Reaction filtering device for calcium iodate production

By designing a reaction filtration device for calcium iodate production, the problem of long-term use of traditional preparation methods is solved, efficient mixing and filtration is achieved, and production efficiency is significantly improved.

CN222550863UActive Publication Date: 2025-03-04唐山金碘新材料科技有限责任公司
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Patent Information

Application Number
CN202421012126.6
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-05-11
Publication Date
2025-03-04
Estimated Expiration
2034-05-11

AI Technical Summary

Technical Problem

The traditional calcium iodate preparation method takes a long time and affects production efficiency.

Method used

A reaction filtration device for the production of calcium iodate was designed, including a calcium salt solution tank, an iodate solution tank, a filtration reactor and a processing bracket. The efficient mixing and filtration of liquids were achieved through the quantitative drainage structure and the filter structure.

Benefits of technology

The liquid mixing is pushed by rotating airflow, which improves the mixing efficiency and uniformity; through circulating flow and liquid level control, the continuous reaction and the purity of the product are ensured, and the production efficiency is significantly improved.

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Abstract

The utility model discloses a reaction filtering device for calcium iodate production, which comprises a calcium salt solution tank, an iodate solution tank, a filtering reaction kettle and a processing bracket, and relates to the technical field of calcium iodate production, two liquids are mixed and stirred through the pushing of rotating airflow, and the mixing efficiency and uniformity are improved; through the operation of the drainage two-way pump, the circular flow of gas between the filtering reaction kettle and the transfer inflatable airbag is realized, the stable air pressure in the reaction kettle is maintained, and the proceeding of the reaction is facilitated; the liquid level on the inner side of the filtering reaction kettle is accurately controlled through the expansion of the inner expansion circular ring air bag, so that the reacted liquid can be smoothly drained into the J-shaped siphon drainage tube.
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Description

Technical Field

[0001] The utility model relates to the technical field of calcium iodate production, in particular to a reaction filtering device for calcium iodate production. Background Art

[0002] Calcium iodate is a white crystal or powder, odorless and tasteless, with a melting point of up to 540°C (decomposition). It is slightly soluble in water, but insoluble in alcohol solvents, but soluble in nitric acid, showing stable chemical properties. Usually, calcium iodate is prepared by reacting sodium iodate solution with calcium chloride solution.

[0003] The traditional preparation method is to dissolve the calcium salt solid in water, and after careful filtration, inject the solution into a reactor filled with iodate solution. After the reaction is carried out for a period of time, solid calcium iodate can be obtained by filtration. However, this production method is time-consuming and not conducive to improving production efficiency. Therefore, it is necessary to seek a faster and more efficient preparation method to meet production needs. In view of this, in-depth research on the above issues has led to the creation of this case. Utility Model Content

[0004] To achieve the above purpose, the utility model is implemented through the following technical scheme: a reaction filtration device for calcium iodate production, comprising: a calcium salt solution tank, an iodate solution tank, a filtration reactor and a processing bracket, wherein the calcium salt solution tank, the iodate solution tank and the filtration reactor are installed on the processing bracket, the calcium salt solution tank and the iodate solution tank are connected to the filtration reactor through a quantitative drainage structure, and a filtration structure is installed on the inner side of the filtration reactor;

[0005] The filtering structure comprises: a partition filter plate, two pairs of J-shaped siphon suction pipes, two pairs of filter set rings, two pairs of filter screens, two pairs of Tesla valve inner tubes, a plurality of trumpet-shaped limit plates, two pairs of arc drainage shaft tubes, two pairs of threaded inner blades, two pairs of inflation valves, two pairs of drainage bidirectional pumps, two pairs of transfer inflation airbags, inner expansion ring airbags and inner expansion drainage bidirectional pumps;

[0006] The partition filter plate is installed on the inner side of the filtering reactor, two pairs of the J-shaped siphon suction flow tubes are inserted into the partition filter plate in a cross shape, two pairs of the filter set rings are respectively mounted on the two pairs of the J-shaped siphon suction flow tubes, two pairs of the filter nets are respectively installed on the inner sides of the two pairs of the filter set rings, two pairs of the Tesla valve inner tubes are respectively inserted on the inner sides of the two pairs of the J-shaped siphon suction flow tubes, a plurality of the trumpet-shaped limit plates are respectively and evenly installed on the two pairs of the J-shaped siphon suction flow tubes, and two pairs of the arc The drainage shaft tube is inserted into the inner side of the filtering reactor in a cross shape, the two pairs of the threaded inner blades are respectively installed on the inner sides of the two pairs of the arc drainage shaft tubes, the two pairs of the inflation valves are respectively connected to the two pairs of the arc drainage shaft tubes, the two pairs of the drainage two-way pumps are respectively connected to the two pairs of the inflation valves, the inner expansion annular airbag is installed on the filtering reactor, the inner expansion drainage two-way pump is connected to the inner expansion annular airbag, and the two pairs of the transit inflation airbags are respectively installed on the two pairs of the drainage two-way pumps.

[0007] Preferably, the quantitative drainage structure comprises: a pair of S-shaped drainage tubes, a pair of J-shaped siphon feeding tubes, a pair of lifting extension blocks, a pair of lifting threaded rods, a pair of lifting threaded tubes, a pair of lifting drive machines, a pair of lifting gear boxes and a plurality of auxiliary lifting limit shaft groups;

[0008] A pair of the drainage S-type drainage tubes are respectively connected to the calcium salt solution tank and the iodate solution tank, a pair of the J-type siphon feeding pipes are respectively inserted into the pair of the drainage S-type drainage tubes, a pair of the lifting threaded tubes are respectively inserted into the calcium salt solution tank and the iodate solution tank through bearings, a pair of the lifting threaded rods are respectively movably inserted into the inner sides of the pair of lifting threaded tubes, a pair of the lifting gear boxes are respectively mounted on the pair of lifting threaded tubes, a pair of the lifting drive motor driving ends are respectively connected to the pair of lifting gear boxes, a pair of the lifting extension blocks are respectively installed on the pair of the lifting threaded rods, a number of the auxiliary lifting limit shaft groups are respectively and evenly installed on the calcium salt solution tank and the iodate solution tank, and a number of the auxiliary lifting limit shaft groups are respectively connected to a pair of the lifting extension blocks.

[0009] Preferably, a pair of the S-shaped drainage tubes are respectively provided with drainage valves.

[0010] Preferably, the filtering reactor is provided with a discharge sealing door.

[0011] Preferably, a temperature sensor is provided inside the filtering reactor.

[0012] Preferably, an electric heating tube and a cooler are provided inside the filtering reactor; Beneficial Effects

[0013] The utility model provides a reaction filtration device for calcium iodate production. It has the following beneficial effects: the reaction filtration device for calcium iodate production, through the rotating airflow push, makes two liquids mixed and stirred, improves the mixing efficiency and uniformity; through the operation of the drainage bidirectional pump, the circulation flow of gas between the filter reactor and the transfer inflatable airbag is realized, the air pressure in the reactor is maintained stable, which is conducive to the reaction; through the expansion of the inner expansion ring airbag, the liquid level inside the filter reactor is accurately controlled, so that the reacted liquid can be smoothly drained into the J-shaped siphon suction tube; the filter net inside the filter set ring on the J-shaped siphon suction tube filters the liquid, ensuring the purity of the reaction product; the cooperation of the Tesla valve inner tube and a number of trumpet-shaped limit pieces effectively avoids the reverse backflow of the J-shaped siphon suction tube, ensuring the stability of the liquid flow; through the cooperation of the lifting drive machine and the lifting extension block, the stable lifting and lowering of the calcium salt solution tank and the iodate solution tank is realized, thereby realizing stable quantitative feeding and ensuring the continuity and stability of the reaction. BRIEF DESCRIPTION OF THE DRAWINGS

[0014] Figure 1 It is a front view and cross-sectional schematic diagram of a reaction filtering device for producing calcium iodate described in the utility model.

[0015] Figure 2 It is a top view and cross-sectional schematic diagram of a reaction filtration device for producing calcium iodate described in the utility model.

