CN105435906A - Adjustable multistage separation type powder selecting machine - Google Patents
Adjustable multistage separation type powder selecting machine Download PDFInfo
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- CN105435906A CN105435906A CN201510939015.9A CN201510939015A CN105435906A CN 105435906 A CN105435906 A CN 105435906A CN 201510939015 A CN201510939015 A CN 201510939015A CN 105435906 A CN105435906 A CN 105435906A
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- 239000000843 powder Substances 0.000 title claims abstract description 50
- 238000000926 separation method Methods 0.000 title claims abstract description 41
- 239000002245 particle Substances 0.000 claims abstract description 32
- 230000005540 biological transmission Effects 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims description 75
- 239000000047 product Substances 0.000 claims description 41
- 230000000694 effects Effects 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 8
- 239000008187 granular material Substances 0.000 claims description 7
- 239000000428 dust Substances 0.000 claims description 5
- 238000009434 installation Methods 0.000 claims description 5
- 238000012216 screening Methods 0.000 claims description 5
- 230000003068 static effect Effects 0.000 claims description 5
- 230000006698 induction Effects 0.000 claims description 4
- 238000009423 ventilation Methods 0.000 claims description 4
- 230000007423 decrease Effects 0.000 claims description 3
- 239000011265 semifinished product Substances 0.000 claims description 3
- 238000005243 fluidization Methods 0.000 claims description 2
- 230000009711 regulatory function Effects 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 238000012546 transfer Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 238000000227 grinding Methods 0.000 abstract description 30
- 238000000034 method Methods 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000009826 distribution Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 2
- 238000012545 processing Methods 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 6
- 238000003801 milling Methods 0.000 description 5
- 230000006870 function Effects 0.000 description 4
- 239000004568 cement Substances 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000003116 impacting effect Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
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- 239000002893 slag Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/10—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone
- B02C23/12—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone with return of oversize material to crushing or disintegrating zone
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
- B02C23/24—Passing gas through crushing or disintegrating zone
- B02C23/28—Passing gas through crushing or disintegrating zone gas moving means being integral with, or attached to, crushing or disintegrating element
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
- B02C23/24—Passing gas through crushing or disintegrating zone
- B02C23/30—Passing gas through crushing or disintegrating zone the applied gas acting to effect material separation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C2015/002—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs combined with a classifier
Abstract
The invention discloses an adjustable multistage separation type powder selecting machine. The adjustable multistage separation type powder selecting machine is characterized by comprising a feeding pipe device (1), a bearing component (2), a dynamic rotor (3), a multistage separation particle size adjusting system (4), a multistage separation conveying device (5), a transmission device (6) and a shell (7). The adjustable multistage separation type powder selecting machine, provided by the invention, can divide powder-grinded products into three grades to satisfy different process treatment flow demands of a powder grinding system so as to promote actuation of performances of powder grinding equipment, can flexibly adjust the fineness and particle distribution of all grades of products, can strictly control physical and chemical performances, improves the product quality and the efficiency of the powder selecting machine, cannot generate the phenomenon of over powder grinding and thick particle running, and reduces such comprehensive economic benefits as energy consumption. The whole adjustable multistage separation type powder selecting machine is reasonable in structure, convenient for processing and manufacturing, convenient for operation, flexible in adjustment and low in equipment production operation maintenance cost.
Description
Technical field
Material grinding technique field of the present invention, specifically just relates to a kind of adjustable machine for multi-class selective separation of powder for cement industry grinding system, can improve grinding efficiency and Grinding Quality.
Background technology
Current, grinding technology is widely used in cement industry grinding raw material, grog, the raw coal of electric power and the various quality of coal chemical industry grinding and steel plant's grinding blast-furnace cinder and slag etc.Grinding and select powder to be very important two technological processes in whole grinding process system, it selects powder technology directly to affect the key factor of whole grinding system efficiency and final products quality especially.Grinding becomes more tiny powdery fine particle by certain bulk or granular raw mill, the finished product meeting Particle size requirements selecting powder to be about in the powdered granule after grinding is separated, the particle size of finished product and size distribution are two very crucial technical indicators, adopt which kind of powder concentrator technology finally to decide this two technical indicators.
