CN109127169A - A kind of side air inlet Verticle vortex powder concentrator selects powder method and application - Google Patents
A kind of side air inlet Verticle vortex powder concentrator selects powder method and application Download PDFInfo
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- CN109127169A CN109127169A CN201811124099.0A CN201811124099A CN109127169A CN 109127169 A CN109127169 A CN 109127169A CN 201811124099 A CN201811124099 A CN 201811124099A CN 109127169 A CN109127169 A CN 109127169A
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- 239000000843 powder Substances 0.000 title claims abstract description 97
- 238000000034 method Methods 0.000 title description 10
- 239000000428 dust Substances 0.000 claims abstract description 7
- 241000237942 Conidae Species 0.000 claims abstract 3
- 239000000463 material Substances 0.000 claims description 56
- 239000002245 particle Substances 0.000 claims description 14
- 238000005192 partition Methods 0.000 claims description 14
- 239000002893 slag Substances 0.000 claims description 7
- 230000009471 action Effects 0.000 claims description 6
- 239000004568 cement Substances 0.000 claims description 4
- 230000005484 gravity Effects 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims description 3
- 241000555745 Sciuridae Species 0.000 claims 2
- 238000005096 rolling process Methods 0.000 claims 2
- 239000011362 coarse particle Substances 0.000 claims 1
- 239000010419 fine particle Substances 0.000 claims 1
- 239000002609 medium Substances 0.000 claims 1
- 238000010187 selection method Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000009434 installation Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000005299 abrasion Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000007480 spreading Effects 0.000 description 2
- 238000003892 spreading Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 241000237983 Trochidae Species 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/10—Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/12—Centrifuges in which rotors other than bowls generate centrifugal effects in stationary containers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
Landscapes
- Combined Means For Separation Of Solids (AREA)
Abstract
本发明公开了一种侧进风立式涡流选粉机、选粉方法及应用，属于粉磨及选粉技术领域，包括设在上部的涡壳和设在下部的锥壳；所述涡壳水平设置，所述涡壳的开口端为进风口；在涡壳上部设有连接收尘装置的出风口；涡壳内设有笼形转子，所述出风口设在笼形转子的上方；在涡壳上方设有与所述笼形转子连接的驱动装置；在所述笼形转子的外侧沿周向设有导风叶片；在所述锥壳内设有壳状的下椎体，所述下椎体置于笼形转子的正下方，下椎体的下端连通有中粗粉出料溜管；所述中粗粉出料溜管的末端向下伸至所述锥壳的外部；所述锥壳的下端连通有粗粉出料溜管。本发明的选粉机结构合理，运行可靠，减少磨损，高效能耗。
The invention discloses a side-inlet vertical eddy current powder separator, a powder separation method and application, belonging to the technical field of grinding and powder separation. Horizontally arranged, the open end of the volute is an air inlet; the upper part of the volute is provided with an air outlet connected to the dust collecting device; the volute is provided with a cage rotor, and the air outlet is arranged above the cage rotor; A drive device connected to the cage rotor is arranged above the volute; wind guide vanes are arranged on the outer side of the cage rotor along the circumferential direction; The body is placed directly under the cage rotor, and the lower end of the lower vertebral body is connected with a medium and coarse powder discharge chute; the end of the medium and coarse powder discharge chute extends downward to the outside of the cone shell; the cone The lower end of the shell is connected with a coarse powder discharge chute. The powder separator of the invention has reasonable structure, reliable operation, reduced wear and high energy consumption.
Description
Technical field
The invention belongs to grinding and powder technical field is selected, more particularly to a kind of side air inlet Verticle vortex powder concentrator, selects powder
Method and application.
Background technique
Powder concentrator is one of key equipment of grinding system, is widely used in the industries such as cement and electric power, and powder concentrator is usual
Using different-grain diameter material particle in air medium stress condition difference material particles are sorted, performance is direct
Influence the energy consumption and production capacity of entire grinding system.The widest high-efficient powder concentrator of domestic and international application is mainly cage rotor choosing at present
Powder machine sorts material using the balance that gas carries power, material self weight and three power of rotor centrifugal force.Cage rotor selects powder
Machine is widely applied in the world, has developed out kind structure type, but there is no variations substantially for its central principle.
