CN103264016B - A kind of material grading apparatus - Google Patents

A kind of material grading apparatus Download PDF

Info

Publication number
CN103264016B
CN103264016B CN201310144994.XA CN201310144994A CN103264016B CN 103264016 B CN103264016 B CN 103264016B CN 201310144994 A CN201310144994 A CN 201310144994A CN 103264016 B CN103264016 B CN 103264016B
Authority
CN
China
Prior art keywords
hopper
air
grade
room
falling
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201310144994.XA
Other languages
Chinese (zh)
Other versions
CN103264016A (en
Inventor
李明和
贺真
李颜
周鹏
郭新春
徐泽进
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
RUITONG PELLETIZING CO Ltd OF XIANGTAN
Original Assignee
RUITONG PELLETIZING CO Ltd OF XIANGTAN
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by RUITONG PELLETIZING CO Ltd OF XIANGTAN filed Critical RUITONG PELLETIZING CO Ltd OF XIANGTAN
Priority to CN201310144994.XA priority Critical patent/CN103264016B/en
Publication of CN103264016A publication Critical patent/CN103264016A/en
Application granted granted Critical
Publication of CN103264016B publication Critical patent/CN103264016B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Combined Means For Separation Of Solids (AREA)

Abstract

The invention provides a kind of material grading apparatus, comprise blower fan, grade divides to fall room and be arranged on described grade and divide and fall air-flow jet pipe on the sidewall of room and charging aperture, described air-flow jet pipe is connected with described blower fan, described air-flow jet pipe place straight line and described charging aperture place straight line have an intersection point, and described air-flow nozzle hole place straight line is horizontal line; Divide the bottom falling room to arrange several hoppers in described grade, the diameter of air-flow nozzle hole is 8-30 times of material particles average diameter.The present invention utilizes the adjustable high velocity air of air-flow nozzle hole, according to the specific area difference of the material fallen from charging aperture, give the horizontal movement speed that different-grain diameter material is different, thus obtain different horizontal displacement distances, leaving, it divides with gravity fall to grade in the corresponding hopper fallen bottom room again, realizes classification object.Further, material does not contact any screening plant body, and do not have relative friction forces, equipment loss is little.