Market has the powder concentrator that plurality of specifications is different from structure, the structure comprised has respective difference.Related documents also discloses the Structure and characteristics of various powder concentrator, but this kind of powder concentrator does not all possess multi-stage separation selects powder function, be only simply separated finished product and non-finished product, and its end properties can not carry out flexible modulation with product demand.In addition, grinding efficiency is not high or select powder to lose efficacy, and causes whole grinding system inefficiency, there is grinding phenomenon thus greatly increased system energy consumption.Some powder concentrator structures are too numerous and diverse, and manufacture, installation, maintenance are all very inconvenient.
Summary of the invention
Object of the present invention is exactly cannot carry out for existing powder concentrator the technological deficiency that multi-stage separation selects powder function, there is provided a kind of and regulate multistage separating powder concentrator, have being carried out multi-stage separation by the graininess granular material mixture of grinding and being delivered to the function in grinding system in next PROCESS FOR TREATMENT flow process respectively, remarkable high grinding efficiency and Grinding Quality within the scope of different-grain diameter.
Technical scheme
A kind of adjustable multistage separating powder concentrator, is characterized in that: it comprises feed pipe device, bearing assembly, dynamic rotor, multi-stage separation particle size adjustment system, multi-stage separation conveying device, transmission device and housing, described feed pipe device top is arranged in bearing assembly upper body, and pass bearing assembly and multi-stage separation conveying device downwards for material decline passway is provided, bearing assembly rotor top is connected by bolt pair with transmission device, rotor bottom is connected by bolt pair with dynamic rotor, bearing assembly rotor is formed a connecting link and the moment of torsion of transmission device is passed to dynamic rotor, bearing assembly static support body is connected with housing by flange, described multi-stage separation particle size adjustment system is fixedly mounted on enclosure interior and is positioned at outside dynamic rotor, multi-stage separation particle size adjustment system and the multi-stage separation conveying device be fixed on housing form passage, the semi-finished product of screening are delivered to outside housing.
Beneficial effect
Adjustable multistage separating powder concentrator provided by the invention, can be divided into three grades by ground prod, meets grinding system different process handling process demand, thus promotes the performance of milling equipment performance; It can accomplish flexible modulation to product fineness at different levels and distribution of particles, can strictly control its physical and chemical performance, improves product quality, improves powder concentrator efficiency, " crossing grinding " and " running thick " phenomenon can not occur, lower the overall economic efficiencies such as energy consumption.Whole adjustable machine for multi-class selective separation of powder is rational in infrastructure, is convenient to processing and manufacturing, and operation is convenient especially, and flexible adjustment, device fabrication operation expense is low.
Accompanying drawing explanation
Accompanying drawing 1 is embodiment of the present invention operating diagram;
Accompanying drawing 2 is the H-H sectional views in accompanying drawing 1.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention will be further described.
Embodiment
As shown in Figure 1, a kind of adjustable multistage separating powder concentrator, is characterized in that: it comprises feed pipe device 1, bearing assembly 2, dynamic rotor 3, multi-stage separation particle size adjustment system 4, multi-stage separation conveying device 5, transmission device 6 and housing 7, described feed pipe device 1 top is arranged in bearing assembly 2 upper body, and pass bearing assembly 2 and multi-stage separation conveying device 5 downwards for material decline passway is provided, bearing assembly 2 rotor top is connected by bolt pair with transmission device 6, rotor bottom is connected by bolt pair with dynamic rotor 3, bearing assembly 2 rotor is formed a connecting link and the moment of torsion of transmission device 6 is passed to dynamic rotor 3, bearing assembly 2 static support body is connected with housing 7 by flange, described multi-stage separation particle size adjustment system 4 is fixedly mounted on housing 7 inside and is positioned at outside dynamic rotor 3, multi-stage separation particle size adjustment system 4 and the multi-stage separation conveying device 5 be fixed on housing 7 form passage, the semi-finished product of screening are delivered to outside housing 7.