According to existing grinding system technology and industrial practice, the feeding manner of cage rotor powder concentrator mainly has at present
Material top, which is fed directly into, brings two kinds into lower part air inlet.Top feeding has that unavoidable feeding is irregular, and
It needs to be equipped with material lift equipment, powder concentrator device structure can also be generated and be seriously worn；Lower stream of airflow brings the mode of material into
Higher air quantity and wind pressure are then needed, the height of big specification equipment lifting is obviously increased, a large amount of material is by gas lift
The energy consumption of system is not only dramatically increased, but also serious erosive wear is generated to powder concentrator internal component, influences system operation
Stable and service life of equipment.
Summary of the invention
The present invention is to solve technical problem present in well-known technique, provides a kind of efficient low-consume and improves equipment life
Side air inlet Verticle vortex powder concentrator, select powder method and application.
The invention is realized in this way
A kind of side air inlet Verticle vortex powder concentrator, including the volute for being located at top and the conical shell for being located at lower part；The volute
Horizontally disposed, the open end of the volute is air inlet；The air outlet of connection dust arrester installation is equipped on volute top；It is set in volute
There is cage rotor, the air outlet is located at the top of cage rotor；
The driving device connecting with the cage rotor is equipped with above volute；The outside of the cage rotor circumferentially
Equipped with wind blade；
Shelly-shaped hypocentrum is equipped in the conical shell, the hypocentrum is placed in the underface of cage rotor, hypocentrum
Lower end is communicated with middle coarse powder discharge pipe；The end of the middle coarse powder discharge pipe extends substantially downward to the outside of the conical shell；It is described
The lower end of conical shell is communicated with coarse powder discharge pipe.
Further, the partition of setting is provided with along air-flow trend in volute bottom.
Further, the spacing of the wind blade is in 20~100mm.
Further, the wind blade and the angle of cage rotor radial direction are 15~75 °.
Further, air inlet Verticle vortex powder concentrator in any of the above-described side selects powder method, includes the following steps:
S1, material bring powder concentrator by air-flow from air inlet, under the action of air intake passage internal partition, air-flow and belongings
Material is divided into two parts to be entered in the volute along air inlet；
Part bulky grain in S2, material is fallen first in the case where gravity, vortex centrifugal power and gas carry power compound action
In to the conical shell；Another part bulky grain is stopped by wind blade, not can enter cage rotor, also falls into the vertebra shell of lower section
Interior, then two parts bulky grain passes through coarse powder discharge pipe together and is discharged powder concentrator；
S3, small particles material follow air-flow pass through wind blade and enter cage rotor powder-separating area domain；In air-flow
High speed rotation cage rotor by material fine grained and middle coarse granule separate, wherein be greater than partition size material fall
Enter in hypocentrum and slide to middle coarse powder discharge pipe, ultimately forms middle coarse powder and be discharged to outside powder concentrator；
S4, cage rotor is passed through in rotation less than the material of partition size, and entered with air-flow by air outlet and select powder
The subsequent dust arrester installation of machine, is finally collected as finished product.
Further, the application of any of the above-described kind of side air inlet Verticle vortex powder concentrator, Verticle vortex powder concentrator is entered the wind in the side
Applied to cement roller press final grinding system.
Further, the application of any of the above-described kind of side air inlet Verticle vortex powder concentrator, Verticle vortex powder concentrator is entered the wind in the side
Applied to raw material final grinding system of roll squeezer.
Further, the application of any of the above-described kind of side air inlet Verticle vortex powder concentrator, Verticle vortex powder concentrator is entered the wind in the side
Applied to various slags or metallurgical slag final grinding system of roll squeezer.
Further, the application of any of the above-described kind of side air inlet Verticle vortex powder concentrator, the side air inlet Verticle vortex select powder
Machine is applied to the final grinding system of roll squeezer of metal or nonmetallic ore.