Description

A kind of material grading apparatus
Technical field
The present invention relates to material grading apparatus field, especially, relate to a kind of material grading apparatus that can carry out real-time multi-layer classification to material.
Background technology
Vibrosieve equipment (as: linear vibrating screen, oval-shaped equal-thickness vibrating screen) is the visual plant of current solid material classification, is widely used in the industries such as mine, building materials, coal separation, the energy, chemical industry.Vibrosieve equipment is generally the exciting force utilizing vibrator (eccentric block or eccentric shaft) to produce, sieve nest is made to do periodic reverse vibration along exciting force direction, material circumference on compass screen surface is beated, required compass screen surface is arrived, to reach classification object regular for the stock grading of different size by different sieve apertures; Amplitude can be adjusted by the weight adjusting eccentric block.
But there is following shortcoming in this equipment:
1, equipment is merely able to carry out point scraping of a particle diameter, if need the material of multiple particle diameter, then needs to use multiple stage screening plant simultaneously;
2, screening plant adopts sieve plate to carry out stock grading, when after sieve pore blockade, screening efficiency can be caused obviously to decline, and the service life of sieve plate only has 2-3 month, and maintenance cost is high; Equipment failure rate is high, and the life-span is short, and in general, the bulk life time of vibratory sieve equipment was at about 5 years;
3, floor space is wide, high to the requirement of foundation of civil work; Each vibrosieve equipment has 2-3 to vibrator, and operation energy consumption is large, needs supporting independently dust pelletizing system.
Summary of the invention
The object of the invention is to provide a kind of material grading apparatus, to solve the technical problem of multi-layer classification, reduction classifying equipoment fault rate simultaneously.
For achieving the above object, the invention provides a kind of material grading apparatus, comprise blower fan, grade divides to fall room and be arranged on described grade and divide and fall air-flow jet pipe on the sidewall of room and charging aperture, described air-flow jet pipe is connected with described blower fan, described air-flow jet pipe central symmetry axis and described charging aperture central symmetry axis have an intersection point, and described air-flow nozzle hole central symmetry axis is horizontal line;
Divide the bottom falling room to arrange several hoppers in described grade, by the hopper nearest apart from described charging aperture as first hopper, then the A/F of first hopper is W 1:
W 1=1.5*L 1
L 1 = Rρ v a 2 2 h g * 3 16 γd * ( 2 ( h + H ) g - 2 h g )
Wherein, L 1for falling into the horizontal flight distance of the material of first hopper, R is resistance coefficient, and ρ is atmospheric density, v afor air-flow absolute velocity, h is air-flow nozzle hole diameter, and H is the vertical height that charging aperture to grade divides the bottom falling room, and γ is the density of material, and d is the material particular diameter of screening;
The diameter h of described air-flow nozzle hole is 8-30 times of material particles average diameter.
Preferably, divide the point of interface of the bottom falling room as initial point in the vertical straight line at described air-flow nozzle exit place and grade, the width of N number of hopper is the distance between the distalis of N number of hopper and nearside point;
The distance of nearside point and initial point is Tn:T n=(L n+ L n-1n>=2)/2
Namely the nearside point position of N number of hopper is the horizontal flight distance that falls into the material of N number of hopper and the half of horizontal flight distance sum of material falling into N-1 hopper;
The distance of distalis and initial point is Yn:Y n=(3L n-L n-1n>=2)/2;
The distalis position of N number of hopper is 3 times of horizontal flight distances falling into the material of N number of hopper and the half of difference of horizontal flight distance of material falling into N-1 hopper.
Preferably, the integral thickness of described material is 10-20 times of material average grain diameter.
Preferably, described grade divides the afterbody falling room to arrange deduster, and the bottom of described deduster arranges ash bucket.
Preferably, described deduster and described grade divide the opposite end falling room link to arrange pipeline to be connected to described blower fan.
Preferably, the grade minute between hopper distalis and next hopper nearside point is fallen mid point bottom room and is arranged baffle plate.
The present invention has following beneficial effect:
1, realize multi-layer classification simultaneously: because the particle diameter of material is different, the specific area of material then can be different, and under certain drop, the speed of material under airflow function of different-grain diameter just there will be difference, and the range ability of material on horizontal level is different.According to this principle, the present invention utilizes the adjustable high velocity air of air-flow nozzle hole, according to the specific area difference of the material fallen from charging aperture, give the horizontal movement speed that different-grain diameter material is different, thus obtain different horizontal displacement distances, leaving, it divides with gravity fall to grade in the corresponding hopper fallen bottom room again, realizes classification object; The grade of material and horizontal range can be regulated by the current rate of blower fan, easy to use;
2, equipment failure rate is low: material is and obtains different horizontal velocities after air flow contacts thus classification, and material does not contact any screening plant body in fact, and do not have relative friction forces, equipment loss is little, and the life-span is long;
3, micro-discharge: equipment air-flow recycles, micronic dust can precipitate gradually in cyclic process, realizes zero-emission to external world, environmental protection.
Except object described above, feature and advantage, the present invention also has other object, feature and advantage.Below with reference to figure, the present invention is further detailed explanation.
Accompanying drawing explanation
The accompanying drawing forming a application's part is used to provide a further understanding of the present invention, and schematic description and description of the present invention, for explaining the present invention, does not form inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the device structure sectional view of the preferred embodiment of the present invention;
