CN118161927A - Pulse bag type dust removal system for treating high-temperature smoke dust of metallurgical furnace - Google Patents
Pulse bag type dust removal system for treating high-temperature smoke dust of metallurgical furnace Download PDFInfo
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- CN118161927A CN118161927A CN202211587891.6A CN202211587891A CN118161927A CN 118161927 A CN118161927 A CN 118161927A CN 202211587891 A CN202211587891 A CN 202211587891A CN 118161927 A CN118161927 A CN 118161927A
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- air
- removal system
- dust removal
- main shell
- air inlet
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- 239000000428 dust Substances 0.000 title claims abstract description 91
- 239000000779 smoke Substances 0.000 title claims abstract description 21
- 238000001816 cooling Methods 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 230000000149 penetrating effect Effects 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims description 23
- 238000007664 blowing Methods 0.000 claims description 18
- 239000002184 metal Substances 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 238000009423 ventilation Methods 0.000 claims description 3
- 239000003517 fume Substances 0.000 claims 9
- 230000001276 controlling effect Effects 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 3
- 230000002035 prolonged effect Effects 0.000 abstract description 3
- 238000003723 Smelting Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005058 metal casting Methods 0.000 description 2
- 238000005272 metallurgy Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28G—CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
- F28G1/00—Non-rotary, e.g. reciprocated, appliances
- F28G1/16—Non-rotary, e.g. reciprocated, appliances using jets of fluid for removing debris
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0039—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices
- B01D46/0041—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for feeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0084—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours provided with safety means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/04—Cleaning filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/44—Auxiliary equipment or operation thereof controlling filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/44—Auxiliary equipment or operation thereof controlling filtration
- B01D46/444—Auxiliary equipment or operation thereof controlling filtration by flow measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/48—Removing dust other than cleaning filters, e.g. by using collecting trays
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B19/00—Programme-control systems
- G05B19/02—Programme-control systems electric
- G05B19/04—Programme control other than numerical control, i.e. in sequence controllers or logic controllers
- G05B19/05—Programmable logic controllers, e.g. simulating logic interconnections of signals according to ladder diagrams or function charts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/025—Other waste gases from metallurgy plants
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Environmental & Geological Engineering (AREA)
- Combustion & Propulsion (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention relates to a pulse bag type dust removal system for treating high-temperature smoke dust of a metallurgical furnace, which comprises a dust remover, a control cabinet and a cooling device, wherein the device comprises a main shell, a top cover and a bottom shell, the main shell is provided with a second air inlet and a second air outlet, and a base is arranged below the bottom shell; a plurality of U-shaped heat exchange tubes are arranged in the main shell, and a plurality of radiating fins are arranged on the heat exchange tubes in a penetrating way; the top cover is provided with a water inlet and a water outlet which are connected with the U-shaped heat exchange tube, and the lower end of the bottom shell is provided with an ash outlet valve; the second air inlet of the cooling device is connected with a high-temperature smoke dust collecting pipeline of the metallurgical furnace, the second air outlet is connected with the first air inlet of the dust remover, and the first air outlet is connected with the fan and the chimney through pipelines. According to the invention, the cooling device is arranged in front of the dust remover, the water cooling mode is adopted to reduce the temperature of high-temperature smoke dust, so that the damage of high-temperature particles in the smoke dust to the filter bag of the dust remover is prevented, the effective operation and high-efficiency dust removal of a dust removal system are ensured, the service life of the filter bag is prolonged, and the operation and maintenance cost of the system is reduced.
Description
Technical Field
The invention relates to the technical field of industrial dust collectors, in particular to a pulse bag type dust collection system for treating high-temperature smoke dust of a metallurgical furnace.
Background
The existing pulse bag type dust collector generally comprises a bracket, an ash bucket, a box body, a filter bag, a blowing ash removing device, a control device and the like, wherein an air inlet and an air outlet are arranged on the side face of the box body, an air inlet channel is arranged between the air inlet and the air outlet, an ash discharging device is arranged below the box body, and the filter bag is connected and fixed with the box body through a filter element mounting frame. The filter bag of the existing dust collector has the defect of low high temperature resistance, and if the dust treated by the dust collector contains high temperature particles, the filter bag can be burnt out.