The positive effect of the present invention and advantage:
1, in the present invention, the on-demand powder air quantity of material is entered by volute side, reduces powder concentrator internal gas flow improving material
Height, to reduce the internal drag of powder concentrator, while the technology arrangement height of powder concentrator equipment can also be reduced, save it is whole
The construction investment of body project；
2, furthermore all being brought by air quantity by powder concentrator, powder concentrator device external do not need material lifting and set material
It is standby, spout and spreading disc mechanism itself are not needed yet, it is structurally reasonable, it is reliable for operation, abrasion is reduced, energy consumption is reduced；
3, material brings top volute by air-flow, realize volute first time eddy flow centrifugal classification and second of cage rotor
Centrifugal classification；The excessive material of most of partial size is pre-separated in first time assorting room, reduces the work of second of sorting
Make load, improves the whole efficiency of separation；
4, it is provided with the partition of setting in volute, the material of gas and carrying enters cage rotor from partition two sides, avoids
Material is assembled around cage rotor, to improve sharpness of separation；
5, by adjusting the deflection angle of the air quantity of powder concentrator, cage rotor revolving speed, different zones wind blade, setting is suitable
Suitable production status is, it can be achieved that select the efficient low-consume of powder process.
Detailed description of the invention
Fig. 1 is the structure chart of air inlet Verticle vortex powder concentrator in side provided in an embodiment of the present invention；
Fig. 2 is the top view of Fig. 1；
Fig. 3 is the top view of plane where cage rotor provided in an embodiment of the present invention.
In figure, 1, volute；1-1, air inlet；1-2, air outlet；1-3, partition；2, conical shell；2-1, coarse powder discharge pipe；3,
Cage rotor；4, support device；5, driving device；6, wind blade；7, hypocentrum；7-1, middle coarse powder discharge pipe.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, with reference to embodiments, to the present invention
It is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, it is not used to
Limit the present invention.
As shown in Figure 1 to Figure 3, the present invention provides a kind of sides to enter the wind Verticle vortex powder concentrator, the whirlpool including being located at top
Shell 1 and the conical shell 2 for being located at lower part；The volute 1 is horizontally disposed, and the open end of the volute 1 is air inlet 1-1；In the whirlpool
1 top of shell is equipped with the air outlet 1-2 of connection dust arrester installation；Cage rotor 3 is equipped in volute 1, the air outlet 1-2 is located at cage type
The top of rotor 3；
Support device 4 is equipped with above volute 1；The support device 4 is equipped with the driving device of driving powder concentrator work
5；The driving device 5 is connect by slewing equipment with the cage rotor 3；
Wind blade 6 is circumferentially uniformly provided in the outside of the cage rotor 3；Meet separation condition outside cage rotor 3
Material can enter the powder-separating area domain of cage rotor 3 by the gap of wind blade 6.
The shelly-shaped hypocentrum 7 of circular cone is equipped in the conical shell 2, the hypocentrum 7 is placed in the underface of cage rotor 3,
The lower end of hypocentrum 7 is communicated with middle coarse powder discharge pipe 7-1；The end of the middle coarse powder discharge pipe 7-1 extends substantially downward to described
The outside of conical shell 2；
Coarse powder discharge pipe 2-1 is communicated in the lower end of the conical shell 2；
Due to the high speed rotation of cage rotor 3, the airflow field for attracting material will form in 3 near zone of cage rotor, this
Sample is largely focused on material around cage rotor 3, and the material near 1 inner wall of volute is less, and this material is unevenly distributed
It will cause after small particles material is swept along by large granular materials and be not easily accessible cage rotor 3, to influence separating effect；Therefore it is
Avoid such case, it is preferred that 1 bottom of volute along air-flow trend be provided with the partition 1-3, the partition 1-3 of setting from
Air inlet 1-1 is extended at about the 1/2 of 1 stroke of volute, and according to realization operating condition needs, the material of air-flow and carrying can be from partition 1-
3 two sides enter volute 1, so as to avoid aggregation of the material around cage rotor 3.
Since the equipment that patent of invention is related to is not intended to specific standard, specific material and specific use environment, so that
Finished product require it is also and nonspecific, therefore can air quantity, 3 revolving speed of cage rotor, different zones wind guide vane by adjusting powder concentrator
Suitable production status is arranged in the deflection angle of piece 6, to realize the efficient low-consume for entirely selecting powder process.
