CN211189591U - Novel combined type dust remover of adaptable different operating modes - Google Patents
Novel combined type dust remover of adaptable different operating modes Download PDFInfo
- Publication number
- CN211189591U CN211189591U CN201921705451.XU CN201921705451U CN211189591U CN 211189591 U CN211189591 U CN 211189591U CN 201921705451 U CN201921705451 U CN 201921705451U CN 211189591 U CN211189591 U CN 211189591U
- Authority
- CN
- China
- Prior art keywords
- chamber
- dust
- partition plate
- efficiency
- dust removal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Cyclones (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model discloses a novel combined type dust remover of adaptable different operating modes. The device comprises a cyclone separator, a high-efficiency dust removal chamber and a partition plate, wherein the cyclone separator is arranged around the outer wall of the high-efficiency dust removal chamber, the partition plate is positioned at the upper part of the high-efficiency dust removal chamber, holes are formed in the partition plate, and the partition plate divides the high-efficiency dust removal chamber into an upper clean gas sub-chamber and a lower dust removal sub-chamber; the filter core of high-efficient clean room is connected on the hole of baffle, the filter core is located dust removal portion down, cyclone and the lower dust removal portion wall sliding connection of high-efficient clean room, cyclone's air outlet and the flue gas access connection of high-efficient clean room. The utility model discloses can require to change the filter core kind according to the dust removal, cyclone can change quantity and the mode of arranging according to operational environment, can require to change the import amount of wind according to different operating modes, have strong adaptability, area is little, the pressure difference is little, dust collection efficiency is high, the easy advantage of installing and maintaining of importing.
Description
Technical Field
The utility model relates to a combined type dust remover field, specifically speaking relates to a novel combined type dust remover of adaptable different work condition.
Background
The pollution of industrial waste gas to the atmosphere cannot be ignored. Fine particles contained in industrial exhaust gas are one of the important sources of air pollution problems such as haze and the like. Therefore, the research and improvement of the industrial dust removal technology are very important for treating the atmospheric pollution.
The most common equipment for industrial dust removal at present is a bag-type dust remover, a filter cartridge dust remover, a cyclone separator and the like. The bag-type dust collector is most widely used, has high dust collection efficiency which can reach more than 99 percent and can filter micro particles below 5 microns. However, in order to improve the dust collection efficiency and the service life of the filter bag and reduce the energy consumption, the air flow speed and the particle size of the particles entering the bag-type dust collector are generally not too large, for example, the filtering air speed of the glass fiber bag-type dust collector with relatively high strength is about 0.5-0.8 m/s, and the particle size of the particles to be treated is usually below 5 microns. And the high temperature and high humidity environment has great adverse effect on the filtering efficiency and the service life of the filter bag. The cartridge dust collector features are similar to a bag-type dust collector. The cyclone separator has a slightly lower filtering efficiency than a bag-type dust collector or a filter cartridge dust collector, and generally treats particles with the particle size of more than 15 microns, and the efficiency is about 80-85%. However, the requirement on the air flow condition is not high, and the special air flow such as high temperature, high humidity and the like can be treated.
Currently, some industrial dust removal systems employ multi-stage filtration in order to compensate for the short plates of various types of dust removal devices. Take cyclone separators and bag house collectors as examples: the dusty airflow enters the cyclone separator after being captured by the exhaust hood, and most of particulate matters, especially particles with larger particle sizes, can be settled under the action of gravity and the like; then the smaller particles enter the bag type dust collector along with the air flow and are filtered by the cloth bag, and finally the clean air flow is discharged through the exhaust pipeline.
However, the multistage filtration generally occupies a large area, the pipeline is complex, the capability of adapting to the working environment is poor, the energy consumption is high, and the design and maintenance cost is high.
