Boiler dust remover with deslagging structure

By introducing cooling and slag discharge functions into the boiler dust collector, the corrosion and inefficiency problems caused by the high flue gas temperature of the existing boiler dust collector are solved, and a longer equipment service life and higher processing efficiency are achieved.

CN222937841UActive Publication Date: 2025-06-03BOTOU KANGJIE ENVIRONMENTAL PROTECTION CO LTD
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Patent Information

Application Number
CN202422113745.0
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-08-30
Publication Date
2025-06-03
Estimated Expiration
2034-08-30

AI Technical Summary

Technical Problem

The existing boiler dust removal device lacks cooling devices, which leads to excessive flue gas temperature and easily corrode the screen plate, reducing dust removal efficiency and shortening the service life of the equipment.

Method used

A boiler dust collector with a slag discharge structure is designed, including a cooling device, a slag discharge device and a dust collector. The cooling device cools the flue gas through the circulating water pipe, and the slag discharge device performs slag discharge of the boiler while removing dust.

Benefits of technology

The cooling device avoids excessive flue gas temperature, extends the service life of the dust removal device, and accelerates the processing speed of the boiler-generated substances through the slag discharge device, and improves the overall processing efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a boiler dust remover with a deslagging structure, and relates to the technical field of boiler dust removal. The outer side of the cooling device is fixedly connected with the outer side of the feeding pipe, and the cooling device is used for cooling flue gas; the outer side of the slag discharging device is fixedly connected with the side, away from the feeding pipe, of the cooling device, and the slag discharging device is used for discharging ash slag; the outer side of the dust removal device is fixedly connected with the side, away from the cooling device, of the slag discharge device, and the dust removal device is used for removing dust in the flue gas; and the bottom of the air outlet pipe is fixedly connected with the top of the dust removal device. According to the device, flue gas is cooled by arranging the cooling device, the situation that the temperature of the flue gas is too high, and the dust removal device is damaged is avoided, the boiler is subjected to slag removal while dust removal is conducted by arranging the slag removal device, and pollutants generated by the boiler are conveniently treated.
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Description

Technical Field

[0001] The utility model relates to the technical field of boiler dust removal, and particularly relates to a boiler dust collector with a slag discharging structure. Background Art

[0002] A boiler is an energy conversion device. The energy input into the boiler includes chemical energy in fuel and electric energy. The boiler outputs steam, high-temperature water or organic heat carriers with a certain amount of heat energy. The hot water or steam generated in the boiler can directly provide the required heat energy for industrial production and people's livelihood, or can be converted into mechanical energy through a steam power device, or further converted into electric energy through a generator.

[0003] However, in the prior art, the slag removal and dust removal of boilers are generally carried out separately, and the efficiency of dust removal and slag removal is relatively low. Moreover, the existing dust removal devices lack a cooling device. When the temperature of the flue gas is too high, it is easy to corrode the sieve plate and reduce the service life of the dust removal device. To solve the above problems, we propose a boiler dust collector with a slag discharging structure. Summary of the Utility Model

[0004] In view of the deficiencies of the prior art, the technical solution adopted by the utility model to solve its technical problems is: a boiler dust collector with a slag discharging structure, including a feed pipe; a cooling device, the outside of the cooling device is fixedly connected to the outside of the feed pipe, and the cooling device is used for cooling the flue gas; a slag discharging device, the outside of the slag discharging device is fixedly connected to the side of the cooling device away from the feed pipe, and the slag discharging device is used for discharging ash and slag; a dust removal device, the outside of the dust removal device is fixedly connected to the side of the slag discharging device away from the cooling device, and the dust removal device is used for removing dust in the flue gas; an air outlet pipe, the bottom of the air outlet pipe is fixedly connected to the top of the dust removal device. By setting the cooling device, the flue gas is cooled to avoid the temperature of the flue gas being too high and damaging the dust removal device. By setting the slag discharging device, while dust is removed, the boiler is slag discharged, which is convenient for treating the pollutants generated by the boiler.