Theoretically, the revolving speed of cage rotor 3 is higher, and air drag is bigger, and the particle selected is thinner, therefore cage rotor 3
Revolving speed can be according to the requirement of finished particle gradation, fineness and Bi Biao come selection；Each cage rotor 3 is by driving device 5
It is driven by slewing equipment, driving device 5 includes motor, and revolving speed adjustment is realized by the frequency control of motor.
The spacing of the wind blade 6 is smaller, the angle between 3 radial direction of wind blade 6 and cage rotor is bigger, then material
Fineness it is thinner, higher than table, but corresponding resistance (air drag, particle and shock of wind blade 6 etc.) can also increase, because
This needs is adjusted according to spacing and angle of the material requirement to wind blade 6.Preferably, the spacing of the wind blade 6
In 20~100mm；The angle of wind blade 6 and cage rotor 3 is 15~75 °.
Above-mentioned side air inlet Verticle vortex powder concentrator selects powder method, includes the following steps:
S1, material bring powder concentrator by air-flow from air inlet 1-1, under the action of air intake passage internal partition 1-3, air-flow and
It carries material and is divided into two parts and enter in the volute 1 along air inlet 1-1；
Part bulky grain in S2, material is fallen first in the case where gravity, vortex centrifugal power and gas carry power compound action
In to the conical shell 2；Another part bulky grain is stopped by wind blade 6, not can enter cage rotor 3, also falls into the cone of lower section
In shell 2, then two parts bulky grain passes through coarse powder discharge pipe 2-1 together and is discharged powder concentrator；
S3, small particles material follow air-flow pass through wind blade 6 and enter cage rotor 3 powder-separating area domain；In gas
Stream high speed rotation cage rotor 3 by material fine grained and middle coarse granule separate, wherein be greater than partition size object
Material falls into hypocentrum 7 and slides to middle coarse powder discharge pipe 7-1, ultimately forms middle coarse powder and is discharged to outside powder concentrator；
S4, cage rotor 3 is passed through in rotation less than the material of partition size, and entered with air-flow by air outlet 1-2
The subsequent dust arrester installation of powder concentrator, is finally collected as finished product.
In the present invention, material brings top volute 1 by air-flow, realizes the first time eddy flow centrifugal classification and second of volute 1
Secondary 3 centrifugal classification of cage rotor；The excessive material of most of partial size is pre-separated in first time assorting room, reduces second
The workload of secondary sorting improves the whole efficiency of separation；Furthermore whole being brought by air quantity by powder concentrator of material, powder concentrator
Device external does not need material lift equipment, itself does not need spout and spreading disc mechanism yet, structurally reasonable, reliable for operation,
Abrasion is reduced, energy consumption is reduced；The on-demand powder air quantity of material is entered by 1 side of volute, reduces powder concentrator internal gas flow improving material
Height, to reduce the internal drag of powder concentrator, while the technology arrangement height of powder concentrator equipment can also be reduced, save it is whole
The construction investment of body project.
