CN219631527U - Continuous vibration crushing classifier capable of classifying online - Google Patents
Continuous vibration crushing classifier capable of classifying online Download PDFInfo
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- CN219631527U CN219631527U CN202221526352.7U CN202221526352U CN219631527U CN 219631527 U CN219631527 U CN 219631527U CN 202221526352 U CN202221526352 U CN 202221526352U CN 219631527 U CN219631527 U CN 219631527U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
The utility model discloses a continuous vibration crushing classifier capable of classifying online, which belongs to the technical field of crushers and comprises a vibration crusher, wherein a feed back pipeline, a classifying chamber and a discharge bin are sequentially arranged at the top end of the vibration crusher, a feed hopper is arranged on the feed back pipeline, a classifying assembly is rotationally connected in the classifying chamber, an air inducing assembly is arranged at the outlet end of the discharge bin, a discharge pipeline is arranged at the bottom end of the vibration crusher, and one end of the discharge pipeline, which is far away from the vibration crusher, extends into the classifying chamber.
Description
Technical Field
The utility model belongs to the technical field of crushers, and particularly relates to a continuous vibration crushing classifier capable of classifying on line.
Background
Compared with a rotary drum ball mill, the vibration pulverizer has the main performance characteristics that the filling rate of grinding media in a cylinder is high, the grinding strength is high, the processing capacity of the same volume is high, and the pulverizing efficiency is high; and the structure is simpler, and the operation is flexible and convenient. In addition, various materials including high hardness materials and products of various fineness including ultrafine powder products having an average particle diameter of 1 μm or even less than 1 μm can be processed by adjusting the amplitude, frequency, type, ratio and diameter of the medium of the vibration.
The vibration pulverizer drives the eccentric shaft vibration exciter to rotate at a high speed by the motor through the universal transmission coupler, so that exciting force is generated to enable the vibration-taking component (cylinder component) to continuously vibrate at high frequency and low amplitude on the elastic supporting device, and materials in the cylinder are subjected to the actions of strong impact, friction, shearing and the like of the grinding body; meanwhile, due to the rotation and relative movement of the grinding body, frequent grinding action is generated on the particles of the material, so that the elastic modulus of the material is reduced, defects and microcrack expansion are generated, and the purpose of crushing the material is achieved. In this process, the feed rate directly affects the processed particle size of the vibratory pulverizer, typically by manual control, and when the feed rate is reduced, finer particles can be produced because more energy is available for each particle to accelerate for pulverization, but in this case the production efficiency is very low, and when the feed rate is increased, its energy cannot be supplied for each particle to accelerate for pulverization, and the acceptable particles are mixed with the unacceptable particles, and at the same time discharged from the vibratory pulverizer, resulting in unacceptable material pulverization.
Disclosure of Invention
The utility model aims to: a continuous vibration crushing classifier capable of classifying on line is provided to solve the above problems existing in the prior art.
The technical scheme is as follows: the utility model provides a but online hierarchical continuous vibration smash grader, includes vibration pulverizer, vibration pulverizer's top is equipped with feed back pipeline, classifying chamber and play feed bin in proper order, be equipped with the feeder hopper on the feed back pipeline, classifying chamber inside rotates and is connected with classifying assembly, the exit end of play feed bin is equipped with induced air subassembly, vibration pulverizer's bottom is equipped with ejection of compact pipeline, vibration pulverizer's one end is kept away from to ejection of compact pipeline extends to classifying chamber inside.
Through adopting above-mentioned technical scheme, add vibration pulverizer from the feeder hopper with the material homoenergetic and smash into the powder particle, at this moment through the inside air of induced air subassembly extraction classifying chamber, this moment the inside negative pressure state that is in of classifying chamber for discharge pipeline inhales the powder particle in the classifying chamber, carry out the classification through classifying assembly this moment to the powder particle, qualified powder particle is discharged from the discharge bin and is collected, unqualified powder particle is got back to vibration pulverizer again along classifying chamber inner wall and smashes, and then prevent to control the material crushing granularity by manual control and lead to the material crushing unqualified, improved production efficiency simultaneously.
Preferably, a return control pipeline is arranged on the return pipeline, the connecting end of the return control pipeline and the return pipeline is higher than the connecting end of the feeding hopper and the return pipeline, the return control pipeline is arranged on the return pipeline at a cutting-in angle alpha, and the cutting-in angle alpha of the return control pipeline is 50-60 degrees.