Disclosure of Invention
The utility model aims to solve the technical problem that a novel combined type dust remover of adaptable different work condition is provided, can integrate the advantage of various dust removers, compensate the short slab of single dust remover, can make the device satisfy the requirement of different operational environment and dust removal operating mode again. In order to achieve the above object, the embodiment of the present invention provides a technical solution:
a novel combined type dust remover adaptable to different working conditions comprises a cyclone separator, a high-efficiency dust removing chamber and a partition plate, wherein the cyclone separator is arranged around the outer wall of the high-efficiency dust removing chamber, the partition plate is positioned at the upper part of the high-efficiency dust removing chamber, holes are formed in the partition plate, and the partition plate divides the high-efficiency dust removing chamber into an upper clean gas sub-chamber and a lower dust removing sub-chamber; the filter core of high-efficient clean room is connected on the hole of baffle, the filter core is located the sub-room that removes dust down, cyclone and the lower sub-room wall sliding connection that removes dust of high-efficient clean room, cyclone's air outlet and the flue gas access connection of high-efficient clean room.
Preferably, the filter element of the high-efficiency dust removal chamber is a bag type dust remover or a filter cartridge dust remover.
As a preferred example, the composite dust remover further comprises an ash bucket, and the ash bucket is positioned at the lower part of the high-efficiency dust removing chamber; the dust hopper is connected with a dust outlet at the bottom of the cyclone separator.
Preferably, the upper clean gas sub-chamber is provided with a clean gas outlet.
As a preferred example, the composite dust remover further comprises a pulse-jet ash removal device, the pulse-jet ash removal device is located in the upper clean gas sub-chamber, and the pulse-jet ash removal device is located above the partition plate.
As a preferred example, the pulse blowing ash removal device comprises an air bag, an electromagnetic pulse valve and a blowing pipe, wherein an air outlet of the blowing pipe is opposite to a bag opening of the filter element, and the electromagnetic pulse valve is positioned in the blowing pipe.
As a preferred example, the filter element of the high-efficiency dust removal chamber is detachably connected with the holes of the partition plate.
As a preferred example, the filter element of the high-efficiency dust removal chamber is in threaded connection with the holes of the partition plate. As a preferable example, the composite dust remover further comprises an automatic regulating valve, and the automatic regulating valve is arranged at a flue gas inlet of the cyclone separator.
Preferably, the composite dust collector further comprises a poppet valve, and the poppet valve is arranged above the air channel of the hole of the partition plate.
Compared with the prior art, the novel combined type dust remover which can adapt to different working conditions can ensure that the external cyclone separator can adapt to different industrial space environments so as to meet different industrial building requirements; meanwhile, the inlet air quantity of the external cyclone separator and the start-stop ratio of the cyclone separator can be changed according to different working condition requirements, the type of the internal filter element can be changed according to the requirements of designers, and the quick-change device can meet the replacement requirement.
Drawings
Fig. 1 is a schematic structural diagram of an embodiment of the present invention;
FIG. 2 is a schematic diagram of a distribution example of the cyclone separators in the embodiment of the present invention;
fig. 3 is a schematic diagram illustrating another distribution of cyclone separators in an embodiment of the present invention.
The figure shows that: the device comprises a cyclone separator 1, a high-efficiency dust removal chamber 2, a partition plate 3, an upper clean gas chamber 4, a filter element 5, an ash bucket 6, a clean gas outlet 7, a gas bag 8, an electromagnetic pulse valve 9 and a blowing pipe 10.
Detailed Description
For further understanding of the technical solutions of the present invention, the following detailed description of the present invention is made with reference to the accompanying drawings and examples.
As shown in fig. 1, an embodiment of the present invention provides a novel combined type dust collector, which includes a cyclone separator 1, a high efficiency dust chamber 2 and a partition plate 3, wherein the cyclone separator 1 is disposed around the outer wall of the high efficiency dust chamber 2, the partition plate 3 is located at the upper portion of the high efficiency dust chamber 2, a hole is formed on the partition plate 3, and the partition plate 3 divides the high efficiency dust chamber 2 into an upper clean gas sub-chamber 4 and a lower dust sub-chamber; filter core 5 of high-efficient clean room 2 is connected on the hole of baffle 3, filter core 5 is located the sub-room that removes dust down, cyclone 1 and the sub-room wall sliding connection that removes dust of high-efficient clean room 2, cyclone 1's air outlet and the flue gas access connection of high-efficient clean room 2. Fig. 1 is only to list the main components, the connecting parts, valves etc. are not illustrated in the figure. Preferably, the filter element 5 is a bag filter or a cartridge filter. Of course, the filter element 5 can also have other structures. The upper clean gas sub-chamber 4 is provided with a clean gas outlet 7. The clean air outlet 7 is used for the cleaned air to flow out of the high-efficiency dust removal chamber 2.