Wherein, 1, blower fan, 2, grade divides and fall room, 3, air-flow jet pipe, 4, charging aperture, 5, hopper, 6, deduster, 7, ash bucket, 8, baffle plate.
Detailed description of the invention
Below in conjunction with accompanying drawing, embodiments of the invention are described in detail, but the multitude of different ways that the present invention can limit according to claim and cover is implemented.
See Fig. 1, a kind of material grading apparatus, comprise blower fan 1, grade divides to fall room 2 and be arranged on described grade and divide and fall air-flow jet pipe 3 on the sidewall of room 2 and charging aperture 4, described air-flow jet pipe 3 is connected with described blower fan 1, described air-flow jet pipe 3 central symmetry axis and described charging aperture 4 central symmetry axis have an intersection point, and described air-flow jet pipe 3 export center symmetry axis is horizontal line;
Divide the bottom falling room 2 to arrange several hoppers 5 in described grade, by the hopper 5 nearest apart from described charging aperture 4 as first hopper, then the A/F of first hopper is W 1:
W 1=1.5*L 1
Consider the dispersion in material dropping process and deviation, by first hopper width W 1be set to the horizontal flying distance L of material 11.5 times, make material fall into hopper central position.
And fall into the horizontal flight distance L of the material of first hopper 1computational process as following:
In the gas flow, the size being subject to the directed force F of air-flow when material does relative motion to air-flow is:
F=Rρs(v a-v) 2
In formula, R is resistance coefficient, and with material shapes, surface nature is relevant with Reynolds number; ρ is atmospheric density, and unit is kg/m 3; S is the front face area of material, and namely material is in the projected area of airflow direction, and unit is m 2; v afor the absolute velocity of air-flow, unit is m/s; V is the absolute velocity of material, and unit is m/s.
In order to simplify calculating, do not consider the diffusion of spout air-flow, setting material is 0 (level, vertical component velocity are 0) by the speed before spout, and material particular diameter is d, then material by the time t of spout is:
t = 2 h g
So horizontal component velocity v of being obtained by spout of material levelfor:
V level=Ft/m
In formula, m is the quality of material particles, and unit is Kg.
After abbreviation
In formula, γ is the density of material, and unit is kg/m 3.
To a certain fixture, fixing material, it is a constant.
By deriving above, obtaining the horizontal range L that material runs on the drop of H is:
L 1 = Rρ v a 2 2 h g * 3 16 γd * ( 2 ( h + H ) g - 2 h g )
Wherein, L 1for falling into the horizontal flight distance of the material of first hopper, R is resistance coefficient, and ρ is atmospheric density, v afor the absolute velocity of air-flow, h is air-flow nozzle hole diameter, and H is the vertical height that charging aperture to grade divides the bottom falling room, and γ is the density of material, and d is the material particular diameter of screening.
For guaranteeing the classification efficiency of equipment, the material of system feeding mouth is evenly distributed, and the diameter h of described air-flow nozzle hole is 8-30 times of material particles average diameter, ensures that air-flow can penetrate material.The height that the integral thickness of material and material particles are piled up, then can be the 10-20 of material average grain diameter doubly.
Preferably, the vertical line and the grade that described air-flow jet pipe 3 are exported place divide the point of interface of the bottom falling room 2 as initial point, and the width of N number of hopper is the distance between the distalis of N number of hopper and nearside point;
The distance Tn of nearside point and initial point falls into this material in hopper horizontal flight distance and the half of difference falling into last material in hopper horizontal flight distance, then with fall into last material in hopper horizontal flight distance sum, that is:
T n=(L n-L n-1)/2+L n-1n≥2
After simplification, obtain:
T n=(L n+L n-1)/2 n≥2
That is to say: the nearside point position of N number of hopper is the horizontal flight distance that falls into the material of N number of hopper and the half of horizontal flight distance sum of material falling into N-1 hopper.
To be Yn be the distance of distalis and initial point falls into this material in hopper horizontal flight distance and the half of difference falling into last material in hopper horizontal flight distance, then with fall into this material in hopper horizontal flight distance sum, that is:
Y n=(L n-L n-1)/2+L nn≥2
After simplification, obtain:
Y n=(3L n-L n-1)/2 n≥2;
That is to say: the distalis position of N number of hopper is 3 times of horizontal flight distances falling into the material of N number of hopper and the half of difference of horizontal flight distance of material falling into N-1 hopper.
Such as, as the horizontal flight distance L of material falling into first hopper 1for 2m, fall into the horizontal flight distance L of the material of first hopper 2for 5m, fall into the horizontal flight distance L of the material of first hopper 2during for 10m:
The width W of first hopper 1=1.5*L 1=1.5*2=3m
The nearside point of second hopper and the distance T of initial point 2=(L 2+ L 1)/2=(2+5)/2=3.5m
The distalis of second hopper and the distance Y of initial point 2=(3L 2-L 1)/2=(3*5-2)/2=13/2=6.5m
The nearside point of the 3rd hopper and the distance T of initial point 3=(L 3+ L 2)/2=(10+5)/2=7.5m
3rd distalis of hopper and the distance Y of initial point 3=(3L 3-L 2)/2=(3*10-5)/2=25/2=12.5m.
Preferably, can two crossing inclined-planes that to be set to this section of bottom mid point bottom room be top fall the grade minute between hopper distalis with next hopper nearside point, then make full use of the clearance spaces between two hoppers, make the material falling into this clearance spaces fall into both sides hopper along inclined-plane.
Or, the grade minute between hopper distalis and next hopper nearside point can fall mid point bottom room baffle plate be set, material is kept off in the hopper close to this material drop point.
Described grade divides the afterbody falling room to arrange deduster, and the bottom of described deduster arranges ash bucket, micronic dust can be made to enter deduster with air-flow, and naturally fall in ash bucket along with the exhaustion of air velocity.
Described deduster and described grade are divided and are fallen the relative other end in room and arrange pipeline and be connected to described blower fan, recycle fan airflow, environmental protection.
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for a person skilled in the art, the present invention can have various modifications and variations.Within the spirit and principles in the present invention all, any amendment done, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.

