Nanometer slurry separator for zirconium silicate ultrafine powder production

By designing a nanoslurry separator in the production of zirconium silicate ultrafine powder, using the dual centrifugal force of the feed pipe and spiral blades, combined with the re-separation operation of the filter mechanism, the problem of mixing coarse materials and fine materials of the separator is solved, and the problem of mixing the separator with fine materials is improved. Production rates and reduce costs.

CN222197372UActive Publication Date: 2024-12-20TANGSHAN KANGTAO NEW MATERIALS CO LTD
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Patent Information

Application Number
CN202420878103.7
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-04-25
Publication Date
2024-12-20
Estimated Expiration
2034-04-25

AI Technical Summary

Technical Problem

During the separation process of existing zirconium silicate ultrafine powder production and separator, the coarse material is easily mixed with fine materials, resulting in increased workload and production cost of secondary processing, affecting the production rate of zirconium silicate ultrafine powder.

Method used

A nano slurry separator is designed, using a feed pipe to set along the tangent direction of the shell, combining the rotating shaft and the spiral blade to generate double centrifugal force, and the slurry is roughly filtered and centrifuged again to reduce the medium-coarse material. The amount of mixed fine material.

Benefits of technology

More complete slurry separation is achieved, the production rate of zirconium silicate ultrafine powder is improved, and the production cost is reduced.

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Abstract

The utility model relates to the technical field of zirconium silicate superfine powder production equipment, and provides a nano slurry separator for zirconium silicate superfine powder production, which comprises a shell, a feeding pipe convenient for zirconium silicate slurry to enter is fixedly communicated with one side of the shell, a rotating shaft is rotatably mounted in the center of an inner cavity of the shell, and a spiral blade is fixed on the outer wall of the rotating shaft. The feeding pipe is arranged in the tangential direction of the shell, slurry can rotate along the inner wall of the shell when entering the shell, so that centrifugal force is generated, the slurry is separated more completely in cooperation with centrifugal force and double centrifugation generated by the rotating shaft and the spiral blades, and the separation effect is guaranteed. The filtering mechanism can roughly filter slurry discharged from the bottom of the shell, the filtered slurry is guided into the feeding pipe again through the slurry pump, centrifugal separation operation is conducted again, the amount of mixed fine materials in medium-coarse materials is reduced, and therefore the production rate of the zirconium silicate superfine powder is increased, and the production cost is reduced.
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Description

Technical Field

[0001] The utility model relates to the technical field of zirconium silicate ultrafine powder production equipment, and specifically relates to a nano-slurry separator for zirconium silicate ultrafine powder production. Background Art

[0002] Zirconium silicate has the advantages of high temperature resistance, strong corrosion resistance, good wear resistance, strong impact toughness and long service life. It is widely used in float glass additives, ceramic glazes, ceramic sandblasting and ceramic grinding beads. High-purity ultrafine zirconium silicate powder and microbeads are the development trend of zirconium silicate powder. In the production process of zirconium silicate ultrafine powder, a separator is needed to centrifuge the raw liquid slurry to produce qualified zirconium silicate ultrafine powder.

[0003] However, during the use of the existing separator, the coarse material produced during the separation process is easily mixed with the fine material. If it is directly discharged for secondary processing, the workload of the secondary processing will increase, the production cost will be increased, and the production rate of the zirconium silicate ultrafine powder will also be affected. Utility Model Content

[0004] The utility model provides a nano-slurry separator for producing zirconium silicate ultrafine powder, which solves the problem that during the use of the separator in the related technology, coarse materials generated in the separation process are easily mixed with fine materials. If they are directly discharged for secondary processing, the workload of the secondary processing will be increased, the production cost will be increased, and the production rate of the zirconium silicate ultrafine powder will also be affected.