In the composite dust remover of the embodiment, the external dust-containing gas enters the high-efficiency dust removing chamber 2 through the cyclone separator 1. In the cyclone separator 1, dust with larger particles in the dust-containing gas is discharged from a lower outlet of the cyclone separator 1, and gas with smaller particles in the dust is discharged from an upper gas outlet and enters the high-efficiency dust removal chamber 2. The partition 3 divides the high-efficiency dust removal chamber 2 into an upper clean gas sub-chamber 4 and a lower dust removal sub-chamber. The gas exiting the cyclone 1 enters the lower dust extraction sub-chamber of the high efficiency dust extraction chamber 2. In the lower dust removal subchamber, the gas containing smaller dust particles is filtered by the filter element 5 to become clean air, and the clean air passes through the filter element 5 and enters the upper clean gas subchamber 4.
The combined type dust remover of this embodiment, through 1 first grade filtration of cyclone, through 5 second grade filtrations of filter core, realized gaseous purification again. Through setting up two-stage filtration for gas purification is more thorough. The combined type dust remover of the embodiment has a compact structure, and can be arranged in a workshop to realize air purification.
In addition, in this embodiment, the number of bag-type dust collectors (or filter cartridge dust collectors), the number of cyclones, and the arrangement are not limited to those listed in this embodiment. And the gas inlet of the cyclone separator 1 is a dust-containing gas inlet. In this embodiment, the number of the filter elements 5, the number of the cyclone separators 1, and the arrangement mode are determined by specific working conditions and device environmental conditions. The preferred embodiment exemplifies two cyclone separator 1 arrangements: as shown in fig. 2, the cyclone separators 1 are arranged at two opposite sides of the high-efficiency dust removal chamber 2; as shown in fig. 3, the cyclone separator 1 is arranged at the peripheral side of the high-efficiency dust removing chamber 2. Through reasonable arrangement of the cyclone separator 1, the purification of air in a plant can be realized. If a production line is started up on one side of the plant, the cyclone 1 corresponding to that side can be started up. If all lines of the plant are started up, all cyclones 1 can be started up.
By adopting the structure, the two-stage filtering device is integrated into one device, and the space volume of the device is greatly reduced by arranging the shared ash bucket.
As a preferable example, the composite dust remover also comprises an ash hopper 6. The ash bucket 6 is positioned at the lower part of the high-efficiency dust removal chamber 2. The ash hopper 6 is connected with a dust outlet at the bottom of the cyclone separator 1. The ash bucket 6 is shared by the cyclone separator 1 and the high-efficiency dust removal chamber 2. The dust collecting device can conveniently collect dust, is convenient for daily management and maintenance, and reduces the occupied space of the device.
In the preferred embodiment, the dust-containing gas enters the cyclone separator 1 from the dust-containing gas inlet, firstly, in the dust removing process of the cyclone separator 1, the particulate matters larger than 15 micrometers are separated and enter the dust hopper 6, then the airflow with most of dust removed enters the high-efficiency dust removing chamber 2, after the dust removing effect of the filter element 5, the particulate matters smaller than 15 micrometers are captured, and the clean airflow enters the upper clean gas sub-chamber 4 and then is discharged from the clean gas outlet 7.
Preferably, the composite dust remover further comprises a pulse blowing ash removal device, wherein the pulse blowing ash removal device is positioned in the upper clean gas sub-chamber 4, and the pulse blowing ash removal device is positioned above the partition plate 3. Preferably, the pulse blowing ash removal device comprises an air bag 8, an electromagnetic pulse valve 9 and a blowing pipe 10, wherein an air outlet of the blowing pipe 10 is opposite to a bag opening of the filter element 5, and the electromagnetic pulse valve 9 is positioned in the blowing pipe 10.
