Dry quenching fly ash transfer system

By setting up a crusher in the dry coke quenching dust removal ash transport system, large particles of dust are crushed into small particles, the problems of damaged ash transport pipe wall and equipment blockage are solved, and the service life and transportation efficiency of the equipment are improved.

CN222664887UActive Publication Date: 2025-03-25ANYANG IRON & STEEL +1
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Patent Information

Application Number
CN202420547650.7
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-03-21
Publication Date
2025-03-25
Estimated Expiration
2034-03-21

AI Technical Summary

Technical Problem

In the existing dry quenching dust removal ash transportation system, large particles of dust cause damage to the ash pipe wall, polluting the environment, equipment failure and service life are reduced.

Method used

A dry coke quenching dust removal ash transport system is designed. By setting up a crusher in the transport system, large particles of dust are crushed into small particles to avoid damage to the ash transport pipe wall and equipment blockage.

Benefits of technology

It effectively avoids damage to the ash pipe wall and equipment blockage, reduces pollution and maintenance costs, and improves the service life of the equipment.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of fly ash treatment, in particular to a dry quenching fly ash transfer system, which comprises a middle bin, a scraper conveyor, a bucket elevator, a crusher and an ash bin, the middle bin is connected with the bucket elevator through a first blanking chute, the bucket elevator is connected with the ash bin through a second blanking chute, and the crusher is connected with the ash bin through a second blanking chute. The crusher is arranged on the second discharging chute and used for crushing dust in the second discharging chute and then conveying the crushed dust into the ash bin for transferring. The coke powder recycling device is simple in structure and reasonable in design, and by arranging the crusher, coke powder is crushed into small particles and then transferred, so that the coke powder recycling efficiency is improved, and the coke powder recycling efficiency is improved. Environment pollution caused by damage of the wall of the ash conveying pipe and equipment shutdown caused by blockage of equipment by large-particle coke powder are avoided, and the service life of the equipment is prolonged.
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Description

Technical Field

[0001] The utility model relates to the technical field of dust removal ash treatment, in particular to a dry quenching dust removal ash transfer system. Background Art

[0002] At present, the primary dust removal ash of 140T CDQ is transported by negative pressure tanker to achieve fully closed transportation. Since the particles of primary dust removal ash of CDQ are relatively large, with a particle size of usually 8 to 10 cm, the tanker will wear the ash extraction pipe wall when extracting ash, thus causing the pipe wall to be damaged and causing the dust removal ash to leak out and pollute the environment, and also reduce the service life of the equipment and increase the maintenance cost. At the same time, large particles will also cause the ash conveying pipeline to be blocked, leading to equipment failure.

[0003] In view of this, the present application aims to provide a CDQ dust transfer system to better solve the above-mentioned technician problems. Utility Model Content

[0004] In order to solve the above problems, the utility model provides a dry quenching dust transfer system, which provides a crusher to avoid damage to the ash pipe wall and pollution of the environment, and large particles of coke powder blocking the equipment and causing equipment shutdown, thereby increasing the service life of the equipment.

[0005] The technical solution adopted by the utility model is:

[0006] A dry quenching dust ash transfer system comprises an intermediate bin, a scraper conveyor, a bucket elevator, a crusher and an ash bin, wherein the intermediate bin is connected to the bucket elevator via a first discharge chute, the bucket elevator is connected to the ash bin via a second discharge chute, and the crusher is arranged at the second discharge chute to crush the dust in the second discharge chute and then send it into the ash bin for transfer.

[0007] Furthermore, an electric ash discharge valve is provided at the bottom end of the intermediate bin.

[0008] Furthermore, the second discharge chute is provided with an anti-blocking material level meter near the top of the pulverizer, and the anti-blocking material level meter is interlocked with the electric format ash discharge valve, the scraper conveyor, the bucket elevator and the pulverizer.

[0009] Furthermore, the first material discharge chute is set at an inclined angle, and the inclined angle is set to 40-60°; the second material discharge chute is set at an inclined angle, and the inclined angle is set to 30-45°.

[0010] Furthermore, the crusher is provided with a crushing box, a crushing roller group, a driving structure and a screen structure; the crushing box is installed on the second discharge chute; the crushing roller group is rotatably installed on the crushing box, and the crushing roller group is provided with a crushing tooth structure for crushing dust particles; the driving structure is arranged on one side of the crushing box and is drivingly connected to the crushing roller group; the screen structure is arranged at the bottom end of the crushing box for screening the discharge material.

[0011] Furthermore, a pressure-resistant layer is connected to the surface of the crushing roller set, and a plurality of pressure-resistant blocks for mounting the crushing tooth structure are arranged on the pressure-resistant layer.