[0005] The technical solution of the utility model is as follows:

[0006] A nano-slurry separator for producing zirconium silicate ultrafine powder comprises a shell, one side of the shell is fixedly connected with a feed pipe for convenient entry of zirconium silicate slurry, a rotating shaft is rotatably installed at the center of the inner cavity of the shell, the outer wall of the rotating shaft is fixed with a spiral blade, the top of the rotating shaft is fixed with a liquid guide tube, the top of the liquid guide tube passes through the top wall of the shell through a leakproof bearing and is fixed with a rotating joint, the top of the rotating joint is fixed with a fine material outlet pipe, the outer wall of the liquid guide tube is fixed with a No. 1 gear, the No. 1 gear is meshingly connected with a No. 2 gear, the top wall of the shell is fixed with a driving motor, the power shaft at the top of the driving motor is fixedly connected to the bottom axis position of the No. 2 gear, the top wall of the shell is fixed with a protective shell corresponding to the position of the driving motor and the liquid guide tube, the protective shell is fixedly connected to the fine material outlet pipe, the bottom end of the shell is fixedly connected with a filtering mechanism, a slurry pump is arranged on one side of the filtering mechanism, the feed port of the slurry pump is connected to the bottom of the filtering mechanism through a No. 1 connecting pipe, and the discharge port of the slurry pump is fixedly connected to the feed pipe through a No. 2 connecting pipe.

[0007] Preferably, both upper and lower ends of the rotating shaft are hollow, and a plurality of material guide grooves are symmetrically provided on the side walls at both upper and lower ends of the rotating shaft.

[0008] Preferably, the filtering mechanism includes an outer shell fixed at the bottom end of the shell, a coarse filter plate arranged obliquely is fixed in the outer shell, a coarse material outlet pipe is fixedly connected to the side wall of the outer shell, a discharge pipe is fixedly connected to the bottom wall of the outer shell, and the discharge pipe is fixedly connected to one end of a No. 1 connecting pipe.

[0009] Preferably, the outer shell and the bottom of the housing are both conical.

[0010] Preferably, the ports of the coarse material outlet pipe, the feed pipe and the fine material outlet pipe are all provided with connecting flanges.

[0011] Preferably, the feed pipe is arranged along the tangential direction of the shell.

[0012] The beneficial effects of the utility model are:

[0013] 1. The feed pipe provided in the utility model is arranged along the tangential direction of the shell, so that the slurry can rotate along the inner wall of the shell when entering the shell, thereby generating centrifugal force. Combined with the centrifugal force generated by the rotating shaft and the spiral blades, double centrifugation makes the slurry separation more complete and ensures the separation effect.

[0014] 2. The filtering mechanism provided in the utility model can roughly filter the slurry discharged from the bottom of the shell. The filtered slurry is reintroduced into the feed pipe through a slurry pump and centrifuged again to reduce the amount of mixed fine material in the coarse material, thereby increasing the production rate of ultrafine zirconium silicate powder and reducing production costs. BRIEF DESCRIPTION OF THE DRAWINGS

[0015] The utility model is further described in detail below in conjunction with the accompanying drawings and specific implementation methods.

[0016] Figure 1 This is a three-dimensional diagram of the external structure of the utility model;

[0017] Figure 2 This is a three-dimensional diagram of the internal structure of the housing of the utility model;

[0018] Figure 3 This is a three-dimensional diagram of the rotating shaft structure of the utility model;

[0019] Figure 4 It is a three-dimensional diagram of the filter mechanism structure of the utility model.

[0020] In the figure: 1. Shell; 2. Feed pipe; 3. Rotating shaft; 4. Spiral blade; 5. Liquid guide tube; 6. Rotary joint; 7. Fine material outlet pipe; 8. Gear No. 1; 9. Gear No. 2; 10. Driving motor; 11. Protective shell; 12. Filter mechanism; 121. Outer shell; 122. Coarse filter plate; 123. Discharge pipe; 13. Coarse material outlet pipe; 14. Connecting pipe No. 1; 15. Slurry pump; 16. Connecting pipe No. 2; 17. Connecting flange; 18. Material guide trough. DETAILED DESCRIPTION

[0021] The following will be combined with the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.