In the high-efficiency dust removal chamber 2, a filter bag (or a filter cylinder) in the filter element 5 adopts compressed air to carry out pulse blowing dust removal. When the ash removal treatment of the filter element 5 is needed, the electromagnetic pulse valve 9 is started, and the gas in the gas bag 8 is ejected out of the injection pipe 10 in a pulse mode. Because the air outlet of the blowing pipe 10 is opposite to the bag opening of the filter element 5, the sprayed air forms pulse to the bag body of the filter element 5 and flows from the inner side of the filter element 5 to the outer side of the filter element 5. This achieves the ash removal treatment of the filter element 5. The dust detached from the filter element 5 falls into the dust hopper below.
Preferably, the filter element 5 of the high-efficiency dust removal chamber 2 is in threaded connection with the hole of the partition plate 3. The threaded connection is a detachable fixed connection and has the advantages of simple structure, reliable connection, convenient assembly and disassembly and the like. The bag filter or the filter cartridge can thus be exchanged quickly by itself or with respect to one another.
Preferably, the combined dust collector further comprises an automatic regulating valve, and the automatic regulating valve is arranged at a flue gas inlet of the cyclone separator 1. And adjusting the opening of the automatic regulating valve according to the requirement of the working condition, and changing the inlet component and the wind speed. Of course, the number of the cyclone separators used or closed can be determined according to the air volume requirement.
Preferably, the composite dust collector further comprises a poppet valve, and the poppet valve is arranged above the air channel of the hole of the partition plate 3. And the hole air passage is provided with a lift valve which can control the communication or cut-off state of the high-efficiency dust removal chamber and the air purification chamber.
The types of fumes produced are different due to the industrial industry. However, the filter element 5 has high requirements on flue gas, such as not too high temperature and humidity, not too large air volume and the like. However, the cyclone separator 1 has the characteristics of high temperature resistance and wear resistance. Therefore, the dusty gas firstly enters the cyclone separator 1, so that the requirements of different working conditions can be better met, the flow speed and the temperature of the dusty gas flow can be reduced, larger-particle-size particles can be separated, the workload of the filter element 5 is reduced, and the working requirements of the filter element 5 are met. Meanwhile, the cyclone separator can only remove large particles larger than 15 micrometers, the efficiency is low, but the filter element can remove fine particles smaller than 15 micrometers, and the dust removal efficiency is high, so that the filter elements 5 are sequentially arranged behind the cyclone separator 1, and the advantages can be complemented.
In the dust remover of the embodiment, the filter element 5 in the high-efficiency dust removing chamber 2 can be replaced, so that different dust removing requirements can be met; the position of the cyclone separator 1 is variable, so that different working environments and working condition requirements can be met; the ash bucket is shared, so that the space can be saved and the cleaning is convenient.
The present invention and its embodiments have been described above schematically, and the description is not limited thereto, and what is shown in the drawings is only one of the embodiments of the present invention, and the actual structure is not limited thereto. Therefore, if the person skilled in the art receives the teaching of the present invention, without departing from the inventive spirit of the present invention, the person skilled in the art should also design the similar structural modes and embodiments without creativity to the technical solution, and all shall fall within the protection scope of the present invention.
Claims (10)
1. A novel combined type dust remover adaptable to different working conditions is characterized by comprising a cyclone separator (1), a high-efficiency dust removing chamber (2) and a partition plate (3), wherein the cyclone separator (1) is arranged around the outer wall of the high-efficiency dust removing chamber (2), the partition plate (3) is positioned at the upper part of the high-efficiency dust removing chamber (2), holes are formed in the partition plate (3), and the partition plate (3) divides the high-efficiency dust removing chamber (2) into an upper clean gas sub-chamber (4) and a lower dust removing sub-chamber; filter core (5) of high-efficient clean room (2) are connected on the hole of baffle (3), filter core (5) are located the sub-room that removes dust down, cyclone (1) and the sub-room wall sliding connection that removes dust of the lower of high-efficient clean room (2), the air outlet of cyclone (1) and the flue gas access connection of high-efficient clean room (2).
2. The hybrid precipitator of claim 1, wherein the filter element (5) of the high efficiency precipitation chamber (2) is a bag precipitator or a cartridge precipitator.
3. The composite precipitator of claim 1 further comprising an ash hopper (6), said ash hopper (6) being located at a lower portion of the high efficiency precipitation chamber (2); the ash hopper (6) is connected with a dust outlet at the bottom of the cyclone separator (1).