[0005] Preferably, the cooling device includes a pipeline, the outside of the pipeline is fixedly connected to the outside of the feed pipe, and a circulating water pipe is sleeved outside the pipeline. The two ends of the circulating water pipe are fixedly connected to a water storage tank. By setting the cooling device, the flue gas is cooled to avoid the temperature of the flue gas being too high and damaging the dust removal device. At the same time, the cooling device recovers the heat of the flue gas through water flow, reducing energy waste.

[0006] Preferably, the slag discharging device includes an air inlet pipe, the outer side of the air inlet pipe is fixedly connected to the side of the pipeline away from the feed pipe, the bottom of the air inlet pipe is fixedly connected with a slag discharging assembly, and the side of the slag discharging assembly away from the air inlet pipe is fixedly connected with a cooling bin. By setting the slag discharging device, the device can discharge slag and remove dust from the boiler simultaneously, accelerating the processing speed of the substances generated by the boiler.

[0007] Preferably, the slag discharging assembly includes a slag discharging pipe, the top of the slag discharging pipe is fixedly connected to the bottom of the air inlet pipe, the side of the slag discharging pipe away from the air inlet pipe is fixedly connected to the outer side of the cooling bin, a blower is fixedly connected to the outer side of the slag discharging pipe, and a guiding plate is fixedly connected to the inner side of the air inlet pipe. By setting the slag discharging assembly, the ash slag is processed, separating the ash slag from the flue gas and preventing the ash slag from entering the dust removal device.

[0008] Preferably, the dust removal device includes a housing, the outer side of the housing is fixedly connected to the side of the air inlet pipe away from the pipeline, a sieve plate is fixedly connected to the inner side of the housing, and an activated carbon plate is fixedly connected to the inner side of the air outlet pipe. By setting the dust removal device, the flue gas is processed to prevent the direct emission of the flue gas to the outside world, preventing the flue gas from polluting the atmosphere and protecting the health of the staff.

[0009] Preferably, a connecting pipe is fixedly connected to the top of the housing, the bottom of the connecting pipe penetrates through the housing and is fixedly connected with a spray head, and a drain pipe is fixedly connected to the bottom of the housing. The sieve plate is backflushed by water flow to prevent dust from accumulating on the sieve plate and affecting the filtering effect of the sieve plate. At the same time, the water flow further reduces the temperature of the flue gas, preventing the discharged flue gas from scalding the human body.

[0010] The beneficial effects of the present utility model are as follows:

[0011] 1. By setting the cooling device, the present utility model cools the flue gas, preventing the temperature of the flue gas from being too high and damaging the dust removal device, extending the service life of the dust removal device. At the same time, the cooling device recovers the heat of the flue gas through water flow, reducing energy waste.

[0012] 2. By setting the slag discharging device, the present utility model enables the device to discharge slag and remove dust from the boiler simultaneously, accelerating the processing speed of the substances generated by the boiler. BRIEF DESCRIPTION OF THE DRAWINGS

[0013] Figure 1 is the front view of the present utility model;

[0014] Figure 2 is the sectional view of the present utility model;

[0015] Figure 3 is the structural schematic diagram of the cooling device of the present utility model;

[0016] Figure 4 is a structural sectional view of the slag discharging assembly of the present utility model;

[0017] Figure 5 is a structural schematic diagram of the dust removal device of the present utility model;

[0018] Figure 6 is a structural sectional view of the dust removal device of the present utility model.

[0019] In the figure: 1, feed pipe; 2, cooling device; 21, pipe; 22, circulating water pipe; 23, water storage tank; 3, slag discharging device; 31, intake pipe; 32, slag discharging assembly; 321, slag discharging pipe; 322, fan; 323, guiding plate; 33, cooling bin; 4, dust removal device; 41, housing; 42, sieve plate; 43, activated carbon plate; 44, connecting pipe; 45, spray head; 46, drain pipe; 5, outlet pipe. Specific embodiments

[0020] The present utility model will be further described in detail below with reference to the accompanying drawings and specific embodiments. The embodiments of the present utility model are given for purposes of illustration and description, and are not intended to be exhaustive or to limit the present utility model to the disclosed form. Many modifications and variations are obvious to those of ordinary skill in the art. The embodiments are chosen and described in order to better explain the principles and practical applications of the present utility model, and to enable those of ordinary skill in the art to understand the present utility model and design various embodiments with various modifications suitable for specific purposes.