Described feed pipe device 1 is positioned at powder concentrator center, and it comprises feed pipe 101, feed pipe 101
Material is abrasion-proof stainless steel material, and thickness is 8 ~ 12mm.
Described bearing block assembly 2 comprises bearing block 200, bearing group 201, bearing seal 202, bearing block overcoat 203 and bearing block inner sleeve 204, described bearing group 201 comprises bearing one 201a and bearing two 201b, be arranged on the upper and lower of bearing block 200 respectively, bearing group 201 inner ring and outer ring are formed with bearing block inner sleeve 204 and bearing block overcoat 203 respectively and coordinate, and in the top of bearing one and bearing two bottom respectively installation shaft hold sealing 202,202 ' and avoid Bearing outer dust to enter Bearing inner causing damage to bearing.
Describedly arrange up and down for vertical bearing 201, upper bearing (metal) 201a pattern is angular contact bearing, and lower bearing 201b pattern is deep groove ball bearing, and its pairing use can bear axis and the dynamic and static load of radial direction.
Described dynamic rotor 3 is revolving structure and rotating speed is adjustable, and its speed of gyration is adjustable in 70 ~ 165rpm range of speeds; .
Described multi-stage separation particle size adjustment system 4 has airflow field and dust granules material field water conservancy diversion regulatory function in powder concentrator;
Described multi-stage separation particle size adjustment system 4 is for comprising for support body and blade, and blades installation forms screening and flow-guiding channel on support body;
Described blade is annular blade.
Described multi-stage separation conveying device 5 comprises final finished device for transporting objects 501, semi-product material conveying device 1 and semi-product material conveying device 2 503, described final finished device for transporting objects 501 is positioned at housing 7 top, semi-product material conveying device 2 503 is between semi-product material conveying device 502 and housing 7, be fixed on housing 7 by support, it is inner that semi-product material conveying device 1 part is positioned at semi-product material conveying device 2 503, its transfer passage is through semi-product material conveying device 2 503 and housing 7, and weld together with housing 7.
Described semi-product material conveying device 502 is dynamic fluidized induction system;
Described dynamic fluidized induction system comprises customization special-shaped ventilation wear-resistance transmission medium layer 502a, high-pressure axial flow fan 502b and pipe-line system 502c, abnormity ventilation wear-resistance transmission medium layer 502a is arranged on the bottom of semi-product material conveying device 502, upper surface contacts with material, lower surface and lower case form gas channel, the perforate of semi-product material conveying device 502 lower case, weld with pipe-line system 502c and form flow delivery systems, axial flow blower is arranged on the end of pipe-line system 502c, provides fluidisation power to whole system;
The pressure-air that described high-pressure axial flow fan 502b produces produces dynamic fluidized effect to fine particulate semi-product material.
Described transmission device 6 comprises and is made up of frequency converter 601, drive motors 602, driving belt 603, big belt pulley 604, small belt pulley 605 and case 606, described frequency converter 601 is connected with drive motors 602 with remote control terminal respectively, remote control information is passed to drive motors 602, drive motors 602 output shaft is equipped with small belt pulley 605, small belt pulley 605 is connected with big belt pulley 604 by driving belt 603, and big belt pulley 604 controls dynamic rotor 3 and turns round.
