Impurity removal device for preparing ammonium bifluoride from BOE waste liquid
By designing a decomposition device including a decomposition cylinder, a filter box and a sealed ceiling, using technical means such as stirring, heating and electric cylinder control, the problem of low impurity removal efficiency of existing devices is solved, and solid precipitation and impurities are achieved rapid cleaning and simplification of ammonium hydrogen fluoride preparation process.
Patent Information
- Application Number
- CN202421309480.5
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-06-11
- Publication Date
- 2025-02-25
- Estimated Expiration
- 2034-06-11
AI Technical Summary
The existing BOE waste liquid decompression device for preparing ammonium hydrogen fluoride is difficult to improve the decompression efficiency and cannot quickly clean up solid precipitation and impurities.
A decomposition device including a decompression cylinder, a filter box and a sealed ceiling is designed, and agitated with an electric stirrer. The electric heater increases the reaction rate. The electric cylinder controller moves the filter plate to gather precipitation and impurities and passes the Suction pump and pressure relief valve enable quick cleaning.
The decomposition removal efficiency is improved, so that solid precipitation and impurities can quickly accumulate on the side of the feeding plate and clean it, simplifying the subsequent preparation of ammonium hydrogen fluoride.
Smart Images

Figure CN222524294U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of ammonium bifluoride preparation, in particular to an impurity removal device for preparing ammonium bifluoride from BOE waste liquid. Background Art
[0002] In the process of preparing ammonium bifluoride using BOE waste liquid, impurity removal is an important step. Specifically, this usually involves using barium hydroxide as a precipitant to remove impurities in the waste liquid. After adding barium hydroxide, it needs to be fully stirred for generally 30-60 minutes, and then filtered to obtain a filtrate. The filter residue is mainly barium sulfate precipitate generated by ammonium sulfate and barium hydroxide in BOE waste liquid, and barium hexafluorosilicate precipitate generated by ammonium fluorosilicate and barium hydroxide. After this step of impurity removal treatment, the impurities in the filtrate are effectively removed, laying the foundation for the subsequent preparation of ammonium bifluoride.
[0003] The impurity removal device for preparing ammonium bifluoride from BOE waste liquid in the past has the following disadvantages: 1. It is not convenient to improve the impurity removal efficiency, and solid precipitation and impurities cannot be gathered on one side of the material stripping plate for quick cleaning. Therefore, those skilled in the art provide an impurity removal device for preparing ammonium bifluoride from BOE waste liquid to solve the problems raised in the above background technology. Utility Model Content
[0004] The main purpose of the utility model is to provide an impurity removal device for preparing ammonium bifluoride from BOE waste liquid to solve the problems raised in the above background technology.
[0005] In order to achieve the above purpose, the utility model provides the following technical solutions:
[0006] A device for removing impurities from BOE waste liquid to prepare ammonium bifluoride, comprising a removal cylinder, a filter box and a sealing top cover;
[0007] An electric cylinder is installed at one end of the filter box through a mounting seat, and a linkage piece is installed on the output shaft of the electric cylinder through screws, a filter screen plate is installed on one side of the linkage piece through screws, and the filter screen plate passes through a plug-in interface located on one side of the filter box, the filter screen plate is located in the filter box, and a material-pickup plate is installed on the top side of the filter screen plate through screws, an enlarged top plate is installed on the top of the filter box through bolts, a debris-removing barrel is installed on the top of the enlarged top plate through bolts, a feeding port is provided on the top of the debris-removing barrel, and a sealing top cover is engaged with the top of the feeding port, an electric agitator is installed on the top of the sealing top cover through a mounting seat, and the stirring blades of the electric agitator are located in the debris-removing barrel, and the bottom end of the debris-removing barrel is connected to the filter box through a connecting pipe, and a suction pump is provided on the connecting pipe.
[0008] As a further solution of the utility model: an electric cylinder controller is installed on the upper end of the electric cylinder by screws, the output end of the electric cylinder controller is electrically connected to the input end of the electric cylinder by a wire, and a drain port is provided on one side of the bottom end of the filter box. The electric cylinder controller is used to control the output stroke of the electric cylinder to move the filter screen toward the outside of the filter box.
[0009] As a further solution of the utility model: an impurity taking port is provided on one side of the filter box and located at the upper end of the plug interface, and an impurity taking port is connected to one side of the impurity taking port with an impurity taking cover plate via a hinge.
[0010] As a further solution of the utility model: a pressure relief pipe is arranged on the top of the impurity removal barrel and located on one side of the feeding port, and a pressure relief valve is arranged on the pressure relief pipe.
[0011] As a further solution of the utility model: a pressure gauge is installed on one side of the impurity removal barrel by means of screws, and a detection end of the pressure gauge is located inside the impurity removal barrel.
[0012] As a further solution of the utility model: an electric heater is installed at one end of the impurity removal barrel through a mounting seat and the heating end of the electric heater is located in the impurity removal barrel, and the electric heater is used to heat the reaction solution in the impurity removal barrel to increase the reaction rate.