4. A composite precipitator in accordance with claim 1, wherein said upper clean gas sub-chamber (4) is provided with a clean gas outlet (7).
5. The composite precipitator of claim 1 further comprising a pulse-jet ash removal device, said pulse-jet ash removal device being located in the upper clean gas sub-chamber (4), said pulse-jet ash removal device being located above the partition (3).
6. The combined dust collector of claim 5, wherein the pulse blowing ash removal device comprises an air bag (8), an electromagnetic pulse valve (9) and a blowing pipe (10), an air outlet of the blowing pipe (10) is opposite to a bag opening of the filter element (5), and the electromagnetic pulse valve (9) is positioned in the blowing pipe (10).
7. The combined precipitator according to claim 1, wherein the filter element (5) of the high efficiency precipitation chamber (2) is detachably connected to the holes of the partition plate (3).
8. The combined dust collector as claimed in claim 5, wherein the filter element (5) of the high efficiency dust collecting chamber (2) is in threaded connection with the holes of the partition plate (3).
9. A combined precipitator in accordance with claim 1, further comprising a self-regulating valve, said self-regulating valve being disposed at the flue gas inlet of the cyclone separator (1).
10. The composite precipitator in accordance with claim 1 further comprising poppet valves disposed above the orifice passages of the separator plate (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921705451.XU CN211189591U (en) | 2019-10-12 | 2019-10-12 | Novel combined type dust remover of adaptable different operating modes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921705451.XU CN211189591U (en) | 2019-10-12 | 2019-10-12 | Novel combined type dust remover of adaptable different operating modes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211189591U true CN211189591U (en) | 2020-08-07 |
Family
ID=71879356
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921705451.XU Active CN211189591U (en) | 2019-10-12 | 2019-10-12 | Novel combined type dust remover of adaptable different operating modes |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211189591U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113713542A (en) * | 2021-08-20 | 2021-11-30 | 太原重工股份有限公司 | Cyclone and filtering composite dust remover |
-
2019
- 2019-10-12 CN CN201921705451.XU patent/CN211189591U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113713542A (en) * | 2021-08-20 | 2021-11-30 | 太原重工股份有限公司 | Cyclone and filtering composite dust remover |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106861305B (en) | Internal filtering negative pressure type dust removing device and dust removing method thereof | |
| CN101972572A (en) | Compartment blowback dust remover | |
| CN201524509U (en) | Zincum powder dust collecting device | |
| CN107150000B (en) | Static powder spraying equipment with branch type air duct | |
| CN102698526B (en) | Internal filtering dust filtering equipment | |
| CN211189591U (en) | Novel combined type dust remover of adaptable different operating modes | |
| CN201855636U (en) | Blowback dust remover in branch room | |
| CN202638181U (en) | Inner-filtering type dust filter device | |
| CN208599380U (en) | A kind of metallic filtering film dust-extraction unit | |
| CN102755806B (en) | A kind of cleaner of parasitic type combination and operation method thereof | |
| CN111871610A (en) | Vertical electrostatic fabric filter | |
| CN1830520A (en) | Cylindrical self-suction glass fiber bag type dust separator | |
| CN208959515U (en) | A kind of polishing class dust pulse dust collector | |
| CN201008775Y (en) | Large wind quantity combined broaching filter cartridge precipitator | |
| CN212491999U (en) | Large-air-volume micro-dust collecting separator | |
| CN202666642U (en) | Parasitic combined dust collecting device | |
| CN212548711U (en) | Large-air-volume micro-dust collecting, separating and purifying system | |
| CN202036887U (en) | Dust collecting device for sintering pipe | |
| CN205252786U (en) | Filter element dust wiper | |
| CN212492179U (en) | Flue gas purification system | |
| CN203437007U (en) | W-shaped pre-de-dusting device | |
| CN208287691U (en) | A kind of cabinet type deduster enhancing wind pressure | |
| CN2626585Y (en) | Glass fiber bag-type dust collector | |
| CN100393390C (en) | Combined filter tube element pulse dust-collector | |
| CN219441132U (en) | Portable dust filters collection device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |