CN208990423U - The pulse dust collector of material production recycling raw material - Google Patents
The pulse dust collector of material production recycling raw material Download PDFInfo
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- CN208990423U CN208990423U CN201821748502.2U CN201821748502U CN208990423U CN 208990423 U CN208990423 U CN 208990423U CN 201821748502 U CN201821748502 U CN 201821748502U CN 208990423 U CN208990423 U CN 208990423U
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Abstract
The utility model relates to material production fields, and in particular to the pulse dust collector of material production recycling raw material.The pulse dust collector of material production recycling raw material, including pulse dust collector ontology, dust and gas entrance is arranged in the pulse dust collector ontology lower end, net gas outlet is arranged in upper end, dust export is arranged in bottom, recyclable device is connected before dust and gas entrance, the recyclable device includes cylinder, air inlet pipe, discharge gate, gas outlet, the air inlet pipe is inserted into cylinder from cylinder top and is extended downwardly, the air inlet pipe lower end is connected to bulb, bulb is cylindrical in shape outer diameter greater than air inlet pipe outside diameter, the gas outlet is higher than bulb and is opened in cylinder lateral wall, it is connected to the dust and gas entrance of pulse dust collector ontology, the discharge gate is set to cylinder body bottom, by discharge valve closure.The utility model can separate and recover the feed particles in dust and gas, realize the separation of feed particles, dust, net gas.
Description
Technical field
The utility model relates to material production fields, and in particular to the pulse dust collector of material production recycling raw material.
Background technique
It when just carrying out material generation, needs to be arranged deduster in production line many places and is dusted, column are as at elevator, stirred
At machine, and in dedusting, it is easy to suck short grained raw material, causes to waste.Pulse dust collector in the prior art can carry out
Dedusting and it is convenient for deashing, but still remains the above problem.
Utility model content
The purpose of this utility model is to provide materials to produce the pulse dust collector with recycling raw material, solves existing pulse
The raw material of fine particle is easily sucked wasting problem when in use by deduster.
In order to solve the above technical problems, the utility model uses following technical scheme:
The pulse dust collector of material production recycling raw material, including pulse dust collector ontology, the pulse dust collector sheet
Dust and gas entrance is arranged in body lower end, and net gas outlet is arranged in upper end, and bottom is arranged dust export, connects recyclable device before dust and gas entrance,
The recyclable device includes cylinder, air inlet pipe, discharge gate, gas outlet, and the air inlet pipe is inserted into cylinder simultaneously from cylinder top
It extends downwardly, the air inlet pipe lower end is connected to bulb, and bulb is cylindrical in shape outer diameter greater than air inlet pipe outside diameter, the outlet
Mouth is higher than bulb and is opened in cylinder lateral wall, is connected to the dust and gas entrance of pulse dust collector ontology, the discharge gate is set to
Cylinder body bottom, by discharge valve closure.
Dust and gas mixes the cylinder that short grained raw material first enters recyclable device from air inlet pipe, due to the outlet of recyclable device
Mouthful it is higher than bulb, therefore the dust and gas of carrying raw material particle rises from gas outlet after air inlet pipe, bulb and enters pulse dust removal
Device ontology, in the process, since bulb is cylindrical in shape outer diameter greater than air inlet pipe outside diameter, space increases when dust and gas rises, pressure
Reduce, the feed particles mixed fall therewith, and feed particles are discharged under the control of blow-off valve through discharge gate, realize recycling.And
Tiny dust, which continues gas is followed to enter pulse dust collector ontology, to be dusted, and the structure of pulse dust collector ontology has been existing
Technology is well known to those skilled in the art, and last net gas is exported from net gas to be discharged, and dust is discharged from dust export, realizes
The separation of dust, feed particles, net gas.
Preferably, setting spiral plate forms helical duct in the bulb.Dust and gas declines in bulb inside spin,
The hang time is promoted, part material particle is i.e. separable in the process, and separating effect is more preferably faster.
Preferably, filter opening is arranged on the spiral plate, filter opening size is depending on feedstock particle size, feed particles
Stopped, need to rotate and decline along spiral plate, and dust and gas then can realize the quick separating of feed particles by filter opening.