[0021] Embodiment:

[0022] Please refer to Figures 1-6, the present utility model provides a technical solution: a boiler dust collector with a slag discharge structure, including a feed pipe 1; a cooling device 2, the outer side of the cooling device 2 is fixedly connected to the outer side of the feed pipe 1, and the cooling device 2 is used to cool the flue gas; a slag discharge device 3, the outer side of the slag discharge device 3 is fixedly connected to the side of the cooling device 2 away from the feed pipe 1, and the slag discharge device 3 is used to discharge ash; a dust removal device 4, the outer side of the dust removal device 4 is fixedly connected to the side of the slag discharge device 3 away from the cooling device 2, and the dust removal device 4 is used to remove dust in the flue gas; an air outlet pipe 5, the bottom of the air outlet pipe 5 is fixedly connected to the top of the dust removal device 4. When in use, the ash and flue gas of the boiler are discharged into the feed pipe 1, and the ash and flue gas move along the feed pipe 1 into the cooling device 2. The cooling device 2 cools the ash and flue gas. The ash and flue gas with decreased temperature move along the cooling device 2 into the slag discharge device 3. The slag discharge device 3 discharges the ash, and the flue gas flows along the slag discharge device 3 into the dust removal device 4. After being dust-removed by the dust removal device 4, the flue gas flows out along the air outlet pipe 5. By setting the cooling device 2 to cool the flue gas, it is avoided that the temperature of the flue gas is too high and the dust removal device 4 is damaged. By setting the slag discharge device 3, while dust removal is carried out, the boiler is slag-discharged, which is convenient for treating the pollutants generated by the boiler.

[0023] The cooling device 2 includes a pipeline 21, the outer side of the pipeline 21 is fixedly connected to the outer side of the feed pipe 1, and a circulating water pipe 22 is sleeved outside the pipeline 21. Both ends of the circulating water pipe 22 are fixedly connected with a water storage tank 23. When in use, the ash and flue gas move along the feed pipe 1 into the cooling device 2, and the ash and flue gas move along the pipeline 21 towards the slag discharge device 3. During this period, the water storage tank 23 sends the cold water inside into the circulating water pipe 22, and the cold water flows along the circulating water pipe 22 to the pipeline 21. The water flow exchanges heat with the flue gas to reduce the temperature of the ash and flue gas. The ash and flue gas with decreased temperature flow along the pipeline 21 into the slag discharge device 3. By setting the cooling device 2 to cool the flue gas, it is avoided that the temperature of the flue gas is too high and the dust removal device 4 is damaged. At the same time, the cooling device 2 recovers the heat of the flue gas through the water flow, reducing the waste of energy.

[0024] The slag discharge device 3 includes an air inlet pipe 31, the outer side of the air inlet pipe 31 is fixedly connected to the side of the pipeline 21 away from the feed pipe 1, and a slag discharge assembly 32 is fixedly connected to the bottom of the air inlet pipe 31. The side of the slag discharge assembly 32 away from the air inlet pipe 31 is fixedly connected with a cooling bin 33. When in use, the ash and flue gas with decreased temperature flow along the pipeline 21 into the air inlet pipe 31, the flue gas flows along the air inlet pipe 31 into the dust removal device 4, and the ash moves along the slag discharge assembly 32 into the cooling bin 33. There is cooling water stored in the cooling bin 33, and the cooling water cools the ash. After cooling is completed, the ash is further processed. By setting the slag discharge device 3, the device can carry out slag discharge and dust removal of the boiler at the same time, accelerating the speed of treating the substances generated by the boiler.