[0012] Furthermore, a feed opening is provided at the top of the pulverizing box, and the feed opening is designed to be open.

[0013] The beneficial effects of the utility model are as follows:

[0014] The utility model provides a dry quenching coke dust removal ash transfer system, comprising an intermediate bin, a scraper conveyor, a bucket elevator, a crusher and an ash bin, wherein the intermediate bin is connected to the bucket elevator via a first discharge chute, the bucket elevator is connected to the ash bin via a second discharge chute, the crusher is arranged at the second discharge chute, and is used to crush the dust in the second discharge chute and then send it into the ash bin for transfer. The utility model has a simple structure and a reasonable design. By arranging a crusher, the coke powder is crushed into small particles and then transferred, thereby avoiding the damage of the ash conveying pipe wall to pollute the environment and the large particles of coke powder clogging the equipment to cause equipment shutdown, thereby improving the service life of the equipment. BRIEF DESCRIPTION OF THE DRAWINGS

[0015] Figure 1 This is a schematic diagram of the structure of some embodiments of the present application;

[0016] Figure 2 This is a schematic diagram of the structure of a pulverizer in some embodiments of the present application;

[0017] Figure 3 This is a schematic cross-sectional view of a crushing roller on one side of a crushing roller assembly in some embodiments of the present application.

[0018] Description of reference numerals:

[0019] Intermediate bin 1, electric format ash discharge valve 11, scraper conveyor 2, bucket elevator 3, crusher 4, crushing box 41, feed inlet 411, crushing roller set 42, pressure-resistant layer 421, pressure-resistant block 422, drive structure 43, screen structure 44, ash bin 5, first discharge chute 6, second discharge chute 7, anti-blocking material level meter 71. DETAILED DESCRIPTION

[0020] The technical solution of the utility model will be described clearly and completely below in conjunction with the accompanying drawings. Obviously, the described embodiments are part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments of 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] In the description of the present invention, it should be noted that the terms "up", "down", "left", "right", "vertical", "horizontal", "inside", "outside", "front", "back", etc. indicate directions or positional relationships based on the directions or positional relationships shown in the accompanying drawings. They are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific direction, be constructed and operated in a specific direction. Therefore, they cannot be understood as limitations on the present invention.

[0022] In the description of the present invention, it should be noted that, unless otherwise clearly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection, a direct connection, or an indirect connection through an intermediate medium. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0023] like Figure 1 to Figure 3 As shown, the dry quenching dust ash transfer system described in this embodiment includes an intermediate bin 1, a scraper conveyor 2, a bucket elevator 3, a crusher 4 and an ash bin 5. The intermediate bin 1 is connected to the bucket elevator 3 through a first discharge chute 6, and the bucket elevator 3 is connected to the ash bin 5 through a second discharge chute 7. The crusher 4 is arranged in the second discharge chute 7, and is used for crushing the dust in the second discharge chute 7 and then sending it into the ash bin 5 for transfer.

[0024] This embodiment has a simple structure and a reasonable design. By setting a crusher 4, the coke powder is crushed into small particles before being transported, thereby avoiding damage to the ash conveying pipe wall to pollute the environment and large particles of coke powder clogging the equipment to cause equipment shutdown, thereby increasing the service life of the equipment.

[0025] On the basis of the above embodiment, an electric ash discharge valve 11 is provided at the bottom end of the intermediate bin 1 .

[0026] Specifically, the second discharge chute 7 is provided with an anti-blocking material level meter 71 near the top of the crusher 4 , and the anti-blocking material level meter 71 is interlocked with the electric format ash discharge valve 11 , the scraper conveyor 2 , the bucket elevator 3 and the crusher 4 .

[0027] In the present embodiment, an electric ash discharge valve 11 is provided to facilitate flexible control of the coke powder discharge speed in the intermediate bin 1. By providing an anti-blocking material level meter 71, it is possible to monitor in real time whether the coke powder conveying speed exceeds the working capacity of the crusher 4. If material accumulation occurs, the coke powder conveying in the front section is stopped based on interlocking control. After cleaning and unblocking, each component is opened for transportation.

[0028] Specifically, in this embodiment, a crusher 4 is provided to crush 8 to 10 cm of coke powder into a safe ash conveying range of about 1 mm. When the equipment is running, the crusher 4 is started first, and after normal operation, a command is issued to start the electric format ash discharge valve 11, the scraper conveyor 2 and the bucket elevator 3. When the anti-blocking material level meter 71 detects the occurrence of a blockage, the crusher 4 and the electric format ash discharge valve 11, the scraper conveyor 2 and the bucket elevator 3 and other components are immediately stopped. When the system stops, the system is shut down in sequence from front to back. The crusher 4 continues to run for 2-5 minutes after the front-end ash discharge and transfer system stops, and then stops.

[0029] In some embodiments, the first material discharge chute 6 is set at an inclined angle, and the inclined angle is set to 40-60°; the second material discharge chute 7 is set at an inclined angle, and the inclined angle is set to 30-45°.

[0030] The present embodiment specifically shows the inclination angle settings of the first material discharge chute 6 and the second material discharge chute 7 so as to achieve a better material discharge effect. The structure is simple and the material discharge is smooth.

[0031] In some embodiments, the crusher 4 is provided with a crushing box 41, a crushing roller group 42, a driving structure 43 and a screen structure 44; the crushing box 41 is installed on the second discharge chute 7; the crushing roller group 42 is rotatably installed on the crushing box 41; and the crushing roller group 42 is provided with a crushing tooth structure for crushing dust particles; the driving structure 43 is arranged on one side of the crushing box 41 and is drivingly connected to the crushing roller group 42; the screen structure 44 is arranged at the bottom end of the crushing box 41 for screening the discharge material.

[0032] Specifically, a pressure-resistant layer 421 is connected to the surface of the crushing roller set 42 , and a plurality of pressure-resistant blocks 422 for mounting the crushing tooth structure are arranged on the pressure-resistant layer 421 .

[0033] More specifically, a feed opening 411 is provided at the top of the pulverizing box 41 , and the feed opening 411 is designed to be open.

[0034] In this embodiment, the crusher 4 is specifically shown, which crushes the coke powder by setting a crushing roller set 42, and the crushing roller set 42 is driven by a driving structure 43, which can be specifically driven by a driving motor, and a pressure-resistant layer 421 is installed on the surface of the crushing roller set 42, and a pressure-resistant block 422 is installed on the pressure-resistant layer 421 to install a crushing tooth structure. When crushing, the coke powder enters the inside of the crushing roller set 42, and the surface of the coke powder is squeezed by the crushing tooth structure, and the coke powder is broken by using the principle that the smaller the contact surface, the greater the pressure it bears. When crushing, the impact force generated by the crushing is buffered by the pressure-resistant block 422 and the pressure-resistant layer 421, so as to ensure the crushing effect and delay the loss of the crushing roller set 42, so as to effectively improve its service life.

[0035] The above-mentioned embodiments only express several implementation methods of the utility model, and the descriptions thereof are relatively specific and detailed, but they cannot be understood as limiting the scope of the patent of the utility model. It should be pointed out that, for ordinary technicians in this field, several variations and improvements can be made without departing from the concept of the utility model, and these all belong to the protection scope of the utility model. Therefore, the protection scope of the utility model patent shall be based on the attached claims.

Claims

1. A dry quenching dust transfer system, characterized in that: It includes an intermediate bin, a scraper conveyor, a bucket elevator, a crusher and an ash bin. The intermediate bin is connected to the bucket elevator through a first discharge chute, and the bucket elevator is connected to the ash bin through a second discharge chute. The crusher is arranged on the second discharge chute to crush the dust in the second discharge chute and then send it into the ash bin for transportation.

2. The CDQ dust transfer system according to claim 1 is characterized in that: An electric ash discharge valve is provided at the bottom end of the intermediate bin.

3. The CDQ dust transfer system according to claim 2 is characterized in that: The second material discharge chute is provided with an anti-blocking material level meter near the top of the pulverizer, and the anti-blocking material level meter is interlocked with the electric format ash discharge valve, the scraper conveyor, the bucket elevator and the pulverizer.

4. The CDQ dust transfer system according to claim 1 is characterized in that: The first material discharge chute is set at an inclined angle, and the inclined angle is set to 40-60°; the second material discharge chute is set at an inclined angle, and the inclined angle is set to 30-45°.

5. The CDQ dust transfer system according to claim 1 is characterized in that: The crusher is provided with a crushing box, a crushing roller group, a driving structure and a screen structure. The crushing box is installed on the second discharge chute, the crushing roller group is rotatably installed on the crushing box, and the crushing roller group is provided with a crushing tooth structure for crushing dust particles. The driving structure is arranged on one side of the crushing box and is drivingly connected to the crushing roller group. The screen structure is arranged at the bottom end of the crushing box for screening the discharged material.

6. The CDQ dust transfer system according to claim 5 is characterized in that: The surface of the crushing roller wheel set is connected with a pressure-resistant layer, and a plurality of pressure-resistant blocks for mounting the crushing tooth structure are arranged on the pressure-resistant layer.

7. The CDQ dust transfer system according to claim 5, characterized in that: A feeding port is arranged at the top of the pulverizing box body, and the feeding port is arranged to be open.