Preferably, partition is arranged in the pulse dust collector ontology, filter bag, setting above partition are connected to below partition
Injection tube is towards filter bag；Second injection tube is set in the cylinder of the recyclable device towards cylinder inboard wall, the injection tube
Gas bag is connected by electromagnetic impulse valve with the second injection tube.Electromagnetic impulse valve can spray the gas in gas bag through injection tube and second
Blowpipe blowout is respectively blown filter bag and cylinder inboard wall, respectively blows down the dust on being adsorbed on, feed particles, avoids accumulation stifled
Plug.
Preferably, second injection tube is arranged in a ring, it is evenly distributed with nozzle thereon, nozzle is towards in cylinder
Wall is blown more uniform strong.
Preferably, the cylinder lower part wall opens up vertical transparent window, vertical graduated scale is set by transparent window.
Feed particles in recyclable device can be observed by transparent window and accumulate situation, and graduated scale plays directive function, can be according to accumulation speed
Degree clears up feed particles in time.
Compared with prior art, the utility model can at least generate following one kind the utility model has the advantages that the utility model can be by dirt
Feed particles separation and recovery in gas, realizes the separation of feed particles, dust, net gas；The separation of the utility model feed particles
Rapidly and efficiently；The utility model respectively can be blown filter bag and cylinder inboard wall by injection tube and the second injection tube, will inhale respectively
The dust that is attached to, feed particles are blown down, and accumulated plugging is avoided；The second injection tube of the utility model is arranged in a ring, thereon
Even that nozzle is distributed with, nozzle is blown more uniform strong towards cylinder inboard wall；Transparent window and graduated scale is arranged in the utility model
Ruler can be observed feed particles in recyclable device by transparent window and accumulate situation, and graduated scale plays directive function, can be according to accumulation
Speed clears up feed particles in time.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain
The utility model is not used to limit the utility model.
Fig. 1 shows such material production structure of the pulse dust collector of recycling raw material, enumerates one below with reference to legend
A embodiment.
Embodiment 1:
The pulse dust collector of material production recycling raw material, including pulse dust collector ontology 1, the pulse dust collector sheet
Dust and gas entrance is arranged in 1 lower end of body, and net gas outlet is arranged in upper end, and bottom is arranged dust export, connects recyclable device before dust and gas entrance,
The recyclable device includes cylinder 2, air inlet pipe 3, discharge gate 4, gas outlet 5, and the air inlet pipe 3 is inserted into from 2 top of cylinder
Cylinder 2 simultaneously extends downwardly, and 3 lower end of air inlet pipe is connected to bulb 6, and bulb 6 is cylindrical in shape outer diameter greater than outside air inlet pipe 3
Diameter, the gas outlet 5 are higher than bulb 6 and are opened in 2 side wall of cylinder, be connected to the dust and gas entrance of pulse dust collector ontology 1, institute
The discharge gate 4 stated is set to 2 bottom of cylinder, is closed by blow-off valve 7.
Dust and gas mixes the cylinder 2 that short grained raw material first enters recyclable device from air inlet pipe 3, due to going out for recyclable device
Port 5 is higher than bulb 6, therefore the dust and gas of carrying raw material particle rises after air inlet pipe 3, bulb 6 from gas outlet 5 into arteries and veins
Body of deduster 1 is rushed, in the process, is greater than 3 outer diameter of air inlet pipe, space when dust and gas rises since bulb 6 is cylindrical in shape outer diameter
Increasing, pressure reduces, and the feed particles mixed fall therewith, and feed particles are discharged under the control of blow-off valve 7 through discharge gate 4,
Realize recycling.And tiny dust continues gas is followed to enter pulse dust collector ontology 1 and is dusted, pulse dust collector ontology 1
Structure be the prior art, be well known to those skilled in the art.Last net gas is exported from the net gas of pulse dust collector ontology 1
Discharge, dust are discharged from dust export, realize the separation of dust, feed particles, net gas.
Embodiment 2:
The pulse dust collector of material production recycling raw material, including pulse dust collector ontology 1, the pulse dust collector sheet
Dust and gas entrance is arranged in 1 lower end of body, and net gas outlet is arranged in upper end, and bottom is arranged dust export, connects recyclable device before dust and gas entrance,
The recyclable device includes cylinder 2, air inlet pipe 3, discharge gate 4, gas outlet 5, and the air inlet pipe 3 is inserted into from 2 top of cylinder
Cylinder 2 simultaneously extends downwardly, and 3 lower end of air inlet pipe is connected to bulb 6, and bulb 6 is cylindrical in shape outer diameter greater than outside air inlet pipe 3
Diameter, the gas outlet 5 is higher than bulb 6 and is opened in 2 side wall of cylinder, is connected to the dust and gas entrance of pulse dust collector ontology 1, swollen
Setting spiral plate 8 forms helical duct in big portion 6.The discharge gate 4 is set to 2 bottom of cylinder, is closed by blow-off valve 7.