Side air inlet Verticle vortex powder concentrator of the invention can be used for cement roller press final grinding system, it can also be used to raw material
The occasion of final grinding system of roll squeezer and the sorting of the materials such as various slags or steel slag and other metallurgical slag final grinding system of roll squeezer,
The roll squeezer end grinding field that can be applied to metal or nonmetallic ore, can greatly improve grinding efficiency.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in essence of the invention
Made any modifications, equivalent replacements, and improvements etc., should all be included in the protection scope of the present invention within mind and principle.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811124099.0A CN109127169A (en) | 2018-09-26 | 2018-09-26 | A kind of side air inlet Verticle vortex powder concentrator selects powder method and application |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811124099.0A CN109127169A (en) | 2018-09-26 | 2018-09-26 | A kind of side air inlet Verticle vortex powder concentrator selects powder method and application |
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| CN109127169A true CN109127169A (en) | 2019-01-04 |
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ID=64812775
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811124099.0A Pending CN109127169A (en) | 2018-09-26 | 2018-09-26 | A kind of side air inlet Verticle vortex powder concentrator selects powder method and application |
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| Country | Link |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109622252A (en) * | 2019-01-23 | 2019-04-16 | 桂林晟兴机械制造有限公司 | The efficient powder selector of outer circulation flour mill |
| CN110538728A (en) * | 2019-09-04 | 2019-12-06 | 厦门理工学院 | A cyclone powder separator |
| CN115739628A (en) * | 2022-11-17 | 2023-03-07 | 成都利君实业股份有限公司 | Horizontal vortex three-separation powder separator |
| CN116493258A (en) * | 2023-06-28 | 2023-07-28 | 绵阳九方环保节能科技有限公司 | Horizontal vortex powder separator capable of preventing dust accumulation |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0067895A1 (en) * | 1981-06-19 | 1982-12-29 | OMYA GmbH | Centrifugal sifter |
| JPH0549077U (en) * | 1991-12-09 | 1993-06-29 | 石川島播磨重工業株式会社 | Three-way classifier |
| JP2004105805A (en) * | 2002-09-13 | 2004-04-08 | Sharp Corp | Reflux type separator |
| CN200954502Y (en) * | 2006-09-30 | 2007-10-03 | 江苏科行环境工程技术有限公司 | Wind-intaking device of superfine powder sorting machine special for industrial waste dregs |
| CN202155313U (en) * | 2011-06-23 | 2012-03-07 | 中材装备集团有限公司 | Centrifugal vertical cage type dynamic powder concentrator with forced vortex |
| CN102485353A (en) * | 2010-12-03 | 2012-06-06 | 中国石油天然气集团公司 | Composite split type sand selecting method |
| CN206286205U (en) * | 2016-12-20 | 2017-06-30 | 洛阳中联水泥有限公司 | It is a kind of to improve the O Sepa powder concentrators air channel for selecting component efficiency |
| CN209138895U (en) * | 2018-09-26 | 2019-07-23 | 天津水泥工业设计研究院有限公司 | A kind of side air inlet Verticle vortex powder concentrator |
-
2018
- 2018-09-26 CN CN201811124099.0A patent/CN109127169A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0067895A1 (en) * | 1981-06-19 | 1982-12-29 | OMYA GmbH | Centrifugal sifter |
| JPH0549077U (en) * | 1991-12-09 | 1993-06-29 | 石川島播磨重工業株式会社 | Three-way classifier |
| JP2004105805A (en) * | 2002-09-13 | 2004-04-08 | Sharp Corp | Reflux type separator |
| CN200954502Y (en) * | 2006-09-30 | 2007-10-03 | 江苏科行环境工程技术有限公司 | Wind-intaking device of superfine powder sorting machine special for industrial waste dregs |
| CN102485353A (en) * | 2010-12-03 | 2012-06-06 | 中国石油天然气集团公司 | Composite split type sand selecting method |
| CN202155313U (en) * | 2011-06-23 | 2012-03-07 | 中材装备集团有限公司 | Centrifugal vertical cage type dynamic powder concentrator with forced vortex |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109622252A (en) * | 2019-01-23 | 2019-04-16 | 桂林晟兴机械制造有限公司 | The efficient powder selector of outer circulation flour mill |
| CN109622252B (en) * | 2019-01-23 | 2024-03-12 | 桂林晟兴机械制造有限公司 | High-efficiency powder selector of external circulation pulverizer |
| CN110538728A (en) * | 2019-09-04 | 2019-12-06 | 厦门理工学院 | A cyclone powder separator |
| CN115739628A (en) * | 2022-11-17 | 2023-03-07 | 成都利君实业股份有限公司 | Horizontal vortex three-separation powder separator |
| CN115739628B (en) * | 2022-11-17 | 2025-02-07 | 成都利君实业股份有限公司 | Horizontal eddy current three-separation powder separator |
| CN116493258A (en) * | 2023-06-28 | 2023-07-28 | 绵阳九方环保节能科技有限公司 | Horizontal vortex powder separator capable of preventing dust accumulation |
| CN116493258B (en) * | 2023-06-28 | 2023-09-05 | 绵阳九方环保节能科技有限公司 | Horizontal vortex powder separator capable of preventing dust accumulation |
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Application publication date: 20190104 |
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