The course of work of the present invention is: block stock O to be comminuted is entered in milling equipment M1 by powder concentrator feed pipe device 1 and carries out initial grinding, by the air-flow possessing certain speed, the at different levels material A BCs different through preliminary grinding particle size are entered in powder concentrator from the grinding zone of milling equipment M1 afterwards, directly enter multi-stage separation particle size adjustment system 4.The outer ring annular plate blade 401 of described multi-stage separation particle size adjustment system 4 carries out primary separation to the multistage particle diameter material entered in powder concentrator, the material be separated and final finished material A and the mixture of semi-product material B enter inner ring annular plate blade 402 and are again separated, and are separated remaining material and semi-product material C enters milling equipment M1 again by grinding by its semi-product material conveying device 2 503 by outer ring annular plate blade 401.Enter the inner ring annular final finished material A of plate blade 402 and the mixture of semi-product material B under itself and dynamic rotor 3 synergy, isolate final finished material A and semi-product material B, its final finished material A and air-flow be mixed by final finished device for transporting objects 501 export to powder concentrator outer after enter gathering dust in technological process in grinding system, and semi-product material B is also outputted to outside powder concentrator by semi-product material conveying device 502 and enters in the technological process of milling equipment.
By reference to the accompanying drawings shown in 2, the present invention is described in further detail and how accomplishes graininess granular material mixture multi-stage separation.Outer ring annular plate blade 401 is made up of incision blade 401a and swirl vane 401b, its combinations of pairs is a pair vane group, space bar device 401c is had between incision blade 401a and swirl vane 401b, its function is isolation incision blade 401a and swirl vane 402b, stops air-flow and material and enter powder concentrator powder-separating area in the middle of these two blades.Air-flow and mixtures of materials at different levels by outer ring annular plate blade 401 often pair of vane group between gap enter powder concentrator first powder-separating area XX, in this powder-separating area, material bears the effect of airflow buoyancy and self gravitation.Under the drive of air-flow, first the maximum coarse granule material of particle diameter contacts with incision blade 401a and falls down after clashing into its surperficial stall, simultaneously, swirl vane 401b causes the air-flow entered between often pair of vane group gap produce the eddy current physical effect of WW in regional area and cause coarse granule to fall down under self gravitation effect in the instantaneous stall in this region, other small particle diameter material is taken away the first powder-separating area XX because quality is little under airflow buoyancy effect, namely produces the effect of separation.The impact on its surface of material impacting and time started is controlled thus the particle diameter (μm) of the material that controls to drop or fineness (cm2/g) and total amount (t/h) by regulating the angle [alpha] of incision blade 401a.Controlled vortex flow strength size and eddy region area is come thus in controlled vortex flow region, WW drops the particle size (μm) of material or fineness (cm2/g) and total amount (t/h) by regulating the angle beta of swirl vane.
Enter the multistage mixture material of powder concentrator at the mixture AB being isolated semi-product material C, final finished material A and semi-product material B by the first powder-separating area XX, its the latter enters the second powder-separating area YY be made up of inner ring ring-type plate blade 402 and dynamic rotor 3, in this powder-separating area, material bears the effect of airflow buoyancy, self gravitation and centrifugal force.Dynamic rotor 3 rotates and produces centrifugal action to the material at the second powder-separating area YY, the quality material that greatly namely particle diameter is large causes stall to drop because centrifugal force clashes into greatly and first the guide vane 402a of inner ring ring-type plate blade 402, and other small particle diameter material is taken away the second powder-separating area YY because quality is little under airflow buoyancy effect.Material from inner ring ring-type plate blade 402 drops is semi-product material B, under airflow buoyancy effect, be final finished material A by the material taken away.The impact on its surface of material impacting and time started is controlled thus the particle diameter (μm) of the material that controls to drop or fineness (cm2/g) and total amount (t/h) by the angle γ of adjustment inner ring ring-type plate blade 402a.Controlled the centrifugal force of different-grain diameter material by adjustment dynamic rotor 3 speed of gyration, its strength of clashing into guide vane be there are differences, thus control the particle diameter (μm) of material or fineness (cm2/g) and total amount (t/h).