[0025] The slag discharging assembly 32 includes a slag discharging pipe 321. The top of the slag discharging pipe 321 is fixedly connected to the bottom of the air inlet pipe 31. One side of the slag discharging pipe 321 away from the air inlet pipe 31 is fixedly connected to the outer side of the cooling bin 33. A blower 322 is fixedly connected to the outer side of the slag discharging pipe 321. A guiding plate 323 is fixedly connected to the inner side of the air inlet pipe 31. During use, the ash slag and flue gas with reduced temperature flow along the pipeline 21 into the interior of the air inlet pipe 31. The ash slag and flue gas are blocked by the guiding plate 323 in the slag discharging assembly 32 and cannot directly pass through the air inlet pipe 31. At this time, the blower 322 is in an open state. The blower 322 drives the air flow to move towards the direction of the guiding plate 323. The flue gas is driven to move upward, passes through above the guiding plate 323, and then flows along the air inlet pipe 31 into the dust removal device 4. Since the ash slag and some larger impurities are larger and have a greater mass, the air flow cannot drive the ash slag to move. Affected by gravity, the ash slag falls downward into the interior of the slag discharging pipe 321. Since the slag discharging pipe 321 is inclined, the ash slag will slide downward along the slag discharging pipe 321. The ash slag moves along the slag discharging pipe 321 into the interior of the cooling bin 33. By setting the slag discharging assembly 32, the ash slag is processed to separate the ash slag from the flue gas, preventing the ash slag from entering the dust removal device 4.

[0026] The dust removal device 4 includes a housing 41. The outer side of the housing 41 is fixedly connected to one side of the air inlet pipe 31 away from the pipeline 21. A sieve plate 42 is fixedly connected to the inner side of the housing 41. An activated carbon plate 43 is fixedly connected to the inner side of the air outlet pipe 5. During use, the flue gas moves upward along the housing 41 to the sieve plate 42. The sieve plate 42 filters the dust in the flue gas. The filtered flue gas flows upward into the interior of the air outlet pipe 5. After the flue gas passes through the filtration of the activated carbon plate 43, it flows along the air outlet pipe 5 to the outside. By setting the dust removal device 4, the flue gas is processed to prevent the flue gas from being directly discharged to the outside, preventing the flue gas from polluting the atmosphere and protecting the health of the staff.

[0027] A connecting pipe 44 is fixedly connected to the top of the housing 41. The bottom of the connecting pipe 44 penetrates through the housing 41 and is fixedly connected to a spray head 45. A drain pipe 46 is fixedly connected to the bottom of the housing 41. During use, the connecting pipe 44 is connected to an external water source. The external water source sends water flow into the interior of the spray head 45 through the connecting pipe 44. The spray head 45 sprays the water flow, and the water flow flushes the sieve plate 42. After the dust removal is completed, the sewage is discharged through the drain pipe 46. By using the water flow to perform backwashing on the sieve plate 42, it is avoided that dust accumulates on the sieve plate 42, affecting the filtering effect of the sieve plate 42. At the same time, the water flow further reduces the temperature of the flue gas, preventing the discharged flue gas from scalding the human body.

[0028] Working principle:

[0029] During use, the ash and flue gas of the boiler are discharged into the feed pipe 1. The ash and flue gas move along the feed pipe 1 into the cooling device 2. The ash and flue gas move along the pipe 21 towards the slag discharging device 3. During this period, the water storage tank 23 sends the cold water inside into the circulating water pipe 22. The cold water flows along the circulating water pipe 22 to the pipe 21. The water flow exchanges heat with the flue gas to reduce the temperature of the ash and flue gas. The ash and flue gas with reduced temperature flow along the pipe 21 into the slag discharging device 3.

[0030] The ash and flue gas with reduced temperature flow along the pipe 21 into the intake pipe 31. The ash and flue gas are blocked by the guide plate 323 in the slag discharging assembly 32 and cannot directly pass through the intake pipe 31. At this time, the fan 322 is in the on state. The fan 322 drives the air flow to move towards the direction of the guide plate 323. The flue gas is driven to move upward, passes through above the guide plate 323, and then flows along the intake pipe 31 into the dust removal device 4. Since the ash and some larger impurities are larger and have a greater mass, the air flow cannot drive the ash to move. Affected by gravity, the ash falls downward into the slag discharging pipe 321. Since the slag discharging pipe 321 is inclined, the ash will slide downward along the slag discharging pipe 321. The ash moves along the slag discharging pipe 321 into the cooling bin 33. The cooling bin 33 stores cooling water, and the cooling water cools the ash. After the ash is cooled, the ash is further processed.

[0031] The flue gas moves upward along the outer shell 41 to the sieve plate 42. The sieve plate 42 filters the dust in the flue gas. The filtered flue gas flows upward into the outlet pipe 5. After the flue gas is filtered by the activated carbon plate 43, it flows along the outlet pipe 5 to the outside. At the same time, the external water source sends water flow into the spray head 45 through the connecting pipe 44. The spray head 45 sprays the water flow, and the water flow flushes the sieve plate 42. After the dust removal is completed, the sewage is discharged through the drain pipe 46.

[0032] Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art and related fields without creative efforts shall fall within the protection scope of the present invention. The structures, devices, and operation methods not specifically described and explained in the present invention, unless otherwise specified and limited, are implemented according to the conventional means in the art.

Claims

1. A boiler dust collector with a slag discharge structure, characterized in that: include: Feed pipe (1); A cooling device (2), the outer side of the cooling device (2) being fixedly connected to the outer side of the feed pipe (1), and the cooling device (2) being used for cooling the flue gas; A slag discharge device (3), the outer side of the slag discharge device (3) being fixedly connected to a side of the cooling device (2) away from the feed pipe (1), and the slag discharge device (3) being used to discharge ash; A dust removal device (4), the outer side of the dust removal device (4) being fixedly connected to a side of the slag discharge device (3) away from the cooling device (2), and the dust removal device (4) being used to remove dust in the flue gas; An air outlet pipe (5), the bottom of which is fixedly connected to the top of the dust removal device (4).

2. The boiler dust collector with a slag discharge structure according to claim 1, characterized in that: The cooling device (2) comprises a pipeline (21), the outer side of the pipeline (21) is fixedly connected to the outer side of the feed pipe (1), the outer side of the pipeline (21) is sleeved with a circulating water pipe (22), and both ends of the circulating water pipe (22) are fixedly connected to a water storage tank (23).

3. The boiler dust collector with a slag discharge structure according to claim 2, characterized in that: The slag discharge device (3) comprises an air inlet pipe (31), the outer side of the air inlet pipe (31) is fixedly connected to a side of the pipeline (21) away from the feed pipe (1), the bottom of the air inlet pipe (31) is fixedly connected to a slag discharge assembly (32), and the side of the slag discharge assembly (32) away from the air inlet pipe (31) is fixedly connected to a cooling bin (33).

4. The boiler dust collector with a slag discharge structure according to claim 3, characterized in that: The slag discharge assembly (32) comprises a slag discharge pipe (321), the top of the slag discharge pipe (321) is fixedly connected to the bottom of the air inlet pipe (31), the side of the slag discharge pipe (321) away from the air inlet pipe (31) is fixedly connected to the outside of the cooling bin (33), the outside of the slag discharge pipe (321) is fixedly connected to a fan (322), and the inside of the air inlet pipe (31) is fixedly connected to a guide plate (323).

5. The boiler dust collector with a slag discharge structure according to claim 3, characterized in that: The dust removal device (4) comprises an outer shell (41), the outer side of the outer shell (41) is fixedly connected to a side of the air inlet pipe (31) away from the pipeline (21), the inner side of the outer shell (41) is fixedly connected to a sieve plate (42), and the inner side of the air outlet pipe (5) is fixedly connected to an activated carbon plate (43).

6. The boiler dust collector with a slag discharge structure according to claim 5, characterized in that: The top of the shell (41) is fixedly connected to a connecting pipe (44), the bottom of the connecting pipe (44) passes through the shell (41) and is fixedly connected to a spray head (45), and the bottom of the shell (41) is fixedly connected to a drain pipe (46).