Preferably, the classifying assembly comprises a classifying motor arranged at the top end of the discharging bin, a transmission shaft is coaxially arranged at the output end of the classifying motor, one end, far away from the classifying motor, of the transmission shaft penetrates through the discharging bin to extend into the classifying chamber, a classifying wheel is coaxially arranged at the outer side of the extending end of the transmission shaft, and the classifying wheel and the classifying chamber are in the same axis.
Preferably, after the discharging pipeline extends to the inside of the classifying chamber, the discharging pipeline vertically rotates upwards by an angle of 90 degrees, one end of the discharging pipeline, which is positioned in the classifying chamber, is provided with a discharging hopper, and the discharging hopper is positioned under the classifying wheel and is in the same axle center with the classifying wheel.
Preferably, an angle formed between the outer ring of the classifying wheel and the inner wall of the classifying chamber is beta, and beta is 10-15 degrees.
Preferably, the outlet end of the discharging bin is sequentially provided with a collecting pipeline and a collecting chamber, a spiral guide pipeline is arranged outside the collecting chamber, the a end of the guide pipeline is communicated with the collecting pipeline, the b end of the guide pipeline is communicated with the collecting chamber, the top end inside the collecting chamber is vertically provided with an air inlet pipeline, the bottom end of the air inlet pipeline is lower than the b end of the guide pipeline, the top end of the air inlet pipeline extends out of the collecting chamber and the extending end is provided with a connecting pipeline, one end, far away from the air inlet pipeline, of the connecting pipeline is provided with a gas-solid separation assembly, and the bottom end of the collecting chamber is provided with a first charging basket.
Preferably, the gas-solid separation assembly comprises a separation chamber communicated with the connecting pipeline, a plurality of cloth bags for filtering powder particles are vertically arranged in the separation chamber, a pulse device is arranged in the separation chamber, the output ends of the pulse device are respectively positioned in the cloth bags, a second charging basket is arranged at the bottom end of the separation chamber, and the separation chamber is communicated with the air inducing assembly.
Preferably, the induced air subassembly includes the induced air pipeline with the separation chamber switch-on, the induced air pipeline is kept away from the one end of separation chamber and is equipped with the draught fan, the junction of draught fan and induced air pipeline is equipped with exhaust duct, the switch-on end of induced air pipeline and separation chamber is higher than the switch-on end of connecting tube and separation chamber.
Preferably, the bottom end of the vibration pulverizer is provided with a cold water joint, and the cold water joint is positioned in an interlayer at the bottom end of the vibration pulverizer.
Preferably, one end of the discharging pipeline, which is close to the vibration pulverizer, is provided with a discharging control pipeline, the discharging control pipeline is arranged on the discharging pipeline at a cutting-in angle gamma, and the cutting-in angle gamma of the discharging control pipeline is 50-60 degrees.
In summary, the utility model has the following beneficial effects:
the material is added into the vibration pulverizer from the feeder hopper at uniform speed and crushed into powder particles, air in the classifying chamber is extracted through the induced air component at the moment, the interior of the classifying chamber is in a negative pressure state at the moment, the powder particles are sucked into the classifying chamber through the discharging pipeline, the qualified powder particles are discharged from the discharging bin and collected through the classifying component, the unqualified powder particles return to the vibration pulverizer again along the inner wall of the classifying chamber for crushing, and further, the material crushing granularity is prevented from being controlled by manually controlling the feeding amount, so that the material crushing is unqualified, and meanwhile, the production efficiency is improved.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
FIG. 2 is an enlarged view of A of FIG. 1 in accordance with the present utility model;
FIG. 3 is an enlarged view of B of FIG. 1 in accordance with the present utility model;
FIG. 4 is a partial view of the present utility model;
fig. 5 is an enlarged view of C in fig. 1 according to the present utility model.
The reference numerals are: 1. a vibration pulverizer; 11. a feed back pipeline; 12. a feed hopper; 13. a cold water joint; 2. a discharge pipe; 21. discharging a hopper; 3. a classifying chamber; 31. a feed back control pipeline; 32. discharging the material bin; 4. a classification wheel; 41. a transmission shaft; 42. a classifying motor; 5. a collection chamber; 51. a diversion pipeline; 52. an air inlet pipeline; 53. a collection pipe; 54. a first barrel; 6. a separation chamber; 61. a second barrel; 62. a cloth bag; 63. a pulse device; 64. a connecting pipe; 7. an induced draft fan; 71. an induced draft pipe; 72. an exhaust duct; 8. and a discharging control pipeline.