Dust and gas mixes the cylinder 2 that short grained raw material first enters recyclable device from air inlet pipe 3, dust and gas by air inlet pipe 3,
Bulb 6, dust and gas decline in 6 inside spin of bulb, promote the hang time, and part material particle is i.e. separable in the process,
Separating effect is more preferably faster.Due to recyclable device gas outlet 5 be higher than bulb 6, dust and gas pass through bulb 6 after rise from
Gas outlet 5 enters pulse dust collector ontology 1, in the process, since bulb 6 is cylindrical in shape outer diameter greater than 3 outer diameter of air inlet pipe, dirt
Space increases when gas rises, and pressure reduces, and the feed particles mixed fall therewith, and feed particles are through discharge gate 4 in blow-off valve 7
The lower discharge of control, realizes recycling.And tiny dust continues gas is followed to enter pulse dust collector ontology 1 and is dusted, pulse
The structure of body of deduster 1 has been the prior art, is well known to those skilled in the art.Last net gas is from pulse dust collector ontology
1 net gas exports discharge, and dust is discharged from dust export, realizes the separation of dust, feed particles, net gas.
Embodiment 3:
The pulse dust collector of material production recycling raw material, including pulse dust collector ontology 1, the pulse dust collector sheet
Dust and gas entrance is arranged in 1 lower end of body, and net gas outlet is arranged in upper end, and bottom is arranged dust export, connects recyclable device before dust and gas entrance,
The recyclable device includes cylinder 2, air inlet pipe 3, discharge gate 4, gas outlet 5, and the air inlet pipe 3 is inserted into from 2 top of cylinder
Cylinder 2 simultaneously extends downwardly, and 3 lower end of air inlet pipe is connected to bulb 6, and bulb 6 is cylindrical in shape outer diameter greater than outside air inlet pipe 3
Diameter, the gas outlet 5 is higher than bulb 6 and is opened in 2 side wall of cylinder, is connected to the dust and gas entrance of pulse dust collector ontology 1, swollen
Setting spiral plate 8 forms helical duct in big portion 6.Filter opening is set on spiral plate 8, filter opening size according to feedstock particle size and
Fixed, feed particles are stopped, and need to be rotated and be declined along spiral plate 8, and dust and gas then can realize feed particles by filter opening
Quick separating.The discharge gate 4 is set to 2 bottom of cylinder, is closed by blow-off valve 7.
Dust and gas mixes the cylinder 2 that short grained raw material first enters recyclable device from air inlet pipe 3, dust and gas by air inlet pipe 3,
Bulb 6, dust and gas decline in 6 inside spin of bulb, promote the hang time, and part material particle is i.e. separable in the process,
Separating effect is more preferably faster.Due to recyclable device gas outlet 5 be higher than bulb 6, dust and gas pass through bulb 6 after rise from
Gas outlet 5 enters pulse dust collector ontology 1, in the process, since bulb 6 is cylindrical in shape outer diameter greater than 3 outer diameter of air inlet pipe, dirt
Space increases when gas rises, and pressure reduces, and the feed particles mixed fall therewith, and feed particles are through discharge gate 4 in blow-off valve 7
The lower discharge of control, realizes recycling.And tiny dust continues gas is followed to enter pulse dust collector ontology 1 and is dusted, pulse
The structure of body of deduster 1 has been the prior art, is well known to those skilled in the art.Last net gas is from pulse dust collector ontology
1 net gas exports discharge, and dust is discharged from dust export, realizes the separation of dust, feed particles, net gas.
