CN101402073A - Coarse, medium, fine powder multi-stage air separator - Google Patents
Coarse, medium, fine powder multi-stage air separator Download PDFInfo
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- CN101402073A CN101402073A CNA2008102340445A CN200810234044A CN101402073A CN 101402073 A CN101402073 A CN 101402073A CN A2008102340445 A CNA2008102340445 A CN A2008102340445A CN 200810234044 A CN200810234044 A CN 200810234044A CN 101402073 A CN101402073 A CN 101402073A
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Abstract
The invention provides a multistage powder selecting machine for coarse, middle and fine powders. The multistage powder selecting machine comprises a shell, a motor, a rotor, wind guide blades, cyclone cylinders, a feeding pipe and a wind converging pipe; the rotor arranged above the shell is connected with the motor; the periphery of the rotor is provided with the wind guide blades; the lower part of the rotor is provided with a feed dropping hopper; a lower mouth of the feed dropping hopper is provided with a wind locking valve; the periphery of the shell is provided with a plurality of the cyclone cylinders; an upper mouth of the cyclone cylinder is respectively communicated with the shell and the wind converging pipe; a lower mouth of the cyclone cylinder is provided with a discharge valve; a lower mouth of the shell is provided with the feeding pipe; the outer side of the feeding pipe is sleeved with a feed dropping cylinder; a lower mouth of the feed dropping cylinder is provided with a wind locking valve; and a plurality of whole guide plates in spiral arrangement are arranged on the outer wall of the feed dropping hopper above the feed dropping cylinder. The multistage powder selecting machine is particularly suitable for the multistage production of sands and stones, has the advantages that the multistage powder selecting machine has a reasonable structure, more classification times, high classification precision, low manufacturing cost and operation and maintenance expenses and good economic benefit, can effectively improve specific yield and working efficiency and reduce environmental pollution.
Description
Technical field
The present invention relates to a kind of screening installation of powder, the multistage powder concentrator of particularly a kind of carse, medium and small powder.
Background technology
At present, powder concentrator is widely used in the powder manufacturings such as manufacture of cement.Existing traditional centrifugal, cyclone type of existing powder concentrator and rotator type powder concentrator also have the good relatively O-Sepa powder concentrator of performance that comes out in recent years.Existing O-Sepa powder concentrator, its working mechanism is: the material through preliminary grinding feeds powder concentrator by the top charging aperture, fully disperses by spreading disk, buffer board, falls into powder-separating area.Wind by the air inlet of separating chamber both sides, enters powder-separating area through guide vane respectively.The cage rotor of in powder concentrator, forming by vertical vane and horizontal blade, make during revolution that whole powder-separating area inside and outside differential pressure is kept up and down necessarily, steady air current is even, the chance that repeatedly repeats sorting is provided for top-down material, qualified fine powder is extracted out from top by central tube with air-flow, enters follow-up dust-precipitator fines collection is got off; Meal returns grinding machine grinding once more from the cone bottom, form the circle streaming system.Though O-Sepa powder concentrator unit interval treating capacity is big, effectiveness of classification is high, energy-saving and cost-reducing and be widely used, but because the O-Sepa powder concentrator can only carry out classification to the micron order powder material by its rotor, thereby can't satisfy the demand that the sandstone classification is produced, can't with the sandstone finished product by particle diameter>2mm, 2~0.1mm and<three kinds of specifications of 0.1mm realize carse, medium and small three ranking score levels; And, because sandstone coarse granule particle diameter is bigger, also can cause the O-Sepa rotor of powder separator to damage easily, can not run well.At present, in sandstone classification production process, still adopt traditional vibratory sieve, yet vibratory sieve can only be classification face with 2mm usually, can't realize multipass sort, make the particle of 2mm be waste product, cause great waste of raw materials, and production efficiency is low, operation and maintenance cost height, dust are difficult to control, heavy contamination.
Summary of the invention
Technical problem to be solved by this invention is, at the deficiencies in the prior art, a kind of rational in infrastructure, manufacturing cost is provided and operation and maintenance cost is low, classification often, the multistage powder concentrator of effectiveness of classification and output, high efficiency.
