Carbon iron zinc separation device for blast furnace dust

Abstract

The utility model belongs to the dust ash carbon iron zinc separation production field relates to a blast furnace dust ash carbon iron zinc separation device, including the frame, the inner side wall fixed mounting of frame has two line pipes, the common activity installation of two line pipes between has the collecting cylinder, the inside between two line pipes of collecting cylinder is connected with a plurality of electromagnetic board, the one side lower portion of collecting cylinder is provided with the iron export and is inserted. According to the different density of carbon iron zinc in dust ash, carbon particle floats to fluidized bed fluidization box bed surface, iron particle sinks to the bottom of collecting cylinder, zinc is distributed in the middle of fluidized bed fluidization box and collecting cylinder, carbon particle is adsorbed to the positive plate by electric field, and the collection material is discharged to carbon export, and the sinking iron particle is adsorbed through the collecting cylinder, and the mixed particle material of carbon and iron is effectively separated, avoids the high iron content after mixed flotation, improves the separation effect of carbon and iron superfine particle material, and further improves the overall processing efficiency and quality.

Description

Technical Field

[0001] This utility model belongs to the field of blast furnace dust separation of carbon, iron and zinc production, and relates to a blast furnace dust separation device. Background Technology

[0002] The blast furnace dust separation equipment is a multi-stage sorting system specifically designed for the resource utilization of blast furnace gas dust in the metallurgical industry. It contains valuable metal resources such as carbon, iron, and zinc.

[0003] When existing blast furnace dust separation devices are in use, the ultrafine carbon and iron particles are mixed together and difficult to separate completely. After flotation, the carbon concentrate still contains 5-8% iron. In magnetic separation and flotation operations, the separation efficiency for particles smaller than 5μm drops sharply to less than half, affecting the overall separation efficiency and quality. Utility Model Content

[0004] In order to overcome the shortcomings of the prior art, this utility model provides a blast furnace dust removal ash carbon iron zinc separation device.

[0005] The technical solution adopted by this utility model is: a blast furnace dust removal ash carbon-iron-zinc separation device, including a frame, two conduits fixedly installed on the inner side wall of the frame, a collecting cylinder movably installed between the two conduits, multiple electromagnetic plates connected between the two conduits inside the collecting cylinder, an iron outlet inserted through the lower part of one side of the collecting cylinder, a zinc outlet inserted through the middle of the collecting cylinder, a fluidizing box fixedly connected to the upper end of the collecting cylinder, a scraper movably installed inside the fluidizing box, the scraper slidingly installed against the upper wall of the fluidizing box, a positive electrode plate installed on the inner wall of the fluidizing box, and a carbon outlet inserted through one side of the fluidizing box.

[0006] The inner wall of the collecting cylinder of this utility model is provided with several coils.

[0007] The frame of this utility model is fixedly connected to a through plate, and a traction slider is slidably installed on the inner side of the through plate. A magnetic chuck is fixedly connected to the bottom end of the traction slider.

[0008] The fluidization tank of this invention has two sliding grooves on its upper wall, the scraper is slidably disposed in the sliding grooves, and the magnetic chuck is used in conjunction with the scraper.

[0009] A servo motor is installed on the inner side of the frame of this utility model. A threaded rod is installed laterally on the inner side of the frame. The threaded rod is connected to the output shaft of the servo motor. A threaded sleeve is threaded onto the outer surface of the threaded rod. The threaded sleeve is fixedly connected to the traction slider.

[0010] A telescopic bolt is inserted into one side of the magnetic chuck of this utility model. The telescopic bolt abuts against the through plate, and a spring is sleeved on the outer surface of the telescopic bolt.

[0011] An access plate is installed on one side of the collection tube described in this utility model.

[0012] Compared with the prior art, the beneficial effects of this utility model are as follows: After the ash enters and mixes with the fluidizing gas, according to the different densities of carbon, iron and zinc in the dust, carbon particles float to the surface of the fluidized bed, iron particles sink to the bottom of the collecting cylinder, zinc is distributed in the middle between the fluidized bed and the collecting cylinder, carbon particles are adsorbed onto the positive electrode plate by the electric field, and after the magnetic chuck moves, it drives the scraper to scrape the carbon material on the positive electrode plate, and the collected material is discharged to the carbon outlet. The sinking iron particles are adsorbed by the collecting cylinder and discharged from the side iron outlet. Then the zinc gas is discharged from the zinc outlet. This can effectively separate the mixed particles of carbon and iron, avoid the high iron content after mixed flotation, and improve the separation quality of ultrafine carbon and iron particles. Attached Figure Description

[0013] Figure 1 This is a schematic diagram of the overall structure of an embodiment of the present utility model; Figure 2 This is an embodiment of the present utility model. Figure 1 Mid-section structural schematic diagram; Figure 3 This is a cross-sectional structural schematic diagram of the fluidization tank and collection cylinder according to an embodiment of the present invention; Figure 4 This is an embodiment of the present utility model. Figure 2 Schematic diagram of the structure from the middle side view.

[0014] In the diagram: 1. Frame; 2. Servo motor; 3. Threaded rod; 4. Through plate; 5. Threaded sleeve; 6. Fluidizing tank; 7. Carbon outlet; 8. Expansion bolt; 9. Slide rail; 10. Spring; 11. Traction slider; 12. Magnetic chuck; 13. Conduit; 14. Inlet tray; 15. Collection cylinder; 16. Carbon outlet; 17. Coil; 18. Electromagnetic plate; 19. Iron outlet; 20. Zinc outlet; 22. Scraper; 23. Positive electrode plate. Detailed Implementation

[0015] To better understand the technical solution of this utility model, the following description, in conjunction with the accompanying drawings, further illustrates this utility model.

[0016] like Figures 1 to 4As shown, a blast furnace dust removal ash carbon-iron-zinc separation device includes a frame 1. Two conduits 13 are fixedly installed on the inner wall of the frame 1. A collection cylinder 15 is movably installed between the two conduits 13. Multiple electromagnetic plates 18 are connected between the two conduits 13 inside the collection cylinder 15. An iron outlet 19 is inserted through the lower part of one side of the collection cylinder 15, and a zinc outlet 20 is inserted through the middle of the collection cylinder 15. A fluidizing box 6 is fixedly connected to the upper end of the collection cylinder 15. A scraper 22 is movably installed inside the fluidizing box 6 and slides against the upper wall of the fluidizing box 6. A positive electrode plate 23 is provided on the inner wall of the fluidizing box 6. Several coils 17 are provided on the inner wall of the collection cylinder 15. An inlet plate 14 is installed on one side of the collection cylinder 15, and a carbon outlet 16 is inserted through the one side of the fluidizing box 6.

[0017] In Example 1, the dust to be treated is fed into the collection cylinder 15 through the feed port at the top of one side of the fluidized bed fluidizing box 6. The external pipe is connected to the inlet plate 14 to send in fluidizing gas. After the dust enters, it mixes with the fluidizing gas. According to the different densities of carbon, iron and zinc in the dust, carbon particles float to the surface of the fluidized bed 6, iron particles sink to the bottom of the collection cylinder 15, and zinc is distributed in the middle between the fluidized bed 6 and the collection cylinder 15. The carbon particles are adsorbed onto the positive electrode plate 23 by the electric field. The collected material is discharged to the carbon outlet 16. The sinking iron particles are adsorbed by the collection cylinder 15 and discharged from the side iron outlet 19. Then the zinc gas is discharged from the zinc outlet 20. This effectively separates the mixed particles of carbon and iron, avoids high iron content after mixed flotation, and improves the separation effect of ultrafine carbon and iron particles.

[0018] like Figure 1 - Figure 3 As shown, a through plate 4 is fixedly connected to the inner side of the frame 1, and a traction slider 11 is slidably installed on the inner side of the through plate 4. A magnetic chuck 12 is fixedly connected to the bottom end of the traction slider 11.

[0019] In Example 2, the traction slider 11 slides in the through plate 4, thereby driving the magnetic chuck 12 to move and then driving the scraper 22 to scrape the carbon material on the positive electrode plate 23.

[0020] like Figure 1 - Figure 3 As shown, two grooves 9 are opened on the upper wall of the chute 9. The scraper 22 is slidably set with the chute 9. The magnetic chuck 12 is used in conjunction with the scraper 22. The servo motor 2 is installed on the inner side of the frame 1. The threaded rod 3 is installed horizontally on the inner side of the frame 1. The threaded rod 3 is connected to the output shaft of the servo motor 2. The threaded sleeve 5 is threaded on the outer surface of the threaded rod 3. The threaded sleeve 5 is fixedly connected to the traction slider 11. The telescopic bolt 8 is inserted on one side of the magnetic chuck 12. The telescopic bolt 8 abuts against the through plate 4. The outer surface of the telescopic bolt 8 is fitted with a spring 10.

[0021] In Example 3, after the servo motor 2 is turned, the output end drives the threaded rod 3 to rotate, so that the threaded sleeve block 5 moves horizontally along the thread groove. When the magnetic chuck 12 moves, it drives the telescopic bolt 8 to abut against the through plate 4 and compress the spring 10, resulting in good circulation.