Claims (6)

1. a material grading apparatus, it is characterized in that, comprise blower fan, grade divides to fall room and be arranged on described grade and divide and fall air-flow jet pipe on the sidewall of room and charging aperture, described air-flow jet pipe is connected with described blower fan, described air-flow jet pipe central symmetry axis and described charging aperture central symmetry axis have an intersection point, and air-flow nozzle hole central symmetry axis is horizontal line;
Divide the bottom falling room to arrange several hoppers in described grade, by the hopper nearest apart from described charging aperture as first hopper, then the A/F of first hopper is W 1:
W 1=1.5*L 1
L 1 = Rρv a 2 2 h g * 3 16 γ d * ( 2 ( h + H ) g - 2 h g )
Wherein, L 1for falling into the horizontal flight distance of the material of first hopper, R is resistance coefficient, and ρ is atmospheric density, v afor air-flow absolute velocity, h is air-flow nozzle hole diameter, and H is the vertical height that charging aperture to grade divides the bottom falling room, and γ is the density of material, and d is the material particular diameter of screening;
The diameter h of described air-flow nozzle hole is 8-30 times of material particles average diameter.
2. a kind of material grading apparatus according to claim 1, it is characterized in that, divide the point of interface of the bottom falling room as initial point in the vertical straight line at described air-flow nozzle exit place and grade, the A/F of N number of hopper is the distance between the distalis of N number of hopper and nearside point;
The distance of nearside point and initial point is Tn:T n=(L n+ L n-1n>=2)/2
Namely the nearside point position of N number of hopper is the horizontal flight distance that falls into the material of N number of hopper and the half of horizontal flight distance sum of material falling into N-1 hopper;
The distance of distalis and initial point is Yn:Y n=(3L n-L n-1n>=2)/2;
The distalis position of N number of hopper is 3 times of horizontal flight distances falling into the material of N number of hopper and the half of difference of horizontal flight distance of material falling into N-1 hopper.
3. a kind of material grading apparatus according to claim 1, is characterized in that, the integral thickness of described material is 10-20 times of material average grain diameter.
4. a kind of material grading apparatus according to claim 1, is characterized in that, described grade divides the afterbody falling room to arrange deduster, and the bottom of described deduster arranges ash bucket.
5. a kind of material grading apparatus according to claim 4, is characterized in that, described deduster and described grade divide the opposite end falling room link to arrange pipeline to be connected to described blower fan.
6. a kind of material grading apparatus according to claim 2, is characterized in that, the grade minute between hopper distalis and next hopper nearside point is fallen mid point bottom room and arranged baffle plate.
CN201310144994.XA 2013-04-24 2013-04-24 A kind of material grading apparatus Active CN103264016B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310144994.XA CN103264016B (en) 2013-04-24 2013-04-24 A kind of material grading apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310144994.XA CN103264016B (en) 2013-04-24 2013-04-24 A kind of material grading apparatus

Publications (2)

Publication Number Publication Date
CN103264016A CN103264016A (en) 2013-08-28
CN103264016B true CN103264016B (en) 2015-09-30

Family

ID=49007702

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310144994.XA Active CN103264016B (en) 2013-04-24 2013-04-24 A kind of material grading apparatus

Country Status (1)

Country Link
CN (1) CN103264016B (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107008539B (en) * 2017-05-24 2022-10-25 湖北馥雅食品科技有限公司 Low-temperature pulverizer for high-grease materials
CN107138414B (en) * 2017-05-31 2019-06-25 深圳磐汩新能源有限公司 Particle classifying equipment
CN109954873A (en) * 2017-12-26 2019-07-02 中国科学院苏州纳米技术与纳米仿生研究所 Sieve the method and device of the laser spheroidization cemented carbide powder of varying particle size
CN109366782A (en) * 2018-06-08 2019-02-22 国宏中晶集团有限公司 A kind of preparation facilities and method of the thermoplastic sulfurized rubber containing waste-tyre rubber-powder
CN110947618A (en) * 2019-12-05 2020-04-03 芜湖鼎恒材料技术有限公司 Rectifier with adjustable go up and down
CN112121528B (en) * 2020-08-31 2021-10-22 山东省地矿工程勘察院 Mud pit with mud purifies and classification function
CN114558778B (en) * 2022-04-29 2022-07-05 中国空气动力研究与发展中心计算空气动力研究所 Micron-sized powder material controllable classification airflow sieve and screening method