Detailed Description
In the following description, numerous specific details are set forth in order to provide a more thorough understanding of the present utility model. It will be apparent, however, to one skilled in the art that the utility model may be practiced without one or more of these details. In other instances, well-known features have not been described in detail in order to avoid obscuring the utility model.
The utility model provides a but online hierarchical continuous vibration smash grader, as in fig. 1, including vibration pulverizer 1, vibration pulverizer 1's top is vertical to be equipped with feed back pipeline 11, vibration pulverizer 1's one end is kept away from to feed back pipeline 11 is vertical to be equipped with classifying chamber 3, classifying chamber 3 top is equipped with out feed bin 32, vibration pulverizer 1, feed back pipeline 11, classifying chamber 3 and ejection of compact storehouse 32 switch on in proper order, be equipped with the feeder hopper 12 that is arranged in adding vibration pulverizer 1 with the material on the feed back pipeline 11, classifying chamber 3 inside rotates and is connected with classifying assembly, ejection of compact storehouse 32's exit end is equipped with induced air subassembly, vibration pulverizer 1's bottom is equipped with ejection of compact pipeline 2, ejection of compact pipeline 2 is put through with vibration pulverizer 1, vibration pulverizer 1's one end is kept away from to ejection of compact pipeline 2 extends to classifying chamber 3 inside.
As shown in figure 1, the material is added into the vibration pulverizer 1 through the feed hopper 12 at uniform speed, the material is pulverized into powder particles by the vibration pulverizer 1 at this time, then the air in the classifying chamber 3 is extracted through the induced air component, at this time, the inside of the classifying chamber 3 is in a negative pressure state, the powder particles are sucked into the classifying chamber 3 by the discharging pipeline 2, at this time, the powder particles are classified by the classifying component, qualified materials enter the classifying component, are discharged and collected by the discharging bin 32, and unqualified powder particles fall into the material return pipeline 11 along the inner wall of the classifying chamber 3 and then return to the vibration pulverizer 1 again for pulverization, so that the material pulverization disqualification caused by controlling the material pulverization granularity by manual control of the feeding amount is prevented, and meanwhile, the production efficiency is improved.
As shown in fig. 4, a return control pipe 31 is disposed on the return pipe 11, the connection end of the return control pipe 31 and the return pipe 11 is higher than the connection end of the feed hopper 12 and the return pipe 11, the return control pipe 31 is disposed on the return pipe 11 at a cutting angle α, the cutting angle α of the return control pipe 31 is 50 ° to 60 °, and the angle is set so that atmospheric pressure tangentially enters the return pipe 11, and then the negative pressure inside the classifying chamber 3 is isolated, so that unqualified powder particles can return to the vibratory pulverizer 1 for re-pulverization, and meanwhile, feeding is also facilitated.
As shown in fig. 1, the classifying assembly comprises a classifying motor 42, the classifying motor 42 is arranged at the top end of the discharging bin 32, the output end of the classifying motor 42 is provided with a transmission shaft 41, the transmission shaft 41 and the output end of the classifying motor 42 are in the same axis, one end of the transmission shaft 41 away from the classifying motor 42 penetrates through the discharging bin 32 and extends to the inside of the classifying chamber 3, a classifying wheel 4 is arranged at the outer side of the extending end of the transmission shaft 41, the classifying wheel 4, the transmission shaft 41 and the classifying chamber 3 are in the same axis, the classifying motor 42 drives the transmission shaft 41 to rotate, at the moment, the rotating shaft drives the classifying wheel 4 to rotate, the classifying wheel 4 drives particles in the classifying chamber 3 to rotate to generate centrifugal force when the air guiding assembly extracts air in the classifying chamber 3, so that the particles in the classifying chamber 3 generate centripetal force towards the center of the classifying wheel 4, the qualified particles are moved towards the center of the classifying wheel 4 because the qualified particles have small particle sizes, the received centrifugal force is smaller than the centripetal force, the qualified particles are discharged and collected from the discharging bin 32 under the action of guiding air, and the unqualified particles have the particle sizes larger than the centripetal force, the received force, and are thrown towards the inner wall of the classifying chamber 3 by the classifying wheel 4 and fall down by the classifying wheel 4 when the unqualified particles are returned to the pulverizer 1.