[0022] Working principle: Dust particles are fed into the collection cylinder 15 through the feed inlet at the top of one side of the fluidized bed fluidizing box 6. An external pipe connects to the inlet plate 14 to supply fluidizing gas. The dust particles mix with the gas. Based on the different densities of carbon, iron, and zinc in the dust particles, carbon particles rise to the surface of the fluidized bed 6, iron particles sink to the bottom of the collection cylinder 15, and zinc particles are distributed between the fluidized bed 6 and the collection cylinder 15. Carbon particles are adsorbed onto the positive electrode plate 23 by the electric field. The servo motor 2 is activated by an external controller. 2. After operation, the output end drives the threaded rod 3 to rotate, causing the threaded sleeve block 5 to move horizontally along the thread groove, thereby driving the traction slider 11 to slide in the through plate 4, which in turn drives the magnetic chuck 12 to move and drive the scraper 22 to scrape the carbon material on the positive electrode plate 23. When the magnetic chuck 12 moves, it drives the telescopic bolt 8 to contact the through plate 4 and compress the spring 10 to prevent foreign objects from getting stuck. The collected material is discharged to the carbon outlet 16. The sinking iron particles are adsorbed by the collection cylinder 15 and discharged from the side iron outlet 19. Then the zinc gas is discharged from the zinc outlet 20 and enters the subsequent acid leaching process.

[0023] Working principle: When in use, first rotate the crank handle 674 to move the mounting plate 63 along with the moving top block 62 to compress the spring 65. When there is enough space between the moving top block 62 and the fixed top block 61 to place the filtration bottle 2, stop rotating and place the filtration bottle 2 on the filtration bottle placement platform 31 between the fixed top block 61 and the moving top block 62. Then, rotate the crank handle 674 and the sliding block 673 to move towards the support plate 671. Under the elastic force of the spring 65, the mounting plate 63 also moves towards the fixed top block 61 until the moving top block 62 and the fixed top block 61 clamp the filtration bottle 2. Stop rotating the crank handle 674. Then, the operator holds the connector 7, with the branch pipe 5 and the connector 7 in a normally connected state. Insert the rubber plug 72 of the connector 7 into the connecting pipe of the filtration bottle 2. According to the number of filtration bottles 2 used, open the manual valve 51 on the corresponding branch pipe 5. Finally, start the vacuum pump to perform the filtration action.

[0024] The above description is only a preferred embodiment of the present utility model. Therefore, all equivalent changes or modifications made to the structure, features and principles described in the claims of the present utility model patent application are included in the scope of the present utility model patent application.

Claims

1. A blast furnace dust removal ash carbon-iron-zinc separation device, characterized in that: The device includes a frame (1), on which two conduits (13) are fixedly installed on the inner wall. A collection cylinder (15) is movably installed between the two conduits (13). Multiple electromagnetic plates (18) are connected between the two conduits (13) inside the collection cylinder (15). An iron outlet (19) is inserted through the lower part of one side of the collection cylinder (15). A zinc outlet (20) is inserted through the middle of the collection cylinder (15). A fluidizing tank (6) is fixedly connected to the upper end of the collection cylinder (15). A scraper (22) is movably installed inside the fluidizing tank (6). The scraper (22) slides against the upper wall of the fluidizing tank (6). A positive electrode plate (23) is installed on the inner wall of the fluidizing tank (6). A carbon outlet (16) is inserted through one side of the fluidizing tank (6).

2. The blast furnace dust removal ash carbon-iron-zinc separation device according to claim 1, characterized in that: The inner wall of the collecting cylinder (15) is provided with several coils (17).

3. The blast furnace dust separation device for carbon, iron, and zinc as described in claim 1, characterized in that: A through plate (4) is fixedly connected to the inner side of the frame (1), and a traction slider (11) is slidably installed on the inner side of the through plate (4). A magnetic chuck (12) is fixedly connected to the bottom end of the traction slider (11).

4. The blast furnace dust removal ash carbon-iron-zinc separation device according to claim 3, characterized in that: The upper wall of the fluidizing tank (6) has two grooves (9), the scraper (22) is slidably disposed with the grooves (9), and the magnetic chuck (12) is used in conjunction with the scraper (22).

5. The blast furnace dust separation device for carbon, iron, and zinc as described in claim 3, characterized in that: A servo motor (2) is installed on the inner side of the frame (1), and a threaded rod (3) is installed horizontally on the inner side of the frame (1). The threaded rod (3) is connected to the output shaft of the servo motor (2). A threaded sleeve (5) is threaded on the outer surface of the threaded rod (3), and the threaded sleeve (5) is fixedly connected to the traction slider (11).

6. The blast furnace dust separation device for carbon, iron, and zinc as described in claim 3, characterized in that: A telescopic bolt (8) is inserted into one side of the magnetic chuck (12). The telescopic bolt (8) abuts against the through plate (4). A spring (10) is sleeved on the outer surface of the telescopic bolt (8).

7. The blast furnace dust separation device for carbon, iron, and zinc as described in claim 1, characterized in that: An access plate (14) is installed on one side of the collection tube (15).

Images