The metallurgical industry and the metal casting factory can generate a large amount of smoke dust in the smelting process, particularly the current environment-friendly equipment level of the steel industry is lower, the pollutant emission amount is high, the environment is seriously influenced, and the improvement of the overall competitiveness of the steel industry is restricted. Typical pollutants in the exhaust gas discharged by iron and steel enterprises mainly comprise dust particles, SO2, dioxin and other pollutants; the smoke dust generated in metal smelting in a foundry factory usually contains a large amount of high-temperature particles, and when the dust is removed by a bag-type dust remover or a plastic-burning plate dust remover, the high-temperature particles often burn out filter bags or plastic-burning plate filter cores, so that not only is direct economic loss caused, but also the dust removing effect of the whole dust removing system is reduced, and even environmental pollution is caused.
At present, the national emission standard of related industries such as metallurgy is further improved, and the market also provides higher requirements for the dust remover and the filter bag or the plastic-sintered plate filter element thereof, so that the service life of the dust remover is required to be prolonged, and the running, using and maintaining costs are reduced. Therefore, it is necessary to redesign or improve the structure of the existing dust removing system, and accordingly improve the technical requirements of the existing dust remover.
Disclosure of Invention
Aiming at the defects of the prior pulse bag type dust collector, the invention aims to provide a high-temperature smoke dust removing system provided with a front cooling device, wherein the cooling device is used for cooling high-temperature smoke dust and preventing high-temperature particles from damaging a filter bag of the dust collector.
The aim of the invention is realized by adopting the following technical scheme:
The pulse bag type dust removing system comprises a dust remover and a control device, wherein the dust remover comprises a bracket, a box body, a blowing device and a filter bag, the filter bag is arranged in the box body, a first air inlet and a first air outlet are formed in the side face of the box body, an ash bucket and an ash discharging device are arranged below the box body, the dust removing system is provided with a cooling device, the device comprises a main shell, a top cover and a bottom shell, a second air inlet and a second air outlet are respectively formed in two sides of the main shell, the top cover and the bottom shell are respectively in detachable movable connection with the main shell through bolts, a base is arranged below the bottom shell, and the bottom shell is fixedly connected with the base;
A plurality of U-shaped metal heat exchange tubes are longitudinally arranged in the main shell, a plurality of metal radiating fins are arranged on the heat exchange tubes in a penetrating mode, and a plurality of penetrating vent holes are formed in the radiating fins; the top cover is provided with a water inlet and a water outlet which are respectively connected with two ends of the U-shaped heat exchange tube; the lower end of the bottom shell is provided with an ash outlet valve;
The second air inlet of the cooling device is connected with a high-temperature smoke dust collecting pipeline of the metallurgical furnace, the second air outlet is connected with the first air inlet of the dust remover, and the first air outlet is connected with the fan and the chimney through pipelines.
As the preferable technical scheme of the invention, the outer side surfaces of the main shell, which are close to the top cover and the bottom shell, are respectively provided with a plurality of air nozzles for jetting accumulated ash, and the air nozzles are communicated with a compressed air source through air pipes; the second air inlet is formed in one side face, close to the top cover, of the main shell, and the second air outlet is formed in the other side face, close to the bottom shell, of the main shell.
As the preferable technical scheme of the invention, the outer side surface of the main shell, which is close to the top cover, is provided with a first air nozzle, and the axis of the first air nozzle is perpendicular to the axis of the second air inlet; the outer side surface of the main shell, which is close to the bottom shell, is provided with a second air tap, and the axis of the second air tap is coaxial with the axis of the second air outlet.
As the preferable technical scheme of the invention, any two adjacent groups of radiating fins are arranged eccentrically to each other, so that the air duct in the main shell forms a curved channel.
As a preferable technical scheme of the invention, the radiating fin is provided with grid-shaped ventilation holes.
As a preferable technical scheme of the invention, the main shell is of a cylindrical structure, and the top cover and the bottom shell are of spherical structures; the base is arranged to be of a square box body structure, and an ash outlet door is arranged on one side face of the base.
As a preferable technical scheme of the invention, the control device comprises a PLC control cabinet and a differential pressure feedback type pulse controller, and the pulse controller is electrically connected with the blowing device;
the blowing device is arranged on the box body and comprises a blowing pipe, a nozzle and an electromagnetic valve, and the electromagnetic valve is arranged on the blowing pipe and is electrically connected with the pulse controller.