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4339532A1 (en) * 1993-02-01 1994-08-04 Jetzlsberger Montage Gmbh Sepn. and grading of solids
DE19700471A1 (en) * 1997-01-09 1998-07-16 Mitteldeutsche Braunkohlengese Simple, horizontal air classification plant separating mineral matter from lignite
CN2387980Y (en) * 1999-09-27 2000-07-19 肖杰明 Frequency-changing horizontal winnow mill
CN201249173Y (en) * 2008-08-13 2009-06-03 云南驰宏锌锗股份有限公司 Totally-enclosed mobile catalyst screening machine
CN102744213A (en) * 2012-06-18 2012-10-24 同济大学 Mineral powder particle jet-flow separation device
CN203140280U (en) * 2013-02-03 2013-08-21 山东领航生物工程有限公司 Grading sorting machine
CN203184236U (en) * 2013-04-24 2013-09-11 湘潭瑞通球团有限公司 Material classification device

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4339532A1 (en) * 1993-02-01 1994-08-04 Jetzlsberger Montage Gmbh Sepn. and grading of solids
DE19700471A1 (en) * 1997-01-09 1998-07-16 Mitteldeutsche Braunkohlengese Simple, horizontal air classification plant separating mineral matter from lignite
CN2387980Y (en) * 1999-09-27 2000-07-19 肖杰明 Frequency-changing horizontal winnow mill
CN201249173Y (en) * 2008-08-13 2009-06-03 云南驰宏锌锗股份有限公司 Totally-enclosed mobile catalyst screening machine
CN102744213A (en) * 2012-06-18 2012-10-24 同济大学 Mineral powder particle jet-flow separation device
CN203140280U (en) * 2013-02-03 2013-08-21 山东领航生物工程有限公司 Grading sorting machine
CN203184236U (en) * 2013-04-24 2013-09-11 湘潭瑞通球团有限公司 Material classification device

Also Published As

Publication number Publication date
CN103264016A (en) 2013-08-28

Similar Documents

Publication Publication Date Title
CN103264016B (en) A kind of material grading apparatus
Kruggel‐Emden et al. Modeling of screening processes with the discrete element method involving non‐spherical particles
US9090413B2 (en) Potential fluidization device for conveying powder materials in a hyperdense bed
CN103406267B (en) Smalls jigging dry-dressing machine
AU2010352883A1 (en) Apparatus for pneumatic vacuum separation of bulk materials
CN108686956B (en) Powder particle sorting device and sorting method
Shinbrot et al. Triboelectrification and razorbacks: geophysical patterns produced in dry grains
CN203184236U (en) Material classification device
CN103934199A (en) Environment-friendly dry type dust-free manufactured sand production device
CN204620430U (en) One selects powder classifying integrated machine
Yang et al. Dry beneficiation of fine coal using planar air jets
Djoković et al. Screening efficiency analysis of vibrosieves with the circular vibrations
CN1099318A (en) Vibration fluidized-bed dry sorting method and apparatus for fine coal
CN106552721B (en) It is centrifuged the dry method cull eliminator that drifts along
CN203304191U (en) Environment-friendly dry type dust-free machine-made sand production device
CN204892350U (en) Distributing device for shale shaker
CN206587917U (en) Centrifuge the dry method cull eliminator that drifts along
JP2008284533A (en) Classifier
JP4889745B2 (en) Electrostatic sorting apparatus and electrostatic sorting method
CN207126656U (en) Nonfluid ore dressing media set and ore separators
RU2403990C1 (en) Device for classification of under-sieve material (sand) of screen aspiration system
CN112517397A (en) Sorting method and sorting device
RU166693U1 (en) DEVICE FOR SEPARATION OF GRAIN AND OTHER BULK MATERIALS
CN215141906U (en) Device for removing heavy metal in fly ash
CN211056010U (en) Vibrating feeder capable of realizing bidirectional feeding

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant