Ore pulp stirring barrel

By eccentrically installing the impeller in the slurry mixing tank and setting the guide plate on the inner wall of the tank, the problem of uneven mixing caused by vortex was solved, the mixing efficiency was improved and the energy consumption was reduced, and more efficient slurry mixing was achieved.

CN224167313UActive Publication Date: 2026-04-28SICHUAN ANNING IRON & TITANIUM CO LTD
View PDF 0 Cites 0 Cited by

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
SICHUAN ANNING IRON & TITANIUM CO LTD
Filing Date
2025-02-27
Publication Date
2026-04-28

AI Technical Summary

Technical Problem

Existing slurry mixing tanks are prone to generating vortices during the mixing process, resulting in uneven mixing and insufficient mixing of reagents and slurry, high energy consumption, and low mixing efficiency.

Method used

The device employs an eccentrically positioned impeller and a guide plate installed on the inner wall of the tank. The guide plate has guide holes. The impeller has a double-layer radial structure, with the impeller axis and the tank axis being 10-20cm apart. A feed pipe is installed at the bottom of the tank, and a discharge pipe is installed at the top.

Benefits of technology

It improves the flow pattern of the slurry, reduces vortex generation, increases mixing efficiency, reduces energy loss, ensures thorough mixing and reaction of materials, maintains slurry stability, and reduces production costs.

✦ Generated by Eureka AI based on patent content.

Smart Images

  • Figure CN224167313U_ABST
    Figure CN224167313U_ABST
Patent Text Reader

Abstract

The utility model relates to an ore pulp stirring barrel, and belongs to the field of vanadium titano-magnetite preparation equipment. The device comprises a barrel body (1) and a stirring impeller (2), the stirring impeller (2) is eccentrically arranged in the barrel body (1), and a flow guide plate (3) is arranged on the inner wall of the side, away from the stirring impeller (2), of the barrel body (1). The device is eccentrically provided with the stirring impeller (2), so that the flowing mode of ore pulp can be changed, the generation of vortexes is reduced, the turbulence degree of the ore pulp is increased, the mixing efficiency is improved, and the energy loss is reduced; the flow guide plate (3) can improve the flowing state of ore pulp in the barrel and avoid dead angles, so that materials can be fully mixed and reacted, meanwhile, the flowing of the ore pulp is dispersed, the descending speed of the liquid level is reduced, the stability and consistency of the ore pulp are kept, and the mixing efficiency is improved. The problems of non-uniform stirring, insufficient mixing, high stirring energy consumption and low stirring efficiency of a medicament and ore pulp due to the fact that an existing ore pulp stirring barrel is easy to generate vortex are solved.
Need to check novelty before this filing date? Find Prior Art

Description

Technical Field

[0001] This utility model relates to a slurry mixing tank, belonging to the field of vanadium-titanium magnetite beneficiation equipment. Background Technology

[0002] In the process of mixing slurry in the beneficiation of vanadium-titanium magnetite, the existing slurry mixing tanks have an impeller axis that coincides with the tank body axis, meaning the impeller is located in the middle of the tank. This structure actually creates a vortex above the impeller during the rotation of the impeller, resulting in uneven mixing and insufficient mixing of the reagents and slurry in the tank, high energy consumption, and low mixing efficiency, which increases production costs. Utility Model Content

[0003] The technical problem to be solved by this utility model is that existing slurry mixing tanks are prone to generating vortices, resulting in uneven mixing and insufficient mixing of reagents and slurry, high energy consumption and low mixing efficiency.

[0004] The technical solution adopted by this utility model to solve its technical problem is: a slurry mixing tank, including a tank body and a stirring impeller, wherein the stirring impeller is eccentrically arranged in the tank body, and a guide plate is provided on the inner wall of the tank body away from the stirring impeller.

[0005] In the aforementioned device, the guide plate is provided with guide holes at intervals.

[0006] The device also includes an adjustment plate, one end of which is connected to the inner wall of the guide hole away from the stirring impeller, and the other end is spaced apart from the guide hole.

[0007] In the aforementioned device, at least two guide plates are arranged at intervals along the circumferential direction of the inner wall of the barrel.

[0008] In the aforementioned device, the guide plate is arranged in at least two layers at intervals along the vertical axis of the barrel.

[0009] The stirring impeller in the above-mentioned device is a double-layer radial impeller structure.

[0010] In the above-mentioned device, the distance between the axis of the stirring impeller and the axis of the barrel is 10-20cm.

[0011] The device described above has a feed pipe on the lower side wall of the barrel and a discharge pipe on the upper side wall.

[0012] The beneficial effects of this invention are as follows: This device changes the traditional method of slurry mixing. The eccentrically mounted impeller alters the slurry's flow pattern during mixing, reducing vortex generation and thus increasing turbulence, improving mixing efficiency, and reducing energy loss. The guide plates installed on the cylinder wall improve the slurry's flow state within the cylinder, preventing dead zones and ensuring thorough mixing and reaction of materials. Simultaneously, they disperse the slurry's flow, reduce the rate of liquid level drop, maintain slurry stability and consistency, and improve mixing efficiency. This reduces the impact of vortices on the impeller, increases mixing efficiency, reduces energy loss, and lowers costs. Attached Figure Description

[0013] Figure 1 This is a schematic cross-sectional view of the present invention.

[0014] Figure 2 This is a top view of the structure of this utility model.