Embodiment 4:
The pulse dust collector of material production recycling raw material, including pulse dust collector ontology 1, the pulse dust collector sheet
Dust and gas entrance is arranged in 1 lower end of body, and net gas outlet is arranged in upper end, and bottom is arranged dust export, connects recyclable device before dust and gas entrance,
The recyclable device includes cylinder 2, air inlet pipe 3, discharge gate 4, gas outlet 5, and the air inlet pipe 3 is inserted into from 2 top of cylinder
Cylinder 2 simultaneously extends downwardly, and 3 lower end of air inlet pipe is connected to bulb 6, and bulb 6 is cylindrical in shape outer diameter greater than outside air inlet pipe 3
Diameter, the gas outlet 5 is higher than bulb 6 and is opened in 2 side wall of cylinder, is connected to the dust and gas entrance of pulse dust collector ontology 1, swollen
Setting spiral plate 8 forms helical duct in big portion 6.Filter opening is set on spiral plate 8, filter opening size according to feedstock particle size and
Fixed, feed particles are stopped, and need to be rotated and be declined along spiral plate 8, and dust and gas then can realize feed particles by filter opening
Quick separating.The discharge gate 4 is set to 2 bottom of cylinder, is closed by blow-off valve 7.
Dust and gas mixes the cylinder 2 that short grained raw material first enters recyclable device from air inlet pipe 3, dust and gas by air inlet pipe 3,
Bulb 6, dust and gas decline in 6 inside spin of bulb, promote the hang time, and part material particle is i.e. separable in the process,
Separating effect is more preferably faster.Due to recyclable device gas outlet 5 be higher than bulb 6, dust and gas pass through bulb 6 after rise from
Gas outlet 5 enters pulse dust collector ontology 1, in the process, since bulb 6 is cylindrical in shape outer diameter greater than 3 outer diameter of air inlet pipe, dirt
Space increases when gas rises, and pressure reduces, and the feed particles mixed fall therewith, and feed particles are through discharge gate 4 in blow-off valve 7
The lower discharge of control, realizes recycling.And tiny dust continues gas is followed to enter pulse dust collector ontology 1 and is dusted, pulse
The structure of body of deduster 1 has been the prior art, is well known to those skilled in the art.Last net gas is from pulse dust collector ontology
1 net gas exports discharge, and dust is discharged from dust export, realizes the separation of dust, feed particles, net gas.
Partition 9 is set in the pulse dust collector ontology 1, filter bag 10 is connected to below partition 9, spray is set above partition 9
Blowpipe 11 is towards filter bag 10；The second injection tube 12 of setting is described towards 2 inner wall of cylinder in the cylinder 2 of the recyclable device
Injection tube 11 and the second injection tube 12 pass through the connection gas bag 14 of electromagnetic impulse valve 13.Electromagnetic impulse valve 13 can be by the gas in gas bag 14
Body is respectively blown filter bag 10 and 2 inner wall of cylinder through injection tube 11 and the blowout of the second injection tube 12, respectively by the ash on being adsorbed on
Dirt, feed particles are blown down, and accumulated plugging is avoided.
Embodiment 5:
The pulse dust collector of material production recycling raw material, including pulse dust collector ontology 1, the pulse dust collector sheet
Dust and gas entrance is arranged in 1 lower end of body, and net gas outlet is arranged in upper end, and bottom is arranged dust export, connects recyclable device before dust and gas entrance,
The recyclable device includes cylinder 2, air inlet pipe 3, discharge gate 4, gas outlet 5, and the air inlet pipe 3 is inserted into from 2 top of cylinder
Cylinder 2 simultaneously extends downwardly, and 3 lower end of air inlet pipe is connected to bulb 6, and bulb 6 is cylindrical in shape outer diameter greater than outside air inlet pipe 3
Diameter, the gas outlet 5 is higher than bulb 6 and is opened in 2 side wall of cylinder, is connected to the dust and gas entrance of pulse dust collector ontology 1, swollen
Setting spiral plate 8 forms helical duct in big portion 6.Filter opening is set on spiral plate 8, filter opening size according to feedstock particle size and
Fixed, feed particles are stopped, and need to be rotated and be declined along spiral plate 8, and dust and gas then can realize feed particles by filter opening
Quick separating.The discharge gate 4 is set to 2 bottom of cylinder, is closed by blow-off valve 7.
