes 11 is connected to the second tank body. A flocculant dispenser 8 is installed on the top of the flocculation tank body 1, and two groups of drug injection ports are installed at the bottom end of the flocculant dispenser 8, one group of drug injection ports is connected to the first tank body, and the other group of drug injection ports is connected to the second tank body.

[0035] Under the control of the valve 10, the first water pipe 9 can only discharge the water that has undergone preliminary sedimentation treatment into the interior of the flocculation tank body 1 through one group of the second water pipes 11. When discharged into the first tank body inside the flocculation tank body 1, the group of dosing ports corresponding to the lower end of the flocculant dosing machine 8 also dosing flocculant into the interior of the first tank body. At this time, the first tank body plays a role in mixing and stirring the flocculant and the water body. After the flocculant and the water body are mixed, they are passed into the interior of the second tank body together. At this time, the second tank body plays a role in settling the flocs.

[0036] A support frame 6 is installed inside the flocculation tank body 1, a first elevator 3 is installed at the bottom of the support frame 6, an inclined tube assembly 4 is installed at the output end of the first elevator 3, the inclined tube assembly 4 includes an upper fixed layer 401, and the upper fixed layer 401 is fixedly connected to the output end of the first elevator 3, and the upper fixed layer 401 is slidably connected to the inside of the flocculation tank body 1, a plurality of upper inclined tubes 402 are evenly arranged inside the upper fixed layer 401, a lower fixed layer 404 is provided at the bottom of the upper fixed layer 401, and a space is formed between the lower fixed layer 404 and the upper fixed layer 401. The baffle comprises a buffer layer cavity 406, and two groups of connecting blocks 403 are symmetrically arranged on the sides of the buffer layer cavity 406. The top ends of the connecting blocks 403 are fixedly connected to the upper fixed layer 401, and the bottom ends of the connecting blocks 403 are fixedly connected to the lower fixed layer 404. A number of lower inclined tubes 405 are evenly arranged inside the lower fixed layer 404. The lower inclined tubes 405 are staggered with the upper inclined tubes 402. The end of the upper inclined tube 402 close to the buffer layer cavity 406 is set to a gradually expanding shape, and the end of the lower inclined tube 405 close to the buffer layer cavity 406 is also set to a gradually expanding shape.

[0037] Inside the first tank body that plays a mixing role, after the water and flocculant are added, the first elevator 3 is started, and the output end of the first elevator 3 carries the inclined tube assembly 4 as a whole to move up and down inside the flocculation tank body 1. When the inclined tube assembly 4 rises, the water flows in from the upper inclined tube 402 and is finally discharged from the lower inclined tube 405. When the overall water flow layer is divided into multiple tributaries and enters the interior of each upper inclined tube 402, a number of vortices will be formed at the inlet of each upper inclined tube 402. When it flows from the bottom end of the upper inclined tube 402 into the interior of the buffer layer cavity 406, a number of vortices will be formed at the outlet of each upper inclined tube 402, and the aggregation will be completed inside the buffer layer cavity 406, and it will be divided into several tributaries again through the top of the lower inclined tube 405. At the same time, it will have a disturbing effect on the water flow, and the outlet end of the upper inclined tube 402 and the inlet end of the lower inclined tube 405 are staggered to facilitate mixing of water at each branch, and finally discharged outward from the bottom end of the lower inclined tube 405, and forming a number of vortices at the end of the lower inclined tube 405. When the inclined tube assembly 4 descends, the process is the opposite. During the back and forth lifting and lowering process of the inclined tube assembly 4, multiple vortices can be formed repeatedly on the water body inside the first tank body. In this process, after the flocculant is added, it will be continuously dispersed and diffused to the entire water body under the action of the vortex and turbulence caused by the movement of the inclined tube assembly 4, breaking the concentration gradient and achieving uniform mixing with the wastewater; at the same time, the up and down movement of the inclined tube layer can also continuously update the contact interface between the water and the inclined tube surface, thereby enhancing the mass transfer process.

[0038] Traditional blade stirring relies on mechanical rotation to generate unidirectional shear force. When rotating at high speed, it is easy to apply concentrated external force to the formed flocs, causing the flocs to break. The vortex and turbulence caused by the lifting and lowering of the inclined tube assembly 4 in this application belong to the three-dimensional flow field effect. The direction of the water flow is constantly changing and the shear force distribution is more uniform. The shear force in a single vortex is smaller, and the impact on the flocs is softer, which can reduce the breakage of the flocs and better maintain the integrity of the flocculent material, which is conducive to subsequent sedimentation. On the other hand, when the inclined tube assembly 4 moves, the water flows through the gradually expanding pipe mouth, the staggered pipe mouth and the buffer layer cavity 406 and other structures, forming multi-region and multi-directional vortices at different positions. Compared with traditional blade stirring, this mixing method has more comprehensive coverage. At the same time, the up and down reciprocating motion of the inclined tube layer continuously updates the contact interface between the water and the inclined tube surface, strengthens the mass transfer process, and makes the flocculant and water body more efficiently and evenly mixed in the three-dimensional flow field. The mixing efficiency is significantly improved, and the problem of floc destruction caused by local high shear force in traditional stirring is avoided.

[0039] During the lifting and lowering process of the inclined tube assembly 4, the water flow will pass back and forth repeatedly from the upper inclined tube 402 and the lower inclined tube 405 inside it, and under the contraction effect of its gradually expanding port, it can generate a certain scouring force on the inner walls of the upper inclined tube 402 and the lower inclined tube 405, and the flocs have the characteristics of loose structure and weak adhesion. The scouring force generated by the water flow passing through the upper inclined tube 402 and the lower inclined tube 405 is sufficient to separate the flocs and impurities attached to their inner walls, effectively preventing their accumulation and ensuring the smooth passage. At the same time, it reduces the problems of reduced treatment efficiency and water quality deterioration caused by blockage, reduces the frequency of equipment maintenance, ensures the stable and efficient operation of the mixing and subsequent sedimentation treatment processes, completes scouring and cleaning while mixing, and regularly exchanges the functions of the first and second tank bodies so that both tank bodies have the opportunity to play the mixing function within a certain period of time and scour the inner walls of their inclined tubes at the same time. There is no need to drain all the water inside the entire tank body and then clean it specifically, which is convenient for saving manpower and material resources.

[0040] See also Figure 6 and Figure 7 The partition assembly 5 includes a partition plate 501, which is fixedly connected to the middle position inside the flocculation tank body 1. A water outlet 504 is provided at the bottom of the partition plate 501. The first tank body is connected to the second tank body through the water outlet 504. A servo motor 502 is installed inside the partition plate 501. The output end of the servo motor 502 is fixedly connected to a transmission connecting rod 503. The transmission connecting rod 503 is rotatably connected to the inside of the partition plate 501. The bottom end of the transmission connecting rod 503 is fixedly connected to a screw 506. The inside of the water outlet 504 is slidably connected to a sealing plate 505. The screw 506 is inserted into the inside of the sealing plate 505, and the screw 506 and the sealing plate 505 are threadedly connected.

[0041] The output end of the servo motor 502 rotates forward or reverse through the transmission connecting rod 503 with the screw 506, and then can drive the sealing plate 505 to rise or fall, so that the sealing plate 505 can be used to complete the opening or blocking of the water outlet 504. When one of the pools is raised and lowered with the inclined tube assembly 4 to mix the flocculant and wastewater, the sealing plate 505 closes the water outlet 504 to prevent the wastewater from invading another pool body. When the flocculant mixing is completed and the flocs are generated, the wastewater needs to be transferred to complete the sedimentation of the flocs. The sealing plate 505 moves upward to open the water outlet 504, and the wastewater can be transferred to another pool body through the water outlet 504.

[0042] See also Figure 3 and Figure 5 As shown, an overflow assembly 2 is also provided inside the flocculation tank body 1, and the overflow assembly 2 includes a second elevator 201, and the second elevator 201 is fixedly connected to the bottom of the support frame 6. The output end of the second elevator 201 is fixedly connected to the overflow pipe 202, and a number of overflow holes 203 are evenly opened on the side of the overflow pipe 202. The end of the overflow pipe 202 is fixedly connected to a water suction hose 204, and the water suction hose 204 is connected to the overflow pipe 202. The top of the water suction hose 204 is fixedly connected to a third water supply pipe 205, and the output end of the third water supply pipe 205 is connected to the acid-base adjustment tank 12.

[0043] In the pool body that plays a sedimentation role, the flocs settle below the inclined tube assembly 4, and the wastewater after flocculation treatment enters the overflow pipe 202 through the overflow hole 203, and is transported into the interior of the acid-base adjustment tank 12 through the water suction hose 204 and the third water supply pipe 205, and is mixed with the reagents put into the acid-base adjustment tank 12 to adjust its pH. After the adjustment is completed, it can be transferred to the quartz sand production line for reuse. The output end of the second elevator 201 can be adjusted in height with the overflow pipe 202, so that the liquid level inside the pool body that plays a sedimentation role is lower than the liquid level inside the pool body that plays a stirring role, so that the waste liquid containing flocs after being mixed with the flocculant can enter the interior of the pool body that plays a sedimentation role through the sealing plate 505 below the partition assembly 5.

[0044] The technical scope of the present invention is not limited to the contents of the above description. Those skilled in the art can make various deformations and modifications to the above embodiments without departing from the technical idea of ​​the present invention, and these deformations and modifications should all fall within the protection scope of the present invention.

Claims

1. A quartz sand production wastewater recycling treatment device, characterized in that: The invention comprises a flocculation tank body, wherein a support frame is installed inside the flocculation tank body, a first elevator is installed at the bottom of the support frame, an inclined tube assembly is installed at the output end of the first elevator, the inclined tube assembly comprises an upper fixed layer, and the upper fixed layer is fixedly connected to the output end of the first elevator, and the upper fixed layer is slidably connected to the interior of the flocculation tank body, a plurality of upper inclined tubes are evenly arranged inside the upper fixed layer, a lower fixed layer is provided at the bottom of the upper fixed layer, a buffer layer cavity is formed by the enclosure between the lower fixed layer and the upper fixed layer, a plurality of lower inclined tubes are evenly arranged inside the lower fixed layer, and the lower inclined tubes and the upper inclined tubes are staggered; A partition assembly is provided in the middle of the flocculation tank body, and the partition assembly divides the interior of the flocculation tank body into two parts, a first tank body and a second tank body, of equal volume; a primary sedimentation assembly is provided on one side of the flocculation tank body, and an acid-base regulating tank is provided on the other side of the flocculation tank body; a first water pipe is fixedly connected to the top of the primary sedimentation assembly, two groups of second water pipes are fixedly connected to the output end of the first water pipe, and a valve is installed at the connection between the two groups of second water pipes, and one group of the second water pipes is connected to the first tank body, and the other group of the second water pipes is connected to the second tank body; A flocculant dispenser is installed on the top of the flocculation tank body, and two groups of dosing ports are installed at the bottom of the flocculant dispenser, one group of dosing ports is connected to the first tank body, and the other group of dosing ports is connected to the second tank body; One end of the upper inclined tube close to the buffer layer cavity is configured to be gradually expanded, and one end of the lower inclined tube close to the buffer layer cavity is also configured to be gradually expanded. Two groups of connecting blocks are symmetrically provided on the sides of the buffer layer cavity, and the top ends of the connecting blocks are fixedly connected to the upper fixed layer, and the bottom ends of the connecting blocks are fixedly connected to the lower fixed layer. The mixing and sedimentation functions of the first and second tank bodies can be carried out alternately. In the flocculation and mixing stage, a liftable inclined tube assembly structure is utilized. The upper and lower inclined tubes are staggered and gradually expanded internally. Multi-region and multi-directional vortices and turbulence are generated through up and down movements. This can not only achieve more uniform and efficient mixing of flocculants and water bodies, but also reduce floc breakage due to the soft three-dimensional flow field, thereby ensuring the sedimentation effect. At the same time, the water flow movement can also flush the inner wall of the inclined tube to prevent floc clogging.

2. The quartz sand production wastewater recycling treatment device according to claim 1, characterized in that: An overflow assembly is also provided inside the flocculation tank body. The overflow assembly includes a second elevator. The second elevator is fixedly connected to the bottom of the support frame. The output end of the second elevator is fixedly connected to the overflow pipe.

3. The quartz sand production wastewater recycling treatment device according to claim 2, characterized in that: A plurality of overflow holes are evenly opened on the side of the overflow pipe, and a water suction hose is fixedly connected to the end of the overflow pipe, and the water suction hose is communicated with the overflow pipe.

4. The quartz sand production wastewater recycling treatment device according to claim 3, characterized in that: The top end of the water suction hose is fixedly connected to a third water delivery pipeline, and the output end of the third water delivery pipeline is communicated with the acid-base regulating tank.

5. The quartz sand production wastewater recycling treatment device according to claim 1, characterized in that: The partition assembly includes a partition plate, which is fixedly connected to the middle position of the flocculation tank body. A water outlet is provided at the bottom of the partition plate, and the first tank body is connected to the second tank body through the water outlet.

6. The quartz sand production wastewater recycling treatment device according to claim 5, characterized in that: A servo motor is installed inside the partition plate. An output end of the servo motor is fixedly connected to a transmission connecting rod, and the transmission connecting rod is rotatably connected to the inside of the partition plate.

7. The quartz sand production wastewater recycling treatment device according to claim 6, characterized in that: The bottom end of the transmission connecting rod is fixedly connected with a screw rod, the interior of the water outlet is slidably connected with a blocking plate, the screw rod is inserted into the blocking plate, and the screw rod and the blocking plate are threadedly connected.

8. The quartz sand production wastewater recycling treatment device according to claim 1, characterized in that: The primary sedimentation assembly includes a sedimentation tank, a buffer tube is coaxially arranged inside the sedimentation tank, a side of the buffer tube is connected to a water inlet pipe, and a mud discharge pipe is fixedly connected to the side of the interior of the sedimentation tank.

9. The quartz sand production wastewater recycling treatment device according to claim 8, characterized in that: The top of the sedimentation tank is fixedly connected with an overflow trough, and the overflow trough is communicated with the first water pipe.

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