As shown in fig. 1, after the discharge pipeline 2 extends into the classifying chamber 3, the discharge pipeline 2 vertically rotates upwards by an angle of 90 degrees, one end of the discharge pipeline 2, which is positioned in the classifying chamber 3, is provided with a discharge hopper 21, the discharge hopper 21 is positioned under the classifying wheel 4, the discharge hopper 21 and the classifying wheel 4 are in the same axle center, and the angle is set, when the discharge pipeline 2 sucks powder particles into the classifying chamber 3, the powder particles are directly classified by the classifying wheel 4, and meanwhile, the contact surface between the powder particles and the classifying wheel 4 is improved by the discharge hopper 21, so that the classifying efficiency is improved.
As shown in fig. 2, the angle formed between the outer ring of the classifying wheel 4 and the inner wall of the classifying chamber 3 is beta, and the beta is 10-15 degrees, so that unqualified powder particles can return to the vibrating pulverizer 1 for re-pulverizing after one-time rebound between the outer ring of the classifying wheel 4 and the inner wall of the classifying chamber 3, and the feed back speed is improved.
As shown in fig. 1, the outlet end of the discharging bin 32 is sequentially provided with a collecting pipeline 53 and a collecting chamber 5, the collecting pipeline 53 is communicated with the collecting chamber 5, a spiral guide pipeline 51 is arranged at the outer side of the collecting chamber 5, the a end of the guide pipeline 51 is communicated with the collecting pipeline 53, the b end of the guide pipeline 51 is communicated with the collecting chamber 5, an air inlet pipeline 52 is vertically arranged at the top end of the inner part of the collecting chamber 5, the bottom end of the air inlet pipeline 52 is lower than the b end of the guide pipeline 51, the top end of the air inlet pipeline 52 extends out of the collecting chamber 5, the extending end of the air inlet pipeline 52 is provided with a connecting pipeline 64, the connecting pipeline 64 is communicated with the air inlet pipeline 52, one end of the connecting pipeline 64 far away from the air inlet pipeline 52 is provided with a gas-solid separation assembly, the bottom end of the collecting chamber 5 is provided with a first charging basket 54, air in the collecting chamber 5 is extracted through an induced air assembly, negative pressure is generated in the collecting chamber 5 at this moment, qualified powder particles are sucked into the collecting chamber 5 through the guide pipeline 51, and flow into the collecting chamber 5, after passing through the guide pipeline 51, air flow flows along the inner wall of the collecting chamber 5 in a spiral shape, the conical end of the collecting chamber 5, qualified powder particles flow is enabled to rotate to generate centrifugal force, the qualified powder particles flow and then fall into the collecting basket 54 by gravity through the collecting basket 54.
As shown in fig. 1, the gas-solid separation assembly comprises a separation chamber 6, the separation chamber 6 is communicated with a connecting pipeline 64, a plurality of cloth bags 62 for filtering powder particles are vertically arranged in the separation chamber 6, a pulse device 63 is arranged in the separation chamber 6, the output ends of the pulse devices 63 are respectively positioned in the cloth bags 62, a second charging basket 61 is arranged at the bottom end of the separation chamber 6, the separation chamber 6 is communicated with an induced air assembly, a small amount of qualified powder particles still can be discharged out of the collection chamber 5 under the action of the induced air, at the moment, air in the separation chamber 6 is extracted through the induced air assembly, at the moment, negative pressure is generated in the separation chamber 6, so that the connecting pipeline 64 sucks a small amount of qualified powder particles into the separation chamber 6, the qualified powder particles can be adsorbed on the cloth bags 62 when entering the classification chamber 3, so that the qualified powder particles are completely separated from air flow, and at the moment, the qualified powder particles adsorbed on the cloth bags 62 are washed into the second charging basket 61 through the pulse device 63 when a certain amount of qualified powder particles accumulate on the cloth bags 62.
As shown in fig. 1, the induced air assembly comprises an induced air pipeline 71, the induced air pipeline 71 is communicated with the classifying chamber 3, an induced draft fan 7 is arranged at one end of the induced air pipeline 71 far away from the separating chamber 6, an exhaust pipeline 72 is arranged at the joint of the induced draft fan 7 and the induced air pipeline 71, the communicated end of the induced air pipeline 71 and the separating chamber 6 is higher than the communicated end of the connecting pipeline 64 and the separating chamber 6, and the induced air assembly is used for inducing air integrally.
As shown in fig. 3, the bottom end of the vibration pulverizer 1 is provided with a cold water joint 13, the cold water joint 13 is positioned inside the interlayer at the bottom end of the vibration pulverizer 1, cold water is introduced into the interlayer at the bottom end of the vibration pulverizer 1 through the cold water joint 13, the inside of the vibration pulverizer 1 is cooled, and meanwhile, heat inside the vibration pulverizer 1 is taken away continuously in the process of sucking powder particles into the classifying chamber 3, so that the temperature balance during vibration pulverizing is improved, and the powder particle quality is improved.