As a preferable technical scheme of the invention, the ash discharging device comprises a manual ash discharging device and an automatic ash discharging device; the manual ash discharging device comprises a star-shaped ash discharging valve, and the automatic ash discharging device comprises a screw conveyor.
As the preferable technical scheme of the invention, the upper end of the filter bag is connected with the filter bag mounting frame, the lower end of the filter bag is connected with the filter bag positioning frame, and a guide plate is arranged between the filter bags.
As a preferable technical scheme of the invention, an air inlet channel is arranged between the first air inlet and the first air outlet, an air quantity regulating valve is arranged on the air inlet channel, and an air channel switching mechanism is arranged on the box body.
The beneficial effects of the invention are as follows: compared with the prior art, the invention has the advantages that the cooling device is arranged in front of the dust collector of the dust collection system, and the cooling device adopts the water cooling mode to reduce the temperature of high-temperature smoke dust, so that the damage of high-temperature particles in the smoke dust to the filter bag of the dust collector is prevented.
The U-shaped metal heat exchange tube is provided with a plurality of layers of staggered grid-shaped radiating fins, the outer side of the main shell is provided with a plurality of air nozzles connected with a high-pressure air source for regularly jetting accumulated ash on the radiating fins, so that the effective operation and high-efficiency dust removal of a dust removal system are ensured, the service life of a filter bag or a plastic-sintered plate of the dust remover is prolonged, and the operation and maintenance cost of the dust removal system is reduced.
The invention adopts the differential pressure feedback type pulse electronic controller to automatically adjust the pulse interval of the blowing system according to the running resistance of the dust removal system, thereby reducing the power loss, and prolonging the service life of vulnerable parts such as the diaphragm, the electromagnetic valve and the like. The invention has the advantages of high efficiency, energy saving, stable operation, reliable performance, high dust removal efficiency and convenient maintenance.
Drawings
FIG. 1 is a schematic diagram of the dust removal system of the present invention;
FIG. 2 is a schematic view of the structure of the dust collector of the present invention;
FIG. 3 is a left-hand structural schematic diagram of FIG. 2;
FIG. 4 is a schematic view of the cooling device of the present invention.
In the figure: 1. the dust remover comprises a dust remover, 2, a box body, 3, a blowing device, 4, an ash discharging device, 5, an escalator platform, 6, a switching mechanism, 7, a filter bag, 8, a guide plate, 9, a first air outlet, 10, a first air inlet, 11, a filter bag positioning frame, 12, an air quantity regulating valve, 13, a screw conveyor, 14, a filter bag mounting frame, 15, an ash bucket, 16, a bracket, 17, a fan, 18, a chimney, 19, a control cabinet, 20, a cooling device, 21, a main shell, 22, a top cover, 23, a bottom shell, 24, a second air inlet, 25, a second air outlet, 26, a base, 27, a heat exchange tube, 28, a radiating fin, 29, an ash outlet valve, 30, a first air nozzle, 31, a second air nozzle, 32, an ash outlet door, 33, a water inlet, 34 and a water outlet.
Detailed Description
The invention is further described with reference to the drawings and the specific embodiments below:
As shown in fig. 1 to 4, a pulse bag type dust removal system for treating high-temperature smoke dust of a metallurgical furnace comprises a dust remover 1 and a control device, wherein the dust remover 1 comprises a bracket 16, a box body 2, a blowing device 3 and a filter bag 7, the filter bag 7 is arranged in the box body 2, a first air inlet 10 and a first air outlet 9 are arranged on the side surface of the box body 2, an ash bucket 15 and an ash discharging device 4 are arranged below the box body 2, the dust removal system is provided with a cooling device 20, the device comprises a main shell 21, a top cover 22 and a bottom shell 23, two sides of the main shell 21 are respectively provided with a second air inlet 24 and a second air outlet 25, the top cover 22 and the bottom shell 23 are respectively in detachable movable connection with the main shell 21 through bolts, a base 26 is arranged below the bottom shell 23, and the bottom shell 23 is fixedly connected with the base 26; a plurality of U-shaped metal heat exchange tubes 27 are longitudinally arranged in the main shell 21, a plurality of metal cooling fins 28 are arranged on the heat exchange tubes 27 in a penetrating manner, and a plurality of penetrating vent holes are formed in the cooling fins 28; the top cover 22 is provided with a water inlet 33 and a water outlet 34, and the water inlet 33 and the water outlet 34 are respectively connected with two ends of the U-shaped heat exchange tube 27; the lower end of the bottom shell 23 is provided with an ash outlet valve 29; the second air inlet 24 of the cooling device 20 is connected with a high-temperature smoke dust collecting pipeline of the metallurgical furnace, the second air outlet 25 is connected with the first air inlet 10 of the dust remover, and the first air outlet 9 is connected with the fan 17 and the chimney 18 through pipelines.