In embodiment of the present invention, separately have any different in above-mentioned regulative mode, the buoyancy of material is adjusted by the air quantity (m3/h) of air-flow in powder concentrator, under the prerequisite that powder concentrator mechanical dimension specification is certain, by the air quantity of the first powder-separating area XX and the second powder-separating area YY, the larger buoyancy produced material of its value is just large, vice versa, the logistics of different-grain diameter is taken away powder-separating area under the effect of airflow buoyancy, and the particle diameter (μm) of such product or fineness (cm2/g) and output (t/h) just can make flexible modulation
Structure, ratio, size etc. that the present embodiment institute accompanying drawings illustrates, content all only in order to coordinate description to disclose, understand for person skilled in the art scholar and read, and be not used to limit the enforceable qualifications of the present invention, therefore the not technical essential meaning of tool, the adjustment of the modification of any structure, the change of proportionate relationship or size, do not affecting under effect that the present invention can produce and the object that can reach, still all should drop on disclosed technology contents and obtain in the scope that can contain.Simultaneously, quote in this description as " on ", D score, "left", "right", " centre ", " clockwise ", " counterclockwise " etc. term, also only for ease of understanding of describing, and be not used to limit the enforceable scope of the present invention, the change of its relativeness or adjustment, under changing technology contents without essence, when being also considered as the enforceable category of the present invention.
Claims (7)
1. an adjustable multistage separating powder concentrator, is characterized in that: it comprises feed pipe device (1), bearing assembly (2), dynamic rotor (3), multi-stage separation particle size adjustment system (4), multi-stage separation conveying device (5), transmission device (6) and housing (7), described feed pipe device (1) top is arranged in bearing assembly (2) upper body, and pass bearing assembly (2) and multi-stage separation conveying device (5) downwards for material decline passway is provided, bearing assembly (2) rotor top is connected by bolt pair with transmission device (6), rotor bottom and dynamic rotor (3)) be connected by bolt pair, bearing assembly (2) rotor is formed a connecting link and the moment of torsion of transmission device (6) is passed to dynamic rotor (3), bearing assembly (2) static support body is connected with housing (7) by flange, described multi-stage separation particle size adjustment system (4) is fixedly mounted on housing (7) inside and is positioned at dynamic rotor (3) outside, multi-stage separation particle size adjustment system (4) and the multi-stage separation conveying device (5) be fixed on housing (7) form passage, the semi-finished product of screening are delivered to outside housing (7).
2. the adjustable multistage separating powder concentrator of one according to claim 1, it is characterized in that: described feed pipe device (1) is positioned at powder concentrator center, it comprises feed pipe (101), feed pipe (101) material is abrasion-proof stainless steel material, and thickness is 8 ~ 12mm.
3. the adjustable multistage separating powder concentrator of one according to claim 1, it is characterized in that: described bearing block assembly (2) comprises bearing block (200), bearing group (201), bearing seal (202, 202 '), bearing block overcoat (203) and bearing block inner sleeve (204), described bearing group (201) comprises bearing one (201a) and bearing two (201b), be arranged on the upper and lower of bearing block (200) respectively, bearing group (201) inner ring and outer ring are formed with bearing block inner sleeve (204) and bearing block overcoat (203) respectively and coordinate, and in the top of bearing one (201a) and bearing two (201b) bottom respectively installation shaft hold sealing (202, 202 ') avoid Bearing outer dust to enter Bearing inner and damage is caused to bearing,
Describedly arrange up and down for vertical bearing group (201), bearing one (201a) pattern is angular contact bearing, and bearing two (201b) pattern is deep groove ball bearing, and its pairing use can bear axis and the dynamic and static load of radial direction.
4. the adjustable multistage separating powder concentrator of one according to claim 1, is characterized in that: described dynamic rotor (3) is for revolving structure and rotating speed is adjustable, and its speed of gyration is adjustable in 70 ~ 165rpm range of speeds.
5. the adjustable multistage separating powder concentrator of one according to claim 1, is characterized in that: described multi-stage separation particle size adjustment system (4) has airflow field and dust granules material field water conservancy diversion regulatory function in powder concentrator;
Described multi-stage separation particle size adjustment system (4) is for comprising for support body and blade, and blades installation forms screening and flow-guiding channel on support body;
Described blade is annular blade.