[0013] Compared with the prior art, the beneficial effects of the utility model are:
[0014] 1. Open the sealed top cover at the top of the feeding port, add BOE waste liquid and barium hydroxide into the impurity removal cylinder, and stir them fully with an electric stirrer. Ammonium sulfate and ammonium fluorosilicate in the BOE waste liquid react with barium hydroxide to form barium sulfate precipitate and barium hexafluorosilicate precipitate. Use an electric heater to heat the reaction solution in the impurity removal cylinder to increase the reaction rate. Use a pressure gauge to detect the pressure value in the impurity removal cylinder. When the pressure is high, open the pressure relief valve to release the pressure.
[0015] 2. Use a suction pump to conveniently suck the solution after the reaction into the filter box and on the top of the filter screen plate. Use the filter screen plate to filter out the fixed precipitate and impurities. The filtered solution is discharged from the drain port to facilitate the subsequent preparation of ammonium bifluoride. Use the electric cylinder controller to control the output stroke of the electric cylinder to move the filter screen plate to the outside of the filter box, so that the solid precipitate and impurities are gathered on one side of the material removal plate. Open the impurity material removal cover plate and quickly clean them out from the impurity material removal port. BRIEF DESCRIPTION OF THE DRAWINGS
[0016] Figure 1 The utility model is a schematic diagram of the overall structure of an impurity removal device for preparing ammonium bifluoride from BOE waste liquid.
[0017] Figure 2The utility model is a side view of an impurity removal device for preparing ammonium bifluoride from BOE waste liquid.
[0018] Figure 3 The utility model is a schematic diagram of the structure of a material-diverting plate of an impurity-removing device for preparing ammonium bifluoride from BOE waste liquid.
[0019] In the figure: 1. Electric cylinder; 2. Electric cylinder controller; 3. Pressure relief pipe; 4. Pressure relief valve; 5. Electric agitator; 6. Sealed top cover; 7. Feeding port; 8. De-impurity barrel; 9. Electric heater; 10. Pressure gauge; 11. Suction pump; 12. Connecting pipe; 13. Expanded top plate; 14. Filter box; 15. Plug interface; 16. Filter screen plate; 17. Linkage plate; 18. Material removal plate; 19. Drain port; 20. Impurity removal cover plate. DETAILED DESCRIPTION
[0020] The following will be combined with the drawings in 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 in 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.
[0021] See also Figure 1-3 In the embodiment of the utility model, a device for removing impurities from BOE waste liquid to prepare ammonium bifluoride comprises an impurity removal cylinder 8, a filter box 14 and a sealing top cover 6;
[0022] An electric cylinder 1 is installed at one end of the filter box 14 through a mounting seat, and a linkage piece 17 is installed on the output shaft of the electric cylinder 1 through screws, a filter screen plate 16 is installed on one side of the linkage piece 17 through screws, and the filter screen plate 16 passes through a plug interface 15 located on one side of the filter box 14, the filter screen plate 16 is located in the filter box 14, and a material-pickup plate 18 is installed on one side of the top of the filter screen plate 16 through screws, an enlarged top plate 13 is installed on the top of the filter box 14 through bolts, a de-impurity barrel 8 is installed on the top of the enlarged top plate 13 through bolts, a feeding port 7 is provided on the top of the de-impurity barrel 8, and a sealing top cover 6 is engaged with the top of the feeding port 7, an electric stirrer 5 is installed on the top of the sealing top cover 6 through a mounting seat, and the stirring blades of the electric stirrer 5 are located in the de-impurity barrel 8, and the bottom end of the de-impurity barrel 8 is connected to the filter box 14 through a connecting pipe 12, and a suction pump 11 is provided on the connecting pipe 12.
[0023] Among them, an electric cylinder controller 2 is installed on the upper end of the electric cylinder 1 by screws, the output end of the electric cylinder controller 2 is electrically connected to the input end of the electric cylinder 1 through a wire, and a drain port 19 is provided on one side of the bottom end of the filter box 14; the electric cylinder controller 2 is used to control the output stroke of the electric cylinder 1 to move the filter screen plate 16 to the outside of the filter box 14.
[0024] Among them, an impurity taking port is opened on one side of the filter box 14 and located at the upper end of the plug-in port 15, and an impurity taking cover plate 20 is connected to one side of the impurity taking port through a hinge; the impurity taking cover plate 20 is opened to quickly clean and take out the impurities from the impurity taking port.
[0025] A pressure relief pipe 3 is provided at the top of the impurity removal barrel 8 and at one side of the feeding port 7, and a pressure relief valve 4 is provided on the pressure relief pipe 3; when the pressure is relatively high, the pressure relief valve 4 is opened to relieve the pressure.
[0026] Among them, a pressure gauge 10 is installed on one side of the impurity removal barrel 8 by means of screws, and the detection end of the pressure gauge 10 is located inside the impurity removal barrel 8; the pressure gauge 10 is used to facilitate the detection of the pressure value inside the impurity removal barrel 8.