The technical solution adopted for the present invention to solve the technical problems is: comprise housing, motor, rotor, wind blade, whirlwind tube, feed pipe and wind converging tube; Rotor is loaded on the top of housing and links to each other with motor, and the periphery of rotor is provided with wind blade, and the below of rotor is provided with material-falling hopper, and the end opening of material-falling hopper is provided with air valve; The periphery of housing is provided with several whirlwind tubes, and the suitable for reading of whirlwind tube interlinks with housing and wind converging tube respectively, and the end opening of whirlwind tube is provided with discharge valve; It is characterized in that: the end opening of housing is provided with feed pipe, is equipped with blanking barrel in the outside of feed pipe, and the end opening of blanking barrel is provided with air valve; On the outer wall of the material-falling hopper above the blanking barrel, be provided with the whole deflector that several piece is provided with in the shape of a spiral.During work, treat that the material of sorting enters in the powder concentrator from the feed pipe of housing below with the wind, the material of larger particles forms fluid bed, falls in the blanking barrel behind the bump cowling panel and discharges through air valve, realizes the one-level sorting; The cowling panel one side is the material of sedimentation larger particles effectively, reduces the resistance of equipment air inlet, can carry out rectification to air-flow on the other hand, makes the particle composition of material narrower, has reduced oarse-grained interference, helps fine granular materials and is sorted out fully.Air-flow rotates the middle and upper part that rises to housing after rectification, through wind blade once more after the rectification, carry out sorting once more by rotor, thicker material falls in the material-falling hopper, discharge the sorting of realization secondary by air valve, thinner material then is assigned with and enters in each whirlwind tube, and the whirlwind tube utilizes the gravity of material self to carry out the sorting of material, and, realize the classification for the third time of material by the discharge valve discharge.Superfine material in the air-flow then enters in the follow-up cleaner by wind converging tube, and fine material is recycled, and realizes the 4th classification of material, has improved rate of energy simultaneously, has reduced the harm of superfine powder to human body and environment.
Above-mentioned whirlwind tube is a centering type whirlwind tube, and its volute angle is 270 °, can effectively reduce equipment resistance like this, increases the dust-collecting efficiency of finished product, and can reduce the input of follow-up cleaner.
The inner chamber of above-mentioned whirlwind tube is provided with the taper radiation shield that prevents reentrainment of dust, and the radiation shield periphery links to each other with the inwall of whirlwind tube by several connecting rods.
Beneficial effect of the present invention is: be specially adapted to the classification production of sandstone, it is rational in infrastructure, classification often, the effectiveness of classification height, manufacturing cost and operation and maintenance cost are low, good in economic efficiency, and can improve specific yield and operating efficiency effectively, reduce environmental pollution.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 is the structural representation of whirlwind tube of the present invention;
Fig. 3 is the vertical view of Fig. 2;
Fig. 4 is the structural representation of cowling panel of the present invention.
Among the figure: 1 is that air valve, 2 is that material-falling hopper, 3 is that whirlwind tube, 4 is that housing, 5 is that rotor, 6 is that wind blade, 7 is that tube connector, 8 is that transmission foundation frame, 9 is that wind converging tube, 10 is that motor, 11 is that heavy frame, 12 is that cowling panel, 13 is that radiation shield, 14 is that discharge valve, 15 is that blanking barrel, 16 is that feed pipe, 17 is an air valve.
The specific embodiment
Below in conjunction with drawings and Examples the present invention is described in further detail: the embodiment of the invention be used for aluminum ore>2mm, 2~0.1mm and<classification and sorting of three kinds of specifications of 0.1mm is an example.
The multistage powder concentrator of the described a kind of carse, medium and small powder of the embodiment of the invention mainly comprises housing 4, motor 10, rotor 5, wind blade 6, feed pipe 16, whirlwind tube 3, blanking barrel 15, material-falling hopper 2 and wind converging tube 9; Rotor 5 is loaded on the top of housing 4 by heavy frame 11, and links to each other with motor 10 on being loaded on heavy frame 11 top transmission foundation frames 8; The peripheral horizontal direction of rotor 5 is provided with the equally distributed wind blade 6 of several piece, and the below of rotor 5 is provided with material-falling hopper 2, and the end opening of material-falling hopper 2 is provided with air valve 1.The periphery of housing 4 is provided with several centering type whirlwind tubes 3, and its volute angle is 270 °, and its inner chamber is provided with the taper radiation shield 13 that prevents reentrainment of dust, and radiation shield 13 has periphery to link to each other with the inwall of whirlwind tube 3 by several connecting rods; The suitable for reading of whirlwind tube 3 interlinks with housing 4 and wind converging tube 9 respectively by tube connector 7, and the end opening of whirlwind tube 3 is provided with duplex weight turnover plate type discharge valve 14; The end opening of housing 4 is provided with feed pipe 16, is equipped with blanking barrel 15 in the outside of feed pipe 16, and the end opening of blanking barrel 15 is provided with air valve 17; On the outer wall of the material-falling hopper above the blanking barrel 15 2, be provided with four to eight cowling panels 12 that are provided with in the shape of a spiral.