6. the adjustable multistage separating powder concentrator of one according to claim 1, it is characterized in that: described multi-stage separation conveying device (5) comprises final finished device for transporting objects (501), semi-product material conveying device one (502) and semi-product material conveying device two (503), described final finished device for transporting objects (501) is positioned at housing (7) top, semi-product material conveying device two (503) is positioned between semi-product material conveying device (502) and housing (7), be fixed on housing (7) by support, it is inner that semi-product material conveying device one (502) part is positioned at semi-product material conveying device two (503), its transfer passage is through semi-product material conveying device two (503) and housing (7), and weld together with housing (7),
Described semi-product material conveying device (502) is dynamic fluidized induction system;
Described dynamic fluidized induction system comprises the special-shaped ventilation wear-resistance transmission medium layer (502a) of customization, high-pressure axial flow fan (502b) and pipe-line system (502c), abnormity ventilation wear-resistance transmission medium layer (502a) is arranged on the bottom of semi-product material conveying device (502), upper surface contacts with material, lower surface and lower case form gas channel, semi-product material conveying device (502) lower case perforate, flow delivery systems is formed with pipe-line system (502c) is fixing, axial flow blower is arranged on the end of pipe-line system 502c, fluidisation power is provided to whole system,
The pressure-air that described high-pressure axial flow fan (502b) produces produces dynamic fluidized effect to fine particulate semi-product material.
7. the adjustable multistage separating powder concentrator of one according to claim 1, it is characterized in that: described transmission device (6) comprises by frequency converter (601), drive motors (602), driving belt (603), big belt pulley (604), small belt pulley (605) and case (606) composition, described frequency converter (601) is connected with drive motors (602) with remote control terminal respectively, remote control information is passed to drive motors (602), small belt pulley (605) drive motors (602) output shaft is equipped with, small belt pulley (605) is connected with big belt pulley (604) by driving belt (603), big belt pulley (604) controls dynamic rotor (3) revolution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510939015.9A CN105435906B (en) | 2015-12-15 | 2015-12-15 | A kind of adjustable multistage separating powder concentrator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510939015.9A CN105435906B (en) | 2015-12-15 | 2015-12-15 | A kind of adjustable multistage separating powder concentrator |
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| Publication Number | Publication Date |
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| CN105435906A true CN105435906A (en) | 2016-03-30 |
| CN105435906B CN105435906B (en) | 2018-02-27 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107470009A (en) * | 2017-09-11 | 2017-12-15 | 西安西热锅炉环保工程有限公司 | The frequency conversion rotation coal dust depth separation equipartition device and method of a kind of medium-speed pulverizer |
| CN107899694A (en) * | 2017-12-13 | 2018-04-13 | 盐城市科瑞达科技咨询服务有限公司 | A kind of efficient vortex formula powder concentrator |
| CN108057490A (en) * | 2017-12-13 | 2018-05-22 | 盐城市科瑞达科技咨询服务有限公司 | A kind of three composition dividing powder separating machine |
| CN109908679A (en) * | 2019-03-26 | 2019-06-21 | 江苏源创环保科技有限公司 | A kind of O-Sepa powder concentrator transmission device |
| CN113828516A (en) * | 2021-08-20 | 2021-12-24 | 天津艾惟科技有限公司 | Material granularity grading device |
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| CN109908679A (en) * | 2019-03-26 | 2019-06-21 | 江苏源创环保科技有限公司 | A kind of O-Sepa powder concentrator transmission device |
| CN113828516A (en) * | 2021-08-20 | 2021-12-24 | 天津艾惟科技有限公司 | Material granularity grading device |
| CN113828516B (en) * | 2021-08-20 | 2023-02-28 | 天津艾惟科技有限公司 | Material granularity grading device |
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