As shown in fig. 5, one end of the discharge pipeline 2, which is close to the vibration pulverizer 1, is provided with a discharge control pipeline 8, the discharge control pipeline 8 is arranged on the discharge pipeline 2 at a cutting-in angle gamma, the cutting-in angle gamma of the discharge control pipeline 8 is 50-60 degrees, and the angle is set so that the atmospheric pressure tangentially enters the return control pipeline 31, and the discharge pipeline 2 is prevented from being incapable of sucking the powder particles into the classifying chamber 3.
Working principle: the induced draft fan 7 is started to induce the whole device, so that the interiors of the classifying chamber 3, the collecting chamber 5 and the separating chamber 6 are all in a negative pressure state, then materials are added into the vibrating pulverizer 1 from the feed hopper 12 at a constant speed, then the materials are pulverized into powder particles by the vibrating pulverizer 1, at the moment, the powder particles are sucked into the pulverizing chamber through the discharging pipeline 2, at the moment, the classifying motor 42 is started to drive the transmission shaft 41 to rotate, the transmission shaft 41 drives the classifying wheel 4 to rotate while rotating, the powder particles rotate to generate centrifugal force, under the action of induced air, the powder particles simultaneously generate centripetal force towards the center of the classifying wheel 4, the disqualified powder particles are subjected to centrifugal force greater than the centripetal force, so that the disqualified powder particles are thrown to the inner wall of the classifying chamber 3 by the classifying wheel 4 and return to the vibrating pulverizer 1 to be pulverized again, and the qualified powder particles are subjected to centrifugal force less than the centripetal force, so that the qualified powder particles move towards the center of the classifying wheel 4, discharging from the discharging bin 32 under the action of induced air, further preventing the material from being crushed and disqualified due to the fact that the material crushing granularity is controlled by manually controlling the feeding amount, improving the production efficiency at the same time, sucking qualified powder particles into the collecting chamber 5 through the collecting pipeline 53 and the guiding pipeline 51 after the qualified powder particles are discharged from the discharging bin 32, enabling air flow to spirally flow towards the conical end of the collecting chamber 5 along the inner wall of the collecting chamber 5 under the action of the guiding pipeline 51, enabling the qualified powder particles to rotate to generate centrifugal force, separating the qualified powder particles from the air flow by the centrifugal force at the moment, throwing the qualified powder particles to the inner wall of the collecting chamber 5, enabling the qualified powder particles to fall into the first charging bucket 54 to be collected by the action of gravity, discharging a small amount of qualified powder particles from the collecting chamber 5 under the action of induced air in the process, sucking a small amount of qualified powder particles into the separating chamber 6 through the connecting pipeline 64 at the moment, then adsorbed on the cloth bag 62, when the qualified powder particles reach a certain amount on the cloth bag 62, the qualified powder particles adsorbed on the cloth bag 62 are flushed down to the second charging basket 61 by the pulse device 63 for collection.
The preferred embodiments of the present utility model have been described in detail above with reference to the accompanying drawings, but the present utility model is not limited to the specific details of the above embodiments, and various equivalent changes can be made to the technical solutions of the present utility model within the scope of the technical concept of the present utility model, and these equivalent changes all fall within the scope of the present utility model.
Claims (10)
1. The utility model provides a but online hierarchical continuous vibration smashes grader, includes vibration crusher (1), its characterized in that, the top of vibration crusher (1) is equipped with feed back pipeline (11), classifying chamber (3) and ejection of compact storehouse (32) in proper order, be equipped with feeder hopper (12) on feed back pipeline (11), classifying chamber (3) inside rotation is connected with classifying assembly, the exit end of ejection of compact storehouse (32) is equipped with induced air subassembly, the bottom of vibration crusher (1) is equipped with ejection of compact pipeline (2), the one end that vibration crusher (1) was kept away from to ejection of compact pipeline (2) extends to classifying chamber (3) inside.
2. The continuous vibration grinding classifier capable of classifying on line according to claim 1, wherein a return control pipeline (31) is arranged on the return pipeline (11), the connection end of the return control pipeline (31) and the return pipeline (11) is higher than the connection end of the feed hopper (12) and the return pipeline (11), the return control pipeline (31) is arranged on the return pipeline (11) at a cutting-in angle alpha, and the cutting-in angle alpha of the return control pipeline (31) is 50-60 degrees.