During work, the aluminum ore for the treatment of sorting enters in the powder concentrator from the feed pipe 16 of housing 4 belows with the wind, the larger particles material of>2mm forms fluid bed, behind bump cowling panel 12, fall in the blanking barrel 15 and discharge through air valve 17, realize the one-level sorting, the material that sub-elects returns crushing system and continues broken.Air-flow rotates the top that rises to housing 4 after rectification, after the rectification once more of wind blade 6, carry out sorting once more by rotor 5, the thick material of 2~0.1mm is fallen in the material-falling hopper 2, discharged by air valve 1, realize the secondary sorting, the material that sub-elects is as the one-level finished product.The thin material of<0.1mm then is assigned with and enters in each whirlwind tube 3, and whirlwind tube 3 utilizes the gravity of material self and centrifugal force to carry out the separation of material, and is discharged by discharge valve 14, realizes the classification for the third time of material, and the material that sub-elects is as the secondary finished product.In the air-flow<the thin material of 5 μ m then enters in the follow-up cleaner by wind converging tube 9, fine material is recycled, realize the 4th classification of material, the superfine material that sub-elects has improved rate of energy simultaneously, has reduced the harm of superfine powder to human body and environment as raw materials such as cement mixtures.
Claims (3)
1, the multistage powder concentrator of a kind of carse, medium and small powder comprises housing, motor, rotor, wind blade, whirlwind tube, feed pipe and wind converging tube; Rotor is loaded on the top of housing and links to each other with motor, and the periphery of rotor is provided with wind blade, and the below of rotor is provided with material-falling hopper, and the end opening of material-falling hopper is provided with air valve; The periphery of housing is provided with several whirlwind tubes, and the suitable for reading of whirlwind tube interlinks with housing and wind converging tube respectively, and the end opening of whirlwind tube is provided with discharge valve; It is characterized in that: the end opening of housing is provided with feed pipe, is equipped with blanking barrel in the outside of feed pipe, and the end opening of blanking barrel is provided with air valve; On the outer wall of the material-falling hopper above the blanking barrel, be provided with the whole deflector that several piece is provided with in the shape of a spiral.
2, the multistage powder concentrator of a kind of carse, medium and small powder according to claim 1, it is characterized in that: the inner chamber of above-mentioned whirlwind tube is provided with the taper radiation shield, and the radiation shield periphery links to each other with the inwall of whirlwind tube by several connecting rods.
3, the multistage powder concentrator of a kind of carse, medium and small powder according to claim 1 and 2, it is characterized in that: above-mentioned whirlwind tube is a centering type whirlwind tube, and its volute angle is 270 °.
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CNA2008102340445A CN101402073A (en) | 2008-11-02 | 2008-11-02 | Coarse, medium, fine powder multi-stage air separator |
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CNA2008102340445A CN101402073A (en) | 2008-11-02 | 2008-11-02 | Coarse, medium, fine powder multi-stage air separator |
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Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102335656A (en) * | 2011-06-22 | 2012-02-01 | 江苏吉能达建材设备有限公司 | Quadric-separated winnowing grader |
CN103608127A (en) * | 2010-07-16 | 2014-02-26 | 萨维工程有限公司 | Pulverizer classifier |
CN104549780A (en) * | 2015-01-14 | 2015-04-29 | 绵阳蓝奥重型机械制造有限公司 | Novel dual-transmission combined efficient sorting machine |
CN105013631A (en) * | 2015-09-03 | 2015-11-04 | 江苏亨特集团华特电气有限公司 | Novel powder grading device |
CN105414032A (en) * | 2015-12-09 | 2016-03-23 | 重庆龙悦食品有限公司 | Three-level grain cleaning device |
CN105414035A (en) * | 2015-12-09 | 2016-03-23 | 重庆龙悦食品有限公司 | Grain second-level winnowing device |
CN105562223A (en) * | 2015-12-18 | 2016-05-11 | 太仓井林机械科技有限公司 | Automatic slag powder concentrating machine |
CN106944157A (en) * | 2016-01-07 | 2017-07-14 | 中国石油化工股份有限公司 | A kind of catalytic cracking catalyst prepares moulding process and system |
CN107041173A (en) * | 2017-03-16 | 2017-08-15 | 新疆农垦科学院 | What a kind of residual film collecting box and the device were constituted broadcasts preceding incomplete film-recovering machine |
CN108311384A (en) * | 2018-02-08 | 2018-07-24 | 遵义市聚源建材有限公司 | One kind being convenient for fines collection powder concentrator |
CN109158316A (en) * | 2018-09-07 | 2019-01-08 | 天津水泥工业设计研究院有限公司 | A kind of compact combination formula powder concentrator for bed-grinding system |
CN109731785A (en) * | 2019-03-08 | 2019-05-10 | 卢继升 | A kind of mineral powder multipass sort system |
CN110538728A (en) * | 2019-09-04 | 2019-12-06 | 厦门理工学院 | Cyclone powder separator |
CN111556781A (en) * | 2017-12-06 | 2020-08-18 | 康明斯滤清系统知识产权公司 | Crankcase ventilation system with vortex breaker reducing tangential outflow fluid pressure drop |
CN112354703A (en) * | 2020-10-20 | 2021-02-12 | 江苏吉达机械制造有限公司 | Adjustable three-separation powder separator |
CN112387597A (en) * | 2020-11-18 | 2021-02-23 | 江苏绿都环境工程有限公司 | Intelligent powder concentrator capable of preventing abrasion and material blockage |
CN113828516A (en) * | 2021-08-20 | 2021-12-24 | 天津艾惟科技有限公司 | Material granularity grading device |
CN114713501A (en) * | 2022-04-15 | 2022-07-08 | 新疆晶硕新材料有限公司 | A particle size grading plant for high temperature hydrolysis nano-material |
-
2008
- 2008-11-02 CN CNA2008102340445A patent/CN101402073A/en active Pending
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103608127A (en) * | 2010-07-16 | 2014-02-26 | 萨维工程有限公司 | Pulverizer classifier |
CN102335656A (en) * | 2011-06-22 | 2012-02-01 | 江苏吉能达建材设备有限公司 | Quadric-separated winnowing grader |
CN102335656B (en) * | 2011-06-22 | 2014-03-12 | 江苏吉能达建材设备有限公司 | Quadric-separated winnowing grader |
CN104549780A (en) * | 2015-01-14 | 2015-04-29 | 绵阳蓝奥重型机械制造有限公司 | Novel dual-transmission combined efficient sorting machine |
CN105013631A (en) * | 2015-09-03 | 2015-11-04 | 江苏亨特集团华特电气有限公司 | Novel powder grading device |
CN105414032A (en) * | 2015-12-09 | 2016-03-23 | 重庆龙悦食品有限公司 | Three-level grain cleaning device |
CN105414035A (en) * | 2015-12-09 | 2016-03-23 | 重庆龙悦食品有限公司 | Grain second-level winnowing device |
CN105562223A (en) * | 2015-12-18 | 2016-05-11 | 太仓井林机械科技有限公司 | Automatic slag powder concentrating machine |
CN106944157A (en) * | 2016-01-07 | 2017-07-14 | 中国石油化工股份有限公司 | A kind of catalytic cracking catalyst prepares moulding process and system |
CN107041173A (en) * | 2017-03-16 | 2017-08-15 | 新疆农垦科学院 | What a kind of residual film collecting box and the device were constituted broadcasts preceding incomplete film-recovering machine |
CN111556781B (en) * | 2017-12-06 | 2022-03-29 | 康明斯滤清系统知识产权公司 | Crankcase ventilation system with vortex breaker reducing tangential outflow fluid pressure drop |
US11619152B2 (en) | 2017-12-06 | 2023-04-04 | Cummins Filtration Ip, Inc. | Crankcase ventilation systems having a swirl breaker to reduce pressure drop in tangentially exiting fluids |
CN111556781A (en) * | 2017-12-06 | 2020-08-18 | 康明斯滤清系统知识产权公司 | Crankcase ventilation system with vortex breaker reducing tangential outflow fluid pressure drop |
CN108311384A (en) * | 2018-02-08 | 2018-07-24 | 遵义市聚源建材有限公司 | One kind being convenient for fines collection powder concentrator |
CN109158316A (en) * | 2018-09-07 | 2019-01-08 | 天津水泥工业设计研究院有限公司 | A kind of compact combination formula powder concentrator for bed-grinding system |
CN109158316B (en) * | 2018-09-07 | 2024-04-23 | 天津水泥工业设计研究院有限公司 | Compact combined powder concentrator for material bed grinding system |
CN109731785A (en) * | 2019-03-08 | 2019-05-10 | 卢继升 | A kind of mineral powder multipass sort system |
CN109731785B (en) * | 2019-03-08 | 2023-09-05 | 卢继升 | Ore powder multistage separation system |
CN110538728A (en) * | 2019-09-04 | 2019-12-06 | 厦门理工学院 | Cyclone powder separator |
CN112354703A (en) * | 2020-10-20 | 2021-02-12 | 江苏吉达机械制造有限公司 | Adjustable three-separation powder separator |
CN112387597A (en) * | 2020-11-18 | 2021-02-23 | 江苏绿都环境工程有限公司 | Intelligent powder concentrator capable of preventing abrasion and material blockage |
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 |
CN114713501A (en) * | 2022-04-15 | 2022-07-08 | 新疆晶硕新材料有限公司 | A particle size grading plant for high temperature hydrolysis nano-material |
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