Dust and gas mixes the cylinder 2 that short grained raw material first enters recyclable device from air inlet pipe 3, dust and gas by air inlet pipe 3,
Bulb 6, dust and gas decline in 6 inside spin of bulb, promote the hang time, and part material particle is i.e. separable in the process,
Separating effect is more preferably faster.Due to recyclable device gas outlet 5 be higher than bulb 6, dust and gas pass through bulb 6 after rise from
Gas outlet 5 enters pulse dust collector ontology 1, in the process, since bulb 6 is cylindrical in shape outer diameter greater than 3 outer diameter of air inlet pipe, dirt
Space increases when gas rises, and pressure reduces, and the feed particles mixed fall therewith, and feed particles are through discharge gate 4 in blow-off valve 7
The lower discharge of control, realizes recycling.And tiny dust continues gas is followed to enter pulse dust collector ontology 1 and is dusted, pulse
The structure of body of deduster 1 has been the prior art, is well known to those skilled in the art.Last net gas is from pulse dust collector ontology
1 net gas exports discharge, and dust is discharged from dust export, realizes the separation of dust, feed particles, net gas.
Partition 9 is set in the pulse dust collector ontology 1, filter bag 10 is connected to below partition 9, spray is set above partition 9
Blowpipe 11 is towards filter bag 10；The second injection tube 12 of setting is described towards 2 inner wall of cylinder in the cylinder 2 of the recyclable device
Injection tube 11 and the second injection tube 12 pass through the connection gas bag 14 of electromagnetic impulse valve 13.Electromagnetic impulse valve 13 can be by the gas in gas bag 14
Body is respectively blown filter bag 10 and 2 inner wall of cylinder through injection tube 11 and the blowout of the second injection tube 12, respectively by the ash on being adsorbed on
Dirt, feed particles are blown down, and accumulated plugging is avoided.Second injection tube 12 is arranged in a ring, is evenly distributed with nozzle, nozzle court thereon
To 2 inner wall of cylinder, it is blown more uniform strong.
Optimum embodiment:
The pulse dust collector of material production recycling raw material, including pulse dust collector ontology 1, the pulse dust collector sheet
Dust and gas entrance is arranged in 1 lower end of body, and net gas outlet is arranged in upper end, and bottom is arranged dust export, connects recyclable device before dust and gas entrance,
The recyclable device includes cylinder 2, air inlet pipe 3, discharge gate 4, gas outlet 5, and the air inlet pipe 3 is inserted into from 2 top of cylinder
Cylinder 2 simultaneously extends downwardly, and 3 lower end of air inlet pipe is connected to bulb 6, and bulb 6 is cylindrical in shape outer diameter greater than outside air inlet pipe 3
Diameter, the gas outlet 5 is higher than bulb 6 and is opened in 2 side wall of cylinder, is connected to the dust and gas entrance of pulse dust collector ontology 1, swollen
Setting spiral plate 8 forms helical duct in big portion 6.Filter opening is set on spiral plate 8, filter opening size according to feedstock particle size and
Fixed, feed particles are stopped, and need to be rotated and be declined along spiral plate 8, and dust and gas then can realize feed particles by filter opening
Quick separating.The discharge gate 4 is set to 2 bottom of cylinder, is closed by blow-off valve 7.2 lower part wall of cylinder opens up vertically
Vertical graduated scale is arranged by transparent window 15 in transparent window 15.Raw material in recyclable device can be observed by transparent window 15
Grain accumulation situation, graduated scale play directive function, can clear up in time feed particles according to stackeding speed.
Dust and gas mixes the cylinder 2 that short grained raw material first enters recyclable device from air inlet pipe 3, dust and gas by air inlet pipe 3,
Bulb 6, dust and gas decline in 6 inside spin of bulb, promote the hang time, and part material particle is i.e. separable in the process,
Separating effect is more preferably faster.Due to recyclable device gas outlet 5 be higher than bulb 6, dust and gas pass through bulb 6 after rise from
Gas outlet 5 enters pulse dust collector ontology 1, in the process, since bulb 6 is cylindrical in shape outer diameter greater than 3 outer diameter of air inlet pipe, dirt
Space increases when gas rises, and pressure reduces, and the feed particles mixed fall therewith, and feed particles are through discharge gate 4 in blow-off valve 7
The lower discharge of control, realizes recycling.And tiny dust continues gas is followed to enter pulse dust collector ontology 1 and is dusted, pulse
The structure of body of deduster 1 has been the prior art, is well known to those skilled in the art.Last net gas is from pulse dust collector ontology
1 net gas exports discharge, and dust is discharged from dust export, realizes the separation of dust, feed particles, net gas.