[0015] The markings in the diagram are: 1 is the barrel body, 2 is the stirring impeller, 3 is the guide plate, 31 is the guide hole, 4 is the regulating plate, 5 is the feed pipe, and 6 is the discharge pipe. Detailed Implementation

[0016] The present invention will be further described below with reference to the accompanying drawings.

[0017] like Figure 1 and Figure 2 As shown, this utility model discloses a slurry mixing tank, comprising a tank body 1 and a stirring impeller 2. The stirring impeller 2 is eccentrically positioned inside the tank body 1, and a guide plate 3 is provided on the inner wall of the tank body 1 on the side away from the stirring impeller 2. Those skilled in the art will understand that this device modifies the installation position of the stirring impeller 2 within the tank body 1 from the traditional central position to an eccentric installation. Simultaneously, the guide plate 3 on the inner wall of the tank body 1 on the side away from the stirring impeller 2 improves the flow state of the slurry within the tank body 1, avoids the formation of dead zones, and allows the materials to be fully mixed and reacted.

[0018] Preferably, the guide plate 3 in the above-mentioned device is provided with guide holes 31 at intervals. Those skilled in the art will understand that, in order to ensure that the material passes smoothly through the guide plate 3, the device preferably provides guide holes 31 at intervals on the guide plate 3, so that the material can flow along the guide holes 31 and achieve uniform mixing.

[0019] Preferably, the above-mentioned device further includes an adjusting plate 4, one end of which is connected to the inner wall of the guide hole 31 away from the stirring impeller 2, and the other end is spaced apart from the guide hole 31. Those skilled in the art will understand that, in order to facilitate control of the material flow direction and avoid accumulation in dead corners, this device preferably connects one end of the adjusting plate 4 to the inner wall of the guide hole 31 away from the stirring impeller 2, and the other end is spaced apart from the guide hole 31, so that the material changes its original flow direction through the adjusting plate 4 to achieve uniform mixing.

[0020] Preferably, in the above-described device, at least two guide plates 3 are spaced apart along the circumferential direction of the inner wall of the barrel 1. Those skilled in the art will understand that the preferred number and arrangement of the guide plates 3 in this device further ensures uniform mixing; therefore, it is preferred that at least two guide plates 3 are spaced apart along the circumferential direction of the inner wall of the barrel 1. In practice, it is preferable that two guide plates 3 are spaced apart along the circumferential direction of the inner wall of the barrel 1, and the midpoint of the line connecting the two guide plates 3 is perpendicular to and coplanar with the axis of the stirring impeller 2.

[0021] Preferably, in the above-described device, the guide plates 3 are arranged in at least two layers at intervals along the vertical direction of the barrel 1. Those skilled in the art will understand that the preferred quantity and arrangement of the guide plates 3 in this device further ensures uniform mixing, and it is preferable that the guide plates 3 are arranged in at least two layers at intervals along the vertical direction of the barrel 1. In practice, it is even more preferable that the guide plates 3 are arranged in two layers at intervals along the vertical direction of the barrel 1.

[0022] Preferably, the stirring impeller 2 in the above-mentioned device is a double-layer radial impeller structure. Those skilled in the art will understand that, in order to increase the stirring effect and ensure uniform mixing of the reagent and the slurry, this device modifies the stirring impeller 2 from the original single-layer radial flow impeller to a double-layer radial flow impeller.

[0023] Preferably, the distance between the axis of the stirring impeller 2 and the axis of the barrel 1 in the above-mentioned device is 10-20 cm. Those skilled in the art will understand that, in order to ensure the stirring effect, the distance between the axis of the stirring impeller 2 and the axis of the barrel 1 is preferably 10-20 cm.

[0024] Preferably, the lower side wall of the barrel 1 is provided with a feed pipe 5, and the upper side wall is provided with a discharge pipe 6. Those skilled in the art will understand that, for convenient feeding and discharging, this device retains the overflow discharge method of the original mixing tank. Preferably, the feed pipe 5 is provided on the lower side wall of the barrel 1, and the discharge pipe 6 is provided on the upper side wall. This allows the slurry to enter from the feed pipe 5 at the lower end of the barrel 1, and after thorough mixing, overflow and discharge from the discharge pipe 6 at the upper end of the barrel 1.

Claims

1. A slurry mixing tank, comprising a tank body (1) and a mixing impeller (2), characterized in that: The stirring impeller (2) is eccentrically positioned inside the barrel (1), and a guide plate (3) is provided on the inner wall of the barrel (1) away from the stirring impeller (2).

2. The slurry mixing tank according to claim 1, characterized in that: The guide plate (3) is provided with guide holes (31) at intervals.

3. A slurry mixing tank according to claim 2, characterized in that: It also includes an adjustment plate (4), one end of which is connected to the inner wall of the guide hole (31) away from the stirring impeller (2), and the other end is spaced apart from the guide hole (31).

4. A slurry mixing tank according to claim 1, characterized in that: The guide plate (3) is provided at least two pieces at intervals along the inner wall of the barrel (1).

5. A slurry mixing tank according to claim 1, characterized in that: The guide plate (3) is arranged in at least two layers at vertical intervals along the barrel body (1).

6. A slurry mixing tank according to claim 1, characterized in that: The stirring impeller (2) has a double-layer radial impeller structure.

7. A slurry mixing tank according to claim 1, characterized in that: The distance between the axis of the stirring impeller (2) and the axis of the barrel (1) is 10-20cm.

8. A slurry mixing tank according to claim 1, characterized in that: The lower side wall of the barrel (1) is provided with a feed pipe (5), and the upper side wall is provided with a discharge pipe (6).