[0027] Among them, an electric heater 9 is installed at one end of the impurity removal barrel 8 through a mounting seat, and the heating end of the electric heater 9 is located in the impurity removal barrel 8; the electric heater 9 is used to heat the reaction solution in the impurity removal barrel 8 to increase the reaction rate.
[0028] The working principle of the utility model is as follows: the sealing top cover 6 on the top of the feeding port 7 is opened, and the BOE waste liquid and barium hydroxide are added into the impurity removal cylinder 8 together, and the electric stirrer 5 is used to fully stir, and the ammonium sulfate and ammonium fluorosilicate in the BOE waste liquid and the barium hydroxide generate barium sulfate precipitation and barium hexafluorosilicate precipitation, and the electric heater 9 is used to heat the reaction solution in the impurity removal cylinder 8 to increase the reaction rate, and the pressure gauge 10 is used to detect the pressure value in the impurity removal cylinder 8. When the pressure is relatively high, the pressure relief valve 4 is opened to relieve the pressure, and the suction pump 11 is used to suck the reacted solution into the filter box 1 4 and is located on the top of the filter screen plate 16, the filter screen plate 16 is used to filter the fixed precipitation and impurities, and the filtered solution is discharged from the drain port 19 to facilitate the subsequent preparation of ammonium bifluoride, and the electric cylinder controller 2 is used to control the output stroke of the electric cylinder 1 to move the filter screen plate 16 to the outside of the filter box 14, so that the solid precipitation and impurities are gathered on the side of the material-diverting plate 18, and the impurity material-taking cover plate 20 is opened to quickly clean and take them out from the impurity material-diverting port. The impurity removal device for preparing ammonium bifluoride from BOE waste liquid is convenient for improving the impurity removal efficiency, and can make the solid precipitation and impurities gather on the side of the material-diverting plate 18 and be quickly cleaned.
[0029] The above description is only a preferred specific implementation manner of the present invention, but the protection scope of the present invention is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes within the technical scope disclosed by the present invention according to the technical scheme and the utility model concept of the present invention, which should be covered by the protection scope of the present invention.
Claims
1. A device for removing impurities from BOE waste liquid to prepare ammonium bifluoride, comprising an impurity removal cylinder (8), a filter box (14) and a sealing top cover (6); It is characterized by: The filter box (14) has an electric cylinder (1) mounted on one end thereof via a mounting seat, and the output shaft of the electric cylinder (1) is mounted with a linkage piece (17) via screws; a filter screen plate (16) is mounted on one side of the linkage piece (17) via screws, and the filter screen plate (16) passes through a plug-in interface (15) located on one side of the filter box (14); the filter screen plate (16) is located in the filter box (14) and a material-dispensing plate (18) is mounted on one side of the top of the filter screen plate (16) via screws; and the top of the filter box (14) is mounted with a An enlarged top plate (13) is provided, a de-impurity barrel (8) is installed on the top of the enlarged top plate (13) by means of bolts, a feeding port (7) is provided on the top of the de-impurity barrel (8), a sealing top cover (6) is engaged with the top of the feeding port (7), an electric stirrer (5) is installed on the top of the sealing top cover (6) by means of a mounting seat, and the stirring blades of the electric stirrer (5) are located in the de-impurity barrel (8), the bottom end of the de-impurity barrel (8) is connected to a filter box (14) by means of a connecting pipe (12), and a suction pump (11) is provided on the connecting pipe (12).
2. The impurity removal device for preparing ammonium bifluoride from BOE waste liquid according to claim 1, characterized in that: An electric cylinder controller (2) is mounted on the upper end of the electric cylinder (1) by means of screws, an output end of the electric cylinder controller (2) is electrically connected to an input end of the electric cylinder (1) by means of a wire, and a drain port (19) is provided on one side of the bottom end of the filter box (14).
3. The impurity removal device for preparing ammonium bifluoride from BOE waste liquid according to claim 1, characterized in that: An impurity taking port is provided on one side of the filter box (14) and located at the upper end of the plug-in port (15), and an impurity taking cover plate (20) is connected to one side of the impurity taking port via a hinge.
4. The impurity removal device for preparing ammonium bifluoride from BOE waste liquid according to claim 1, characterized in that: A pressure relief pipe (3) is provided at the top of the impurity removal cylinder (8) and located on one side of the feeding port (7), and a pressure relief valve (4) is provided on the pressure relief pipe (3).
5. The impurity removal device for preparing ammonium bifluoride from BOE waste liquid according to claim 1, characterized in that: A pressure gauge (10) is installed on one side of the impurity removal barrel (8) by means of screws, and a detection end of the pressure gauge (10) is located inside the impurity removal barrel (8).
6. The impurity removal device for preparing ammonium bifluoride from BOE waste liquid according to claim 1, characterized in that: An electric heater (9) is mounted on one end of the impurity removal barrel (8) via a mounting seat, and a heating end of the electric heater (9) is located inside the impurity removal barrel (8).