CN2147900Y - Supersonic airflow superfine crushing classifier - Google Patents

Supersonic airflow superfine crushing classifier Download PDF

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Publication number
CN2147900Y
CN2147900Y CN 93216762 CN93216762U CN2147900Y CN 2147900 Y CN2147900 Y CN 2147900Y CN 93216762 CN93216762 CN 93216762 CN 93216762 U CN93216762 U CN 93216762U CN 2147900 Y CN2147900 Y CN 2147900Y
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China
Prior art keywords
powder
pulverizing
grader
supersonic
crushing
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Expired - Fee Related
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CN 93216762
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Chinese (zh)
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王宝芬
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Individual
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Individual
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Publication of CN2147900Y publication Critical patent/CN2147900Y/en
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Abstract

A supersonic airflow superfine grinding classifier is a processing device for superfine grinding of materials. It consists of a crushing device and a powder grading device. A plurality of supersonic jet flows are arranged in a crushing chamber of the crushing device, the jet flows carry materials injected into the crushing chamber from a funnel, the materials are collided at the intersection of the jet flows to realize material crushing, the crushed powder enters a grading device and is graded according to the size of powder particles under the action of centrifugal force, the powder meeting the requirements enters a pipeline connected with a collector, and the powder not meeting the requirements is thrown into the crushing chamber for crushing. Its advantages are no abrasion of spray tube, uniform fineness of powder, high pulverizing efficiency and low energy consumption, and is suitable for pulverizing the brittle material with Mohs hardness of 1-10.

Description

Supersonic airstream superfine milling classer
What the utility model was related is the ultra tiny pulverizing grader of a kind of supersonic airstream, and it is the process equipment that object is carried out ultra tiny pulverizing.
For satisfying the needs of modern high technology, the ultra tiny pulverizing technology of object processing is developed rapidly.The common mechanical crushing technology can only make the powder granule diameter reach about 45 microns, and ultra tiny pulverizing technology then can make diameter of particle less than 10 microns.The realization of the broken pulverizer of micropowders in the past is by treating that comminuting matter is blended in the compressed air, and material quickens with the supersonic nozzle of airflow passes particular design, is ejected in pulverizing chamber on the metallic target wall, and material is by bump and fragmentation.Then, obtain powder through vertical grading plant again.The weak point of this equipment is object with the air jet pipe of flowing through, and nozzle wall is easy to wear, and object strikes and corrode the target wall makes powder contain jet pipe and target wall material impurity in addition, can not meet the demands; In addition, it is also inhomogeneous that powder enters the selected fineness of powder of vertical grader.
The purpose of this utility model is to provide a kind of supersonic airstream ultra tiny pulverizing grader, and it can realize that jet pipe does not have wearing and tearing, and powder fineness is even, the crush efficiency height.
The purpose of this utility model is to realize like this, with the supersonic nozzle that three or three or more in opposite directions be provided with of compressed air importing through particular design, in pulverizing chamber, form several bursts of supersonic jets of respective number, these jets carry the material that is injected pulverizing chamber by loading hopper, clash into the material fragmentation of realization mutually in jet intersection, powder after the fragmentation enters horizontal grader, under action of centrifugal force, by the granular size classification, in the pipeline that the satisfactory super-fine powder of particle diameter enters with gatherer is connected, the undesirable powder of particle diameter then is thrown into pulverizing chamber and pulverizes.Therefore, powder fineness is high and even, the crush efficiency height.
Below accompanying drawing is illustrated
Fig. 1---the utility model structural representation
Fig. 2---jet pipe distributed architecture schematic diagram (A-A view)
Fig. 3---grader structural representation (B-B view)
Wherein, 1-reducing mechanism 9-blade
2-pulverizing chamber 10-stator
3-jet pipe 11-rotor
4-annular compression air duct 12-grader motor
5-pulverizing chamber material inlet 13-belt and wheel
Powder outlet conduit after the 6-Materials hopper 14-classification
The outlet of 7-pulverizing chamber powder
The 8-grading plant
Below in conjunction with accompanying drawing structure of the present utility model is specified.
Fig. 1, the ultra tiny pulverizing grader of supersonic airstream are made up of reducing mechanism (1) and grading plant (8).Pulverizing chamber (2) in the reducing mechanism (1) is a cylindrical metal tube, and inside is cavity.Be with annular compression air duct (4) outside the bottom of pulverizing chamber (2), be connected with the supersonic nozzle through particular design (3) that is provided with in opposite directions more than three or three thereon, pulverizing chamber (2) inwall is passed in the outlet of these supersonic nozzles.For being mutually 120 ° of distributions, four jet pipes are mutually 90 ° of symmetrical distributions in the layout of annular compression air duct (4) for three jet pipes, and six become 60 ° to distribute or the jet pipe more than six is even cloth.The given embodiment of the utility model adopts four jet pipe distribution forms (as Fig. 2).Also have material inlet (5) at pulverizing chamber (2) sidewall, this charging aperture is located at the nozzle exit top, and Materials hopper (6) injects pulverizing chamber, and injection technique is general prior art, and this paper no longer describes.Material does not directly pass through jet pipe, has avoided wearing and tearing in the jet pipe.At the pulverizing chamber inner chamber, the material that is injected pulverizing chamber by loading hopper (6) is carried in several burst supersonic jets identical with jet pipe quantity, and intersection clashes into mutually at jet, realizes the material fragmentation.Powder after the pulverizing flows to grading plant.
The grading plant of powder (8) is on pulverizing chamber (2) top, and it is made up of stator (10) and rotor (11).The stator of grading plant (or rotor) axis is vertical mutually with the center line of pulverizing chamber (2), is called horizontal grader again.The blade (9) of even cloth some and angle on the circumference at stator in Fig. 3 (10) two ends, there is wheel paddy at rotor (11) two ends, the left end wheel be solid, right-hand member wheel for hollow, some and angle two blades (9) are taken turns paddy with two ends and are linked as an integral body.Motor (12) is installed the upper end with grader, and the rotation of motor is rotated by the rotor (11) that belt and wheel (13) drive grader.
When powder enters into grading plant (8), powder enters the rotor middle cavity by the passage of the blade (9) of rotor, because classification motor (12) drives rotor (11) and does rotation at a high speed, its rotating speed is 3000-30000 rev/min, thereby powder is under the effect of power, by the granular size classification, the powder grain is satisfactory by the hollow pipeline (14) that is connected with the gatherer (not shown) that enters of rotor (11) right-hand member, and undesirable powder is thrown into pulverizing chamber (2) row pulverizing again.Therefore, resulting powder fineness is even.Rotor (11) velocity of rotation is high more, and the powder average grain diameter is also just more little after the classification, even can reach submicron order.
The utility model has the advantage of object without jet pipe, jet pipe does not have wearing and tearing, adopts horizontal grader in addition, powder impurity mixed volume is few, fineness is evenly distributed, the crush efficiency height, the power consumption low. The brittle material that is applicable to Mohs' hardness 1-10 level is pulverized, and is particularly useful for hard abrasive material such as carborundum and impurity content and asks extremely tight spy to expect such as fluorescent material special ceramics etc.

