Boiling bed convenient for improving dust removal efficiency

By using an ion generator to eliminate static electricity in the fluidized bed and using a negative pressure fan to create negative pressure, the problem of the purified air swirling at the air outlet is solved, achieving efficient dust separation and removal.

CN223659390UActive Publication Date: 2025-12-12ZHEJIANG WANMA MACROMOLECULE MATERIAL
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Patent Information

Application Number
CN202520108625.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-01-16
Publication Date
2025-12-12
Estimated Expiration
2035-01-16

AI Technical Summary

Technical Problem

The existing fluidized bed has low dust removal efficiency, mainly because particulate solid materials generate electrostatic adsorption of dust during the production process, and the purification air swirls at the air outlet, making it difficult for the dust to be carried out.

Method used

An ion generator is used to produce charged particles to eliminate static electricity, and a negative pressure fan is used to create a negative pressure environment to ensure that the purified air effectively carries away the dust.

Benefits of technology

By combining static electricity elimination with a negative pressure fan, effective separation of particulate solid materials and dust is achieved, thus improving dust removal efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a fluidized bed convenient for improving dust removal efficiency, which belongs to the field of fluidized beds and comprises a bed main body provided with an air inlet, an air outlet, a feed port and a discharge port; the ion generator is arranged at the air inlet and / or the material inlet; the anti-overflow cover is communicated with one side of the air outlet and is positioned in the bed main body; and the negative pressure fan is communicated with the other side of the air outlet. The dust collector has the technical effect that the dust collection efficiency is conveniently improved.
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Description

Technical Field

[0001] This utility model relates to fluidized beds, and more particularly to a fluidized bed that facilitates improved dust removal efficiency. Background Technology

[0002] A fluidized bed is a device based on the fluidization phenomenon, where when a fluid passes through a bed of particulate solid materials, if the fluid velocity is high enough, the particulate solid materials will be suspended. It is generally used for dust removal of particulate solid materials such as cross-linked polyethylene insulation or polyvinyl chloride insulation.

[0003] Because the granular solid materials are prone to generating static electricity during the production process, they can attract dust. In addition, the fluidized bed is generally a positive pressure type, and in order to prevent the granular solid materials from flying out during the fluidization process, the air outlet is usually equipped with an overflow cover. This can cause the purification air to swirl at the top of the fluidized bed, making it difficult for the purification air to carry the dust out of the fluidized bed, resulting in low dust removal efficiency. Utility Model Content

[0004] Purpose of the utility model: The purpose of this utility model is to provide a fluidized bed that facilitates improved dust removal efficiency.

[0005] Technical solution:

[0006] A fluidized bed that facilitates improved dust removal efficiency includes:

[0007] The bed body is provided with an air inlet, an air outlet, a material inlet, and a material outlet;

[0008] An ion generator, wherein the ion generator is located at the air inlet and / or the feed inlet;

[0009] An overflow shield connected to one side of the air outlet, the overflow shield being located inside the bed body;

[0010] A negative pressure fan connected to the other side of the air outlet.

[0011] Optional, also includes:

[0012] A feed pipe passing through the feed inlet, at least a portion of which is located within the bed body;

[0013] A dispersion hood is connected to one end of the feed pipe, and the dispersion hood is located inside the bed body.

[0014] Optionally, the feed tube includes a first tube and a second tube that are bent and connected to each other. The first tube passes through the feed port, and the second tube and at least a portion of the first tube are located inside the bed body. The end of the second tube away from the first tube is connected to the dispersion hood.

[0015] Optionally, the first tube is arranged horizontally, and the second tube is arranged vertically.

[0016] Optional, also includes:

[0017] The discharge pipe passes through the discharge port, and at least a portion of the discharge pipe is located within the bed body;

[0018] A regulating valve connected to the discharge pipe.

[0019] Optionally, it also includes a discharge hopper located within the bed body, the small-diameter end of the discharge hopper being connected to the discharge pipe.

[0020] Optionally, it may also include several level sensors of different heights, the detection ends of which are located inside the bed body.

[0021] Optionally, it may also include several legs connected to the bed body.

[0022] Beneficial effects:

[0023] (1) An ion generator is used to generate charged particles (i.e., ions) to facilitate the elimination of static electricity, thereby facilitating the separation of particulate solid materials and dust.

[0024] (2) The negative pressure fan is used to create negative pressure inside the bed body, that is, the amount of purified air entering the air inlet is less than the amount of purified air leaving the air outlet, to prevent the purified air and dust from swirling at the air outlet of the bed body, so that the purified air can carry the dust out of the bed body, thereby improving the dust removal efficiency. Attached Figure Description

[0025] Figure 1 This is a schematic diagram of the structure of a fluidized bed according to Embodiment 1 of the present invention, which facilitates improved dust removal efficiency;

[0026] In the diagram: 1. Bed body; 11. Air inlet; 12. Air outlet; 13. Feed inlet; 14. Discharge outlet; 2. Ion generator; 3. Overflow cover; 4. Negative pressure fan; 5. Feed pipe; 51. First pipe body; 52. Second pipe body; 6. Dispersion cover; 71. Discharge pipe; 72. Regulating valve; 73. Discharge hopper; 8. Level gauge; 9. Support legs. Detailed Implementation

[0027] To make the technical solution of this utility model clearer, the present utility model will be further described in detail below with reference to the accompanying drawings and specific embodiments.

[0028] The present application will be further described in detail below with reference to the accompanying drawings and embodiments. It is understood that the specific embodiments described herein are merely illustrative of the relevant utility model and not intended to limit the utility model. Furthermore, it should be noted that, for ease of description, only the parts related to the utility model are shown in the accompanying drawings. The terms "first," "second," etc., used in this utility model are provided for the convenience of describing the technical solution of this utility model and have no specific limiting effect; they are all general terms and do not constitute a limitation on the technical solution of this utility model. It should be noted that, in the absence of conflict, the embodiments and features in the embodiments of this application can be combined with each other. In the description of this utility model, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," and "outer," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings, and are only for the convenience of describing the utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation, and therefore should not be construed as a limitation on this utility model. In addition, the terms "first," "second," and "third" are used for descriptive purposes only and should not be construed as indicating or implying relative importance. Unless otherwise explicitly specified and limited, the terms "installation," "connection," and "linking" should be interpreted broadly. For example, they can refer to fixed connections, detachable connections, or integral connections; they can refer to mechanical connections or electrical connections; they can refer to direct connections or indirect connections through an intermediate medium; and they can refer to the internal connection of two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model based on the specific circumstances. Multiple technical solutions in the same embodiment, as well as multiple technical solutions in different embodiments, can be arranged and combined to form new technical solutions that do not contradict or conflict, all of which are within the scope of protection claimed by this utility model.

[0029] Example 1

[0030] like Figure 1 This embodiment provides a fluidized bed that facilitates improved dust removal efficiency, comprising: a bed body 1, which has an air inlet 11, an air outlet 12, a feed inlet 13, and a discharge outlet 14; an ion generator 2, which is located at the air inlet 11 and / or the feed inlet 13; an overflow cover 3 connected to one side of the air outlet 12, which is located inside the bed body 1; and a negative pressure fan 4 connected to the other side of the air outlet 12.

[0031] Specifically, the bed body 1 is used to contain purified air and granular solid materials such as cross-linked polyethylene insulation material or polyvinyl chloride insulation material; the ion generator 2 is used to generate charged particles (i.e., ions) to facilitate the elimination of static electricity, thereby facilitating the separation of granular solid materials and dust. The ion generator 2 can be of the corona discharge type, ultraviolet type, etc.; the negative pressure fan 4 is used to create a negative pressure inside the bed body 1, that is, the amount of purified air entering through the air inlet 11 is less than the amount of purified air exiting through the air outlet 12, preventing the purified air and dust from swirling at the air outlet 12 of the bed body 1, thus facilitating the separation of granular solid materials and dust. The purified air carries the dust out of the bed body 1, thereby improving the dust removal efficiency. The air inlet 11 is preferably located at the bottom side of the bed body 1, so that the particulate solid materials in the bed body 1 can all boil. The number of air inlets 11 is preferably multiple, and the multiple air inlets 11 are preferably evenly distributed along the bottom side of the bed body 1 to ensure good uniformity of the purified air entering. The air outlet 12 is preferably located on the top surface of the bed body 1. The negative pressure fan 4 can be centrifugal, axial flow, etc. The overflow cover 3 is used to prevent the particulate solid materials from flying out during the boiling process.

[0032] Furthermore, such as Figure 1 It also includes: a feed pipe 5 passing through the feed inlet 13, at least part of which is located inside the bed body 1; and a dispersion hood 6 connected to one end of the feed pipe 5, which is located inside the bed body 1.

[0033] Specifically, the feed pipe 5 facilitates the entry of particulate solid materials into the bed body 1; the dispersion hood 6 facilitates the entry of particulate solid materials into the bed body 1 in a dispersed manner, thereby facilitating the boiling of particulate solid materials under the action of purification air. The dispersion hood 6 is conical in shape, and the small diameter end of the dispersion hood 6 is connected to one end of the feed pipe 5.

[0034] Furthermore, such as Figure 1 The feed pipe 5 includes a first pipe body 51 and a second pipe body 52 that are bent and connected to each other. The first pipe body 51 passes through the feed port 13. The second pipe body 52 and at least part of the first pipe body 51 are located inside the bed body 1. The end of the second pipe body 52 away from the first pipe body 51 is connected to the dispersion hood 6.

[0035] Specifically, both the first tube 51 and the second tube 52 facilitate the entry of particulate solid material into the bed body 1. Due to their mutual bending and connection, it is easy to adjust the transmission direction of the particulate solid material.

[0036] Furthermore, such as Figure 1 The first tube 51 is arranged horizontally, and the second tube 52 is arranged vertically. Specifically, the horizontally arranged first tube 51 facilitates the reception of particulate solid material from the dehydrator; the vertically arranged second tube 52 facilitates the entry of particulate solid material into the bed body 1 along the direction of gravity, while the purified air flows in the opposite direction to gravity, thereby facilitating the boiling of the particulate solid material.

[0037] Furthermore, such as Figure 1 It also includes: a discharge pipe 71 passing through the discharge port 14, at least part of which is located inside the bed body 1; and a regulating valve 72 connected to the discharge pipe 71. Specifically, the discharge pipe 71 facilitates the discharge of granular solid material from the bed body 1; the regulating valve 72 is used to regulate the discharge rate of granular solid material, and the regulating valve 72 can be a butterfly valve, ball valve, etc.

[0038] Furthermore, such as Figure 1 It also includes a discharge hopper 73 located inside the bed body 1, with the small-diameter end of the discharge hopper 73 connected to the discharge pipe 71. Specifically, the discharge hopper 73 is conical, which facilitates the guidance of granular solid materials, thereby allowing the granular solid materials to smoothly enter the discharge pipe 71.

[0039] Furthermore, such as Figure 1 It also includes several level sensors 8 at different heights, with the detection end of each level sensor 8 located inside the bed body 1. Specifically, the level sensors 8 are used to detect the height of the granular solid material inside the bed body 1. Preferably, there are two level sensors 8 at different heights. An alarm can be triggered when the height of the granular solid material is too low or too high. The level sensors 8 can be capacitive, ultrasonic, or other types.

[0040] Furthermore, such as Figure 1 It also includes several legs 9 connected to the bed body 1. Specifically, the legs 9 are used to support the bed body 1.

[0041] The above embodiments only illustrate several implementation methods of this utility model, and their descriptions are relatively specific and detailed, but they should not be construed as limiting the scope of this utility model patent. It should be noted that those skilled in the art can make various modifications and improvements without departing from the concept of this utility model, and these all fall within the protection scope of this utility model. Therefore, the protection scope of this utility model patent should be determined by the appended claims.

Claims

1. A fluidized bed that facilitates improved dust removal efficiency, characterized in that, include: The bed body (1) is provided with an air inlet (11), an air outlet (12), a feed inlet (13) and a discharge outlet (14); An ion generator (2) is provided at the air inlet (11) and / or the feed inlet (13); An overflow cover (3) is connected to one side of the air outlet (12), and the overflow cover (3) is located inside the bed body (1); A negative pressure fan (4) connected to the other side of the air outlet (12).

2. The fluidized bed according to claim 1, which facilitates improved dust removal efficiency, is characterized in that... Also includes: The feed pipe (5) passing through the feed inlet (13) is at least partially located inside the bed body (1); A dispersion hood (6) is connected to one end of the feed pipe (5), and the dispersion hood (6) is located inside the bed body (1).

3. A fluidized bed according to claim 2, characterized in that, The feed pipe (5) includes a first pipe body (51) and a second pipe body (52) that are bent and connected to each other. The first pipe body (51) passes through the feed port (13). The second pipe body (52) and at least part of the first pipe body (51) are located inside the bed body (1). The end of the second pipe body (52) away from the first pipe body (51) is connected to the dispersion hood (6).

4. A fluidized bed according to claim 3 that facilitates improved dust removal efficiency, characterized in that, The first tube (51) is arranged in a horizontal direction, and the second tube (52) is arranged in a vertical direction.

5. A fluidized bed according to any one of claims 1-4, characterized in that, Also includes: The discharge pipe (71) passing through the discharge port (14) is at least partially located inside the bed body (1); A regulating valve (72) connected to the discharge pipe (71).

6. A fluidized bed according to claim 5, characterized in that, It also includes a discharge hopper (73) located inside the bed body (1), the small diameter end of the discharge hopper (73) being connected to the discharge pipe (71).

7. A fluidized bed according to any one of claims 1-4, characterized in that, It also includes several level gauges (8) of different heights, the detection end of which is located inside the bed body (1).

8. A fluidized bed according to any one of claims 1-4, characterized in that, It also includes several legs (9) connected to the bed body (1).