In this embodiment, the outer side surfaces of the main casing 21, which are close to the top cover 22 and the bottom casing 23, are respectively provided with a plurality of air nozzles for jetting accumulated ash, and the air nozzles are communicated with a compressed air source through an air pipe; the second air inlet 24 is disposed on a side surface of the main housing 21 near the top cover 22, and the second air outlet 25 is disposed on another side surface of the main housing 21 near the bottom shell 23. The outer side surface of the main shell 21, which is close to the top cover 22, is provided with a first air nozzle 30, and the axis of the first air nozzle 30 is perpendicular to the axis of the second air inlet 24; the outer side surface of the main housing 21, which is close to the bottom shell 23, is provided with a second air tap 31, and the axis of the second air tap 31 is coaxial with the axis of the second air outlet 25.
Any two adjacent groups of cooling fins 28 of the cooling device 20 are arranged eccentrically to each other, so that the air duct in the main shell 21 forms a curved channel; the heat sink 28 is provided with mesh-like ventilation holes. The main shell 21 is of a cylindrical structure, and the top cover 22 and the bottom shell 23 are of spherical structures; the base 26 is of a square box structure, and an ash outlet door 32 is arranged on one side surface of the base 26.
In this embodiment, the control device includes a PLC control cabinet 19 and a differential pressure feedback type pulse controller, and the pulse controller is electrically connected with the blowing device 3; the blowing device 3 is arranged on the box body 2, and the blowing device 3 comprises a blowing pipe, a nozzle and an electromagnetic valve, wherein the electromagnetic valve is arranged on the blowing pipe and is electrically connected with the pulse controller.
The ash discharging device 4 comprises a manual ash discharging device and an automatic ash discharging device; the manual ash discharging device comprises a star-shaped ash discharging valve, and the automatic ash discharging device comprises a screw conveyor 13. The upper end of the filter bag 7 is connected with a filter bag mounting frame 14, the lower end of the filter bag 7 is connected with a filter bag positioning frame 11, and a guide plate 8 is arranged between the filter bags 7. An air inlet channel is arranged between the first air inlet 10 and the first air outlet 9, an air quantity regulating valve 12 is arranged on the air inlet channel, a staircase platform 5 is arranged on the box body 2, and an air inlet channel switching mechanism 6 is arranged on the staircase platform 5.
The dust remover 1 is provided with a unit combination type, each unit is provided with 24 groups of filter bags, each group is provided with 14 filter bags, namely 336 filter bags are arranged in each unit, and the filter bags 7 of the embodiment adopt a film composite filter material. According to the invention, the cooling device 20 is arranged in front of the dust collector 1 of the dust collection system, the cooling device 20 adopts a water cooling mode to reduce the temperature of high-temperature smoke dust, and the damage of high-temperature particles in the smoke dust to the filter bag 7 of the dust collector 1 is prevented. The dust removing system is particularly suitable for removing dust and purifying high-temperature smoke dust generated in the metal smelting process, such as industries of metallurgy, metal casting and the like.
The above examples are only for illustrating the concept and technical features of the present invention, and are intended to enable those skilled in the art to understand the technical scheme and embodiments of the present invention, and thus, the scope of the present invention is not limited thereto. All equivalent substitutions or equivalent changes according to the technical proposal of the invention are covered in the protection scope of the claims of the invention.