3. The continuous vibration grinding classifier capable of classifying online according to claim 1, wherein the classifying assembly comprises a classifying motor (42) arranged at the top end of the discharging bin (32), a transmission shaft (41) is coaxially arranged at the output end of the classifying motor (42), one end, far away from the classifying motor (42), of the transmission shaft (41) penetrates through the discharging bin (32) to extend into the classifying chamber (3), a classifying wheel (4) is coaxially arranged outside the extending end of the transmission shaft (41), and the classifying wheel (4) and the classifying chamber (3) are coaxial.
4. A continuous vibration crushing classifier capable of classifying on line according to claim 3, wherein the discharging pipeline (2) is vertically rotated upwards by 90 ° after extending into the classifying chamber (3), one end of the discharging pipeline (2) located in the classifying chamber (3) is provided with a discharging hopper (21), and the discharging hopper (21) is located under the classifying wheel (4) and is coaxial with the classifying wheel (4).
5. A continuously vibrating pulverizer classifier capable of classifying on line according to claim 3, wherein the angle formed between the outer ring of the classifying wheel (4) and the inner wall of the classifying chamber (3) is β, β being 10 ° to 15 °.
6. The continuous vibration crushing classifier capable of classifying online according to claim 1, wherein the outlet end of the discharging bin (32) is sequentially provided with a collecting pipeline (53) and a collecting chamber (5), a spiral guide pipeline (51) is arranged on the outer side of the collecting chamber (5), the a end of the guide pipeline (51) is communicated with the collecting pipeline (53), the b end of the guide pipeline (51) is communicated with the collecting chamber (5), the top end inside the collecting chamber (5) is vertically provided with an air inlet pipeline (52), the bottom end of the air inlet pipeline (52) is lower than the b end of the guide pipeline (51), the top end of the air inlet pipeline (52) extends out of the collecting chamber (5) and the extending end of the air inlet pipeline (52) is provided with a connecting pipeline (64), one end, far away from the air inlet pipeline (52), of the connecting pipeline (64) is provided with a gas-solid separation assembly, and the bottom end of the collecting chamber (5) is provided with a first charging basket (54).
7. The continuous vibration grinding classifier capable of classifying on line according to claim 6, wherein the gas-solid separation assembly comprises a separation chamber (6) communicated with a connecting pipeline (64), a plurality of cloth bags (62) for filtering powder particles are vertically arranged in the separation chamber (6), pulse devices (63) are arranged in the separation chamber (6), output ends of the pulse devices (63) are respectively arranged in the cloth bags (62), a second charging basket (61) is arranged at the bottom end of the separation chamber (6), and the separation chamber (6) is communicated with the air guiding assembly.
8. The continuous vibration grinding classifier capable of classifying on line according to claim 7, wherein the induced air component comprises an induced air pipeline (71) communicated with the separation chamber (6), one end of the induced air pipeline (71) far away from the separation chamber (6) is provided with an induced air draught fan (7), the joint of the induced air draught fan (7) and the induced air pipeline (71) is provided with an exhaust pipeline (72), and the communicated end of the induced air pipeline (71) and the separation chamber (6) is higher than the communicated end of the connecting pipeline (64) and the separation chamber (6).
9. The continuous vibration pulverizer classifier capable of classifying on line according to claim 1, wherein a cold water joint (13) is arranged at the bottom end of the vibration pulverizer (1), and the cold water joint (13) is positioned in an interlayer at the bottom end of the vibration pulverizer (1).
10. The continuous vibration pulverizer classifier capable of classifying on line according to claim 1, wherein one end of the discharge pipe (2) close to the vibration pulverizer (1) is provided with a discharge control pipe (8), the discharge control pipe (8) is arranged on the discharge pipe (2) at a cut-in angle γ, and the cut-in angle γ of the discharge control pipe (8) is 50 ° to 60 °.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202221526352.7U CN219631527U (en) | 2022-06-17 | 2022-06-17 | Continuous vibration crushing classifier capable of classifying online |
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| CN202221526352.7U CN219631527U (en) | 2022-06-17 | 2022-06-17 | Continuous vibration crushing classifier capable of classifying online |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115041281A (en) * | 2022-06-17 | 2022-09-13 | 南京天目超微技术研究开发有限公司 | Continuous vibration crushing classifier capable of realizing online classification |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115041281A (en) * | 2022-06-17 | 2022-09-13 | 南京天目超微技术研究开发有限公司 | Continuous vibration crushing classifier capable of realizing online classification |
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