[0016] In the figure: 1. Calcium salt solution tank; 2. Iodate solution tank; 3. Filtration reactor; 4. Processing bracket; 5. Partition filter plate; 6. J-type siphon suction pipe; 7. Filter set ring; 8. Filter net; 9. Tesla valve inner tube; 10. Trumpet-shaped limit plate; 11. Arc drainage shaft tube; 12. Inflatable valve; 13. Drainage two-way pump; 14. Transfer inflatable airbag; 15. Internal expansion ring airbag; 16. Internal expansion drainage two-way pump; 17. Drainage S-type drainage pipe; 18. J-type siphon feeding pipe; 19. Lifting extension block; 20. Lifting threaded rod; 21. Lifting threaded pipe; 22. Lifting drive machine; 23. Lifting gear box; 24. Auxiliary lifting limit shaft group. DETAILED DESCRIPTION

[0017] Based on the embodiments of the present utility model, all other embodiments obtained by ordinary technicians in the field without making any creative work shall fall within the scope of protection of the present utility model.

[0018] Through the personnel in this field, all the electrical components in this case are connected to their corresponding power supplies through wires, and appropriate controllers and encoders should be selected according to actual conditions to meet the control requirements. The specific connection and control sequence should refer to the following working principle, and the electrical connection between the electrical components is completed in the order of working in sequence. The detailed connection means are well-known technologies in this field. The following mainly introduces the working principles and processes, and no longer explains the electrical control. Example

[0019] like Figure 1-2 As shown, the calcium salt solution tank 1, the iodate solution tank 2 and the filtering reactor 3 are installed on the processing bracket 4, the calcium salt solution tank 1 and the iodate solution tank 2 are connected to the filtering reactor 3 through a quantitative drainage structure, and a filtering structure is installed on the inner side of the filtering reactor 3;

[0020] Specifically, the filtering structure includes: a partition filter plate 5, two pairs of J-shaped siphon suction pipes 6, two pairs of filter set rings 7, two pairs of filter screens 8, two pairs of Tesla valve inner tubes 9, a plurality of trumpet-shaped limit plates 10, two pairs of arc drainage shaft tubes 11, two pairs of threaded inner blades, two pairs of inflation valves 12, two pairs of drainage bidirectional pumps 13, two pairs of transfer inflation airbags 14, inner expansion ring airbags 15 and inner expansion drainage bidirectional pumps 16;

[0021] Specifically, the partition filter plate 5 is installed on the inner side of the filtering reactor 3, two pairs of the J-shaped siphon suction flow tubes 6 are inserted into the partition filter plate 5 in a cross shape, two pairs of the filter set rings 7 are respectively installed on the two pairs of the J-shaped siphon suction flow tubes 6, two pairs of the filter screens 8 are respectively installed on the inner sides of the two pairs of the filter set rings 7, two pairs of the Tesla valve inner tubes 9 are respectively inserted on the inner sides of the two pairs of the J-shaped siphon suction flow tubes 6, a plurality of the trumpet-shaped limit plates 10 are respectively and evenly installed on the two pairs of the J-shaped siphon suction flow tubes 6, and two pairs of the arc drainage axes are respectively installed on the inner sides of the two pairs of the filter set rings 7. The tube 11 is inserted into the inner side of the filtering reactor 3 in a cross shape, the two pairs of the threaded inner blades are respectively installed on the inner sides of the two pairs of the arc drainage shaft tubes 11, the two pairs of the inflation valves 12 are respectively connected to the two pairs of the arc drainage shaft tubes 11, the two pairs of the drainage two-way pumps 13 are respectively connected to the two pairs of the inflation valves 12, the inner expansion annular airbag 15 is installed on the filtering reactor 3, the inner expansion drainage two-way pump 16 is connected to the inner expansion annular airbag 15, and the two pairs of the transfer inflation airbags 14 are respectively installed on the two pairs of the drainage two-way pumps 13;

[0022] It should be noted that, in the above, the raw materials inside the calcium salt solution tank 1 and the iodate solution tank 2 are drained to the inner side of the filtering reactor 3 through the quantitative drainage structure, and the inner side of the filtering reactor 3 is divided into two ends by the partition filter plate 5. At the same time, the drainage bidirectional pump 13 is operated to drain the gas inside the transit inflation airbag 14 to the inner sides of the two pairs of circular arc drainage shaft tubes 11, and the gas is drained to the inner side of the filtering reactor 3 through the two pairs of circular arc drainage shaft tubes 11. The gas inside the circular arc drainage shaft tubes 11 is limitedly rotated by two pairs of threaded inner blades, so as to achieve the goal of draining the rotating airflow to the inner side of the filtering reactor 3, and the two pairs of cross-shaped spiral rotating airflows are used to push the two liquids inside the filtering reactor 3 with rotating airflow, so that the mixed liquid is mixed and stirred, and then the mixture is passed through the filter. The drainage bidirectional pump 13 is operated through the reaction, so as to drain the gas inside the filtering reactor 3 to the inside of the transit inflation airbag 14, so as to achieve the effect of circulating sealed inflation, and the inner expansion drainage bidirectional pump 16 is operated to drive the inner expansion ring airbag 15 to be inflated, and the liquid level inside the filtering reactor 3 is expanded, squeezed and raised by the expansion of the inner expansion ring airbag 15, so that the reacted liquid is drained to the inside of the two pairs of J-shaped siphon suction tubes 6, and is drained to the bottom end of the partition filter plate 5 through the two pairs of J-shaped siphon suction tubes 6 through the siphon principle, and the liquid is filtered through the filter mesh 8 inside the filter set ring 7 on the two pairs of J-shaped siphon suction tubes 6, and the cooperation of the Tesla valve inner tube 9 and a plurality of trumpet-shaped limit plates 10 avoids the reverse backflow of the J-shaped siphon suction tube 6.

[0023] like Figure 1-2 As shown, the quantitative drainage structure includes: a pair of drainage S-type drainage tubes 17, a pair of J-type siphon feeding tubes 18, a pair of lifting extension blocks 19, a pair of lifting threaded rods, a pair of lifting threaded tubes, a pair of lifting driving machines, a pair of lifting gear boxes and a plurality of auxiliary lifting limit shaft groups;

[0024] Specifically, a pair of the drainage S-type drainage tubes 17 are respectively connected to the calcium salt solution tank 1 and the iodate solution tank 2, a pair of the J-type siphon feeding tubes 18 are respectively inserted into the pair of the drainage S-type drainage tubes 17, a pair of the lifting threaded tubes are respectively inserted into the calcium salt solution tank 1 and the iodate solution tank 2 through bearings, a pair of the lifting threaded rods are respectively movably inserted into the inner sides of the pair of lifting threaded tubes, a pair of the lifting gear boxes are respectively sleeved on the pair of the lifting threaded tubes, a pair of the lifting drive machine driving ends are respectively connected to the pair of the lifting gear boxes, a pair of the lifting extension blocks 19 are respectively installed on the pair of the lifting threaded rods, a number of the auxiliary lifting limit shaft groups are respectively and evenly installed on the calcium salt solution tank 1 and the iodate solution tank 2, and a number of the auxiliary lifting limit shaft groups are respectively connected to a pair of the lifting extension blocks 19;

[0025] It should be noted that, in the above, a pair of lifting drive machines are operated to drive a pair of lifting gear boxes on the driving ends of the lifting drive machines to operate, and the lifting threaded tubes on the inner sides thereof are respectively driven to rotate by the pair of lifting gear boxes, and the lifting threaded tubes on the inner sides thereof are respectively driven by the pair of lifting threaded tubes, so that the pair of lifting threaded rods are respectively lifted and lowered along the pair of lifting threaded tubes, and the lifting extension blocks 19 thereon are respectively driven by the pair of lifting threaded rods, and stably lifted and lowered by the pair of lifting extension blocks 19, and inserted into the inner sides of the calcium salt solution tank 1 and the iodate solution tank 2 by the pair of lifting extension blocks 19, and the liquid levels on the inner sides of the calcium salt solution tank 1 and the iodate solution tank 2 are lifted and lowered, so that the J-type siphon feeding pipe 18 drains the liquid to the inner side of the filtering reactor 3, thereby achieving stable quantitative feeding.

[0026] As a preferred solution, further, a pair of the drainage S-shaped drainage tubes 17 are respectively provided with drainage valves.

[0027] As a preferred solution, further, the filtering reactor 3 is provided with a discharge sealing door.

[0028] As a preferred solution, further, a temperature sensor is provided inside the filtering reactor 3 .