[0022] Example 1

[0023] like Figure 1~Figure 2 As shown, this embodiment proposes:

[0024] A nano-slurry separator for producing ultrafine zirconium silicate powder comprises a shell 1, one side of the shell 1 is fixedly connected with a feed pipe 2 for convenient entry of zirconium silicate slurry, a rotating shaft 3 is rotatably installed at the center of the inner cavity of the shell 1, a spiral blade 4 is fixed on the outer wall of the rotating shaft 3, a liquid guide tube 5 is fixed on the top of the rotating shaft 3, the top of the liquid guide tube 5 passes through the top wall of the shell 1 through a leakproof bearing and is fixed with a rotating joint 6, a fine material outlet pipe 7 is fixed on the top of the rotating joint 6, a No. 1 gear 8 is fixed on the outer wall of the liquid guide tube 5, and the No. 1 gear 8 is meshedly connected with a No. 2 gear 9, A driving motor 10 is fixed to the top wall of the shell 1, and a power shaft on the top of the driving motor 10 is fixedly connected to the bottom axis position of the No. 2 gear 9. A protective shell 11 is fixed to the top wall of the shell 1 corresponding to the position of the driving motor 10 and the liquid guide tube 5. The protective shell 11 is fixedly connected to the fine material outlet pipe 7. A filtering mechanism 12 is fixedly connected to the bottom end of the shell 1. A slurry pump 15 is provided on one side of the filtering mechanism 12. The feed port of the slurry pump 15 is connected to the bottom of the filtering mechanism 12 through a No. 1 connecting pipe 14, and the discharge port of the slurry pump 15 is fixedly connected to the feed pipe 2 through a No. 2 connecting pipe 16.

[0025] In this embodiment, the feed pipe 2 is used to introduce zirconium silicate slurry into the shell 1, and the drive motor 10 drives the first gear 8 to rotate through the second gear 9. The first gear 8 drives the liquid guide tube 5 to rotate during the rotation. The liquid guide tube 5 can drive the rotating shaft 3 and the spiral blade 4 to rotate during the rotation, thereby driving the zirconium silicate slurry to rotate in the shell 1. The large solid particles in the zirconium silicate slurry are thrown onto the inner wall of the shell 1 under the action of centrifugal force, and flow down along the inner wall of the shell 1 to the bottom of the shell 1 in a spiral line, and then enter the filtering mechanism 12. The finer particles carried in the liquid of the zirconium silicate slurry rise and are discharged through the fine material outlet pipe 7. The protective shell 11 is used to protect the drive motor 10 and the first gear 8 and the second gear 9. The filtering mechanism 12 is used to roughly filter the slurry discharged from the bottom of the shell 1. The filtered slurry is re-introduced into the feed pipe 2 through the slurry pump 15, and the centrifugal separation operation is performed again, and the coarse material produced by the filtration is discharged through the coarse material outlet pipe 13.

[0026] The upper and lower ends of the rotating shaft 3 are hollow, and the side walls of the upper and lower ends of the rotating shaft 3 are symmetrically provided with a plurality of material guide grooves 18. The feed pipe 2 is arranged along the tangent direction of the housing 1.

[0027] In this embodiment, the guide grooves 18 provided at both ends of the rotating shaft 3 can ensure that the top slurry after centrifugation can be discharged through the fine material outlet pipe 7, and the bottom slurry after centrifugation can smoothly enter the filtering mechanism 12. The feed pipe 2 is arranged along the tangential direction of the shell 1, so that the slurry can rotate along the inner wall of the shell 1 when entering the shell 1, thereby generating centrifugal force, and the centrifugal force generated by the rotating shaft 3 and the spiral blades 4, double centrifugation, so that the slurry separation is more complete, ensuring the separation effect.

[0028] Example 2

[0029] like Figure 3~Figure 4 As shown, based on the same concept as the above-mentioned embodiment 1, this embodiment further proposes:

[0030] The filter mechanism 12 includes a shell 121 fixed to the bottom end of the housing 1, a coarse filter plate 122 arranged obliquely is fixed in the shell 121, a coarse material outlet pipe 13 is fixedly connected to the side wall of the shell 121, a discharge pipe 123 is fixedly connected to the bottom wall of the shell 121, and the discharge pipe 123 is fixedly connected to one end of the No. 1 connecting pipe 14. The bottoms of the shell 121 and the housing 1 are both conical. The ports of the coarse material outlet pipe 13, the feed pipe 2 and the fine material outlet pipe 7 are all provided with connecting flanges 17.

[0031] In this embodiment, the filter mechanism 12 is used to roughly filter the slurry discharged from the bottom of the housing 1, and the filtered slurry is re-introduced into the feed pipe 2 through the slurry pump 15, and the centrifugal separation operation is performed again, and the coarse material produced by the filtration is discharged through the coarse material outlet pipe 13. The connecting flanges 17 provided at the ports of the coarse material outlet pipe 13, the feed pipe 2 and the fine material outlet pipe 7 can facilitate their connection with the corresponding pipelines.

[0032] The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention should be included in the protection scope of the present invention.

Claims

1. A nano-slurry separator for producing ultrafine zirconium silicate powder, characterized in that: The invention comprises a shell (1), one side of the shell (1) is fixedly connected to a feed pipe (2) for facilitating the entry of zirconium silicate slurry, a rotating shaft (3) is rotatably mounted in the center of the inner cavity of the shell (1), a spiral blade (4) is fixed to the outer wall of the rotating shaft (3), a liquid guide tube (5) is fixed to the top of the rotating shaft (3), the top of the liquid guide tube (5) passes through the top wall of the shell (1) through a leakproof bearing and is fixed to a rotating joint (6), a fine material outlet pipe (7) is fixed to the top of the rotating joint (6), a first gear (8) is fixed to the outer wall of the liquid guide tube (5), the first gear (8) is meshingly connected to a second gear (9), and a A driving motor (10), wherein a power shaft at the top of the driving motor (10) is fixedly connected to the bottom axis position of the second gear (9), a protective shell (11) is fixedly provided on the top wall of the housing (1) at positions corresponding to the driving motor (10) and the liquid guide tube (5), the protective shell (11) is fixedly connected to the fine material outlet pipe (7), the bottom end of the housing (1) is fixedly connected to a filter mechanism (12), a slurry pump (15) is provided on one side of the filter mechanism (12), a feed port of the slurry pump (15) is connected to the bottom of the filter mechanism (12) via a first connecting pipe (14), and a discharge port of the slurry pump (15) is fixedly connected to the feed pipe (2) via a second connecting pipe (16).

2. The nano-slurry separator for producing ultrafine zirconium silicate powder according to claim 1, characterized in that: The upper and lower ends of the rotating shaft (3) are both hollow, and the side walls at the upper and lower ends of the rotating shaft (3) are both symmetrically provided with a plurality of material guide grooves (18).

3. The nano-slurry separator for producing ultrafine zirconium silicate powder according to claim 1, characterized in that: The filtering mechanism (12) comprises a shell (121) fixed to the bottom end of the housing (1), a coarse filter plate (122) arranged obliquely is fixed inside the shell (121), a coarse material outlet pipe (13) is fixedly connected to the side wall of the shell (121), a discharge pipe (123) is fixedly connected to the bottom wall of the shell (121), and the discharge pipe (123) is fixedly connected to one end of a No. 1 connecting pipe (14).

4. The nano-slurry separator for producing ultrafine zirconium silicate powder according to claim 3, characterized in that: The bottoms of the outer shell (121) and the housing (1) are both arranged in a conical shape.

5. The nano-slurry separator for producing ultrafine zirconium silicate powder according to claim 3, characterized in that: The ports of the coarse material outlet pipe (13), the feed pipe (2) and the fine material outlet pipe (7) are all provided with connecting flanges (17).

6. The nano-slurry separator for producing ultrafine zirconium silicate powder according to claim 1, characterized in that: The feed pipe (2) is arranged along the tangential direction of the shell (1).