Claims (10)
1. A pulse bag type dust collecting system for metallurgical furnace high temperature smoke and dust is administered, including dust remover and controlling means, the dust remover includes support, box, jetting device and filter bag, and the filter bag is established in the box, and the box side is equipped with first air intake and first air outlet, is equipped with ash bucket and ash discharging device below the box, characterized by: the dust removal system is provided with a cooling device, the device comprises a main shell, a top cover and a bottom shell, a second air inlet and a second air outlet are respectively arranged on two sides of the main shell, the top cover and the bottom shell are respectively and movably connected with the main shell in a detachable mode through bolts, a base is arranged below the bottom shell, and the bottom shell is fixedly connected with the base;
A plurality of U-shaped metal heat exchange tubes are longitudinally arranged in the main shell, a plurality of metal radiating fins are arranged on the heat exchange tubes in a penetrating mode, and a plurality of penetrating vent holes are formed in the radiating fins; the top cover is provided with a water inlet and a water outlet which are respectively connected with two ends of the U-shaped heat exchange tube; the lower end of the bottom shell is provided with an ash outlet valve;
The second air inlet of the cooling device is connected with a high-temperature smoke dust collecting pipeline of the metallurgical furnace, the second air outlet is connected with the first air inlet of the dust remover, and the first air outlet is connected with the fan and the chimney through pipelines.
2. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 1, wherein: the outer side surfaces of the main shell, which are close to the top cover and the bottom shell, are respectively provided with a plurality of air nozzles for jetting accumulated ash, and the air nozzles are communicated with a compressed air source through air pipes; the second air inlet is formed in one side face, close to the top cover, of the main shell, and the second air outlet is formed in the other side face, close to the bottom shell, of the main shell.
3. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 2, wherein: the outer side surface of the main shell, which is close to the top cover, is provided with a first air tap, and the axis of the first air tap is perpendicular to the axis of the second air inlet; the outer side surface of the main shell, which is close to the bottom shell, is provided with a second air tap, and the axis of the second air tap is coaxial with the axis of the second air outlet.
4. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 1, wherein: any two adjacent groups of radiating fins are arranged eccentrically, so that a curved channel is formed by the air duct in the main shell.
5. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 4, wherein: and the radiating fin is provided with grid-shaped ventilation holes.
6. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 1, wherein: the main shell is of a cylindrical structure, and the top cover and the bottom shell are of spherical structures; the base is arranged to be of a square box body structure, and an ash outlet door is arranged on one side face of the base.
7. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 1, wherein: the control device comprises a PLC control cabinet and a differential pressure feedback type pulse controller, and the pulse controller is electrically connected with the blowing device;
the blowing device is arranged on the box body and comprises a blowing pipe, a nozzle and an electromagnetic valve, and the electromagnetic valve is arranged on the blowing pipe and is electrically connected with the pulse controller.
8. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 1, wherein: the ash discharging device comprises a manual ash discharging device and an automatic ash discharging device; the manual ash discharging device comprises a star-shaped ash discharging valve, and the automatic ash discharging device comprises a screw conveyor.
9. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 1, wherein: the upper end of the filter bag is connected with a filter bag mounting frame, the lower end of the filter bag is connected with a filter bag positioning frame, and a guide plate is arranged between the filter bags.
10. The pulse bag house dust removal system for high temperature fume abatement of metallurgical furnaces of claim 1, wherein: an air inlet channel is arranged between the first air inlet and the first air outlet, an air quantity regulating valve is arranged on the air inlet channel, and an air channel switching mechanism is arranged on the box body.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211587891.6A CN118161927A (en) | 2022-12-11 | 2022-12-11 | Pulse bag type dust removal system for treating high-temperature smoke dust of metallurgical furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211587891.6A CN118161927A (en) | 2022-12-11 | 2022-12-11 | Pulse bag type dust removal system for treating high-temperature smoke dust of metallurgical furnace |
Publications (1)
Publication Number | Publication Date |
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CN118161927A true CN118161927A (en) | 2024-06-11 |
Family
ID=91349386
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN202211587891.6A Pending CN118161927A (en) | 2022-12-11 | 2022-12-11 | Pulse bag type dust removal system for treating high-temperature smoke dust of metallurgical furnace |
Country Status (1)
Country | Link |
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CN (1) | CN118161927A (en) |
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2022
- 2022-12-11 CN CN202211587891.6A patent/CN118161927A/en active Pending
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