Partition 9 is set in the pulse dust collector ontology 1, filter bag 10 is connected to below partition 9, spray is set above partition 9
Blowpipe 11 is towards filter bag 10；The second injection tube 12 of setting is described towards 2 inner wall of cylinder in the cylinder 2 of the recyclable device
Injection tube 11 and the second injection tube 12 pass through the connection gas bag 14 of electromagnetic impulse valve 13.Electromagnetic impulse valve 13 can be by the gas in gas bag 14
Body is respectively blown filter bag 10 and 2 inner wall of cylinder through injection tube 11 and the blowout of the second injection tube 12, respectively by the ash on being adsorbed on
Dirt, feed particles are blown down, and accumulated plugging is avoided.Second injection tube 12 is arranged in a ring, is evenly distributed with nozzle, nozzle court thereon
To 2 inner wall of cylinder, it is blown more uniform strong.
Multiple explanatory embodiments spoken of in the present specification refer to the specific structure packet for combining embodiment description
It includes at least one embodiment of the application generality description.It is not certain that statement of the same race, which occur, in multiple places in the description
Refer to the same embodiment.Furthermore, it is understood that is advocated is to combine when describing a structure in conjunction with any one embodiment
Other embodiments realize that this structure is fallen in the scope of the utility model.
Claims (6)
1. the pulse dust collector of material production recycling raw material, including pulse dust collector ontology (1), the pulse dust collector sheet
Dust and gas entrance is arranged in body (1) lower end, and net gas outlet is arranged in upper end, and dust export is arranged in bottom, it is characterised in that: before dust and gas entrance
Connect recyclable device, the recyclable device includes cylinder (2), air inlet pipe (3), discharge gate (4), gas outlet (5), it is described into
Tracheae (3) is from cylinder (2) top insertion cylinder (2) and extends downwardly, and the air inlet pipe (3) lower end is connected to bulb (6), swollen
Big portion (6) is cylindrical in shape outer diameter greater than air inlet pipe (3) outer diameter, and the gas outlet (5) are higher than bulb (6) and are opened in cylinder (2)
Side wall is connected to the dust and gas entrance of pulse dust collector ontology (1), and the discharge gate (4) is set to cylinder (2) bottom, by arranging
Expect valve (7) closing.
2. the pulse dust collector of material production recycling raw material according to claim 1, it is characterised in that: described is swollen
Setting spiral plate (8) forms helical duct in big portion (6).
3. the pulse dust collector of material production recycling raw material according to claim 2, it is characterised in that: the spiral
Filter opening is arranged on (8) in plate.
4. the pulse dust collector of material production recycling raw material according to claim 1, it is characterised in that: the pulse
Partition (9) are set in body of deduster (1), are connected to filter bag (10) below partition (9), injection tube (11) are set above partition (9)
Towards filter bag (10)；Setting the second injection tube (12) is described towards cylinder (2) inner wall in the cylinder (2) of the recyclable device
Injection tube (11) and the second injection tube (12) by electromagnetic impulse valve (13) connection gas bag (14).
5. the pulse dust collector of material production recycling raw material according to claim 4, it is characterised in that: described second
Injection tube (12) is arranged in a ring, is evenly distributed with nozzle thereon, and nozzle is towards cylinder (2) inner wall.
6. the pulse dust collector of material production recycling raw material according to claim 1, it is characterised in that: the cylinder
(2) lower part wall opens up vertical transparent window (15), and vertical graduated scale is arranged by transparent window (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201821748502.2U CN208990423U (en) | 2018-10-26 | 2018-10-26 | The pulse dust collector of material production recycling raw material |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201821748502.2U CN208990423U (en) | 2018-10-26 | 2018-10-26 | The pulse dust collector of material production recycling raw material |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115581975A (en) * | 2022-12-08 | 2023-01-10 | 协鑫高科纳米新材料(徐州)有限公司 | Dust remover is retrieved with tiny particle to fumed silica production |
-
2018
- 2018-10-26 CN CN201821748502.2U patent/CN208990423U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115581975A (en) * | 2022-12-08 | 2023-01-10 | 协鑫高科纳米新材料(徐州)有限公司 | Dust remover is retrieved with tiny particle to fumed silica production |
| CN115581975B (en) * | 2022-12-08 | 2023-03-10 | 协鑫高科纳米新材料(徐州)有限公司 | Dust remover is retrieved with tiny particle to fumed silica production |
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