[0029] As a preferred solution, further, an electric heating tube and a cooler are provided inside the filtering reactor 3 .

[0030] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A reaction filtration device for producing calcium iodate, comprising: A calcium salt solution tank, an iodate solution tank, a filtering reactor and a processing support, wherein the calcium salt solution tank, the iodate solution tank and the filtering reactor are installed on the processing support, the calcium salt solution tank and the iodate solution tank are connected to the filtering reactor through a quantitative drainage structure, and a filtering structure is installed on the inner side of the filtering reactor; The filtering structure comprises: a partition filter plate, two pairs of J-shaped siphon suction pipes, two pairs of filter set rings, two pairs of filter screens, two pairs of Tesla valve inner tubes, a plurality of trumpet-shaped limit plates, two pairs of arc drainage shaft tubes, two pairs of threaded inner blades, two pairs of inflation valves, two pairs of drainage bidirectional pumps, two pairs of transfer inflation airbags, inner expansion ring airbags and inner expansion drainage bidirectional pumps; The partition filter plate is installed on the inner side of the filtering reactor, two pairs of the J-shaped siphon suction flow tubes are inserted into the partition filter plate in a cross shape, two pairs of the filter set rings are respectively mounted on the two pairs of the J-shaped siphon suction flow tubes, two pairs of the filter nets are respectively installed on the inner sides of the two pairs of the filter set rings, two pairs of the Tesla valve inner tubes are respectively inserted on the inner sides of the two pairs of the J-shaped siphon suction flow tubes, a plurality of the trumpet-shaped limit plates are respectively and evenly installed on the two pairs of the J-shaped siphon suction flow tubes, and two pairs of the arc The drainage shaft tube is inserted into the inner side of the filtering reactor in a cross shape, the two pairs of the threaded inner blades are respectively installed on the inner sides of the two pairs of the arc drainage shaft tubes, the two pairs of the inflation valves are respectively connected to the two pairs of the arc drainage shaft tubes, the two pairs of the drainage two-way pumps are respectively connected to the two pairs of the inflation valves, the inner expansion annular airbag is installed on the filtering reactor, the inner expansion drainage two-way pump is connected to the inner expansion annular airbag, and the two pairs of the transit inflation airbags are respectively installed on the two pairs of the drainage two-way pumps.

2. A reaction filtration device for calcium iodate production according to claim 1, characterized in that: The quantitative drainage structure comprises: a pair of S-shaped drainage pipes, a pair of J-shaped siphon feeding pipes, a pair of lifting extension blocks, a pair of lifting threaded rods, a pair of lifting threaded pipes, a pair of lifting driving machines, a pair of lifting gear boxes and a plurality of auxiliary lifting limit shaft groups; A pair of the drainage S-type drainage tubes are respectively connected to the calcium salt solution tank and the iodate solution tank, a pair of the J-type siphon feeding pipes are respectively inserted into the pair of the drainage S-type drainage tubes, a pair of the lifting threaded tubes are respectively inserted into the calcium salt solution tank and the iodate solution tank through bearings, a pair of the lifting threaded rods are respectively movably inserted into the inner sides of the pair of lifting threaded tubes, a pair of the lifting gear boxes are respectively mounted on the pair of lifting threaded tubes, a pair of the lifting drive motor driving ends are respectively connected to the pair of lifting gear boxes, a pair of the lifting extension blocks are respectively installed on the pair of the lifting threaded rods, a number of the auxiliary lifting limit shaft groups are respectively and evenly installed on the calcium salt solution tank and the iodate solution tank, and a number of the auxiliary lifting limit shaft groups are respectively connected to a pair of the lifting extension blocks.

3. A reaction filtration device for calcium iodate production according to claim 2, characterized in that: A pair of drainage S-shaped drainage tubes are respectively provided with drainage valves.

4. A reaction filtration device for calcium iodate production according to claim 3, characterized in that: The filtering reactor is provided with a discharge sealing door.

5. A reaction filtration device for calcium iodate production according to claim 4, characterized in that: A temperature sensor is arranged inside the filtering reactor.

6. A reaction filtration device for calcium iodate production according to claim 5, characterized in that: An electric heating tube and a cooler are arranged inside the filtering reactor.