Claims (4)

1, the ultra tiny pulverizing grader of supersonic airstream is made up of reducing mechanism and grading plant, it is characterized in that:
The pulverizing chamber of a, reducing mechanism (2) is a cylindrical metal tube, inside is cavity, be with annular compression air duct (4) outside the bottom of pulverizing chamber (2), on pipeline, be connected with four supersonic nozzles through particular design (3) that are provided with in opposite directions, the nozzle exit end passes the pulverizing chamber inwall, its top is provided with material inlet (5)
B, grading plant (8) are arranged on pulverizing chamber (2) top, it is made up of stator (10) and rotor (11), around stator (10), go up the blade (9) that even cloth has some and angle, there is wheel paddy at rotor (11) two ends, the left end wheel is solid, be linked as an integral body by the blade (9) that certain angle is installed, its right-hand member wheel is hollow.
2, the ultra tiny pulverizing grader of supersonic airstream according to claim 1 is characterized in that being provided with in opposite directions four jet pipes and is mutually 90 ° of symmetrical distributions.
3, the ultra tiny pulverizing grader of supersonic airstream according to claim 1 is characterized in that being provided with in opposite directions three jet pipes and becomes 120 ° of distributions.
4, the ultra tiny pulverizing grader of supersonic airstream according to claim 1 is characterized in that the jet pipe that is provided with in opposite directions can be six and becomes 60 ° of distributions.
CN 93216762 1993-05-15 1993-05-15 Supersonic airflow superfine crushing classifier Expired - Fee Related CN2147900Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 93216762 CN2147900Y (en) 1993-05-15 1993-05-15 Supersonic airflow superfine crushing classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 93216762 CN2147900Y (en) 1993-05-15 1993-05-15 Supersonic airflow superfine crushing classifier

Publications (1)

Publication Number Publication Date
CN2147900Y true CN2147900Y (en) 1993-12-01

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CN 93216762 Expired - Fee Related CN2147900Y (en) 1993-05-15 1993-05-15 Supersonic airflow superfine crushing classifier

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CN (1) CN2147900Y (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1295020C (en) * 2004-03-05 2007-01-17 昆山密友实业有限公司 Ultra micro air flow pulverizer set with inert gas shielded
CN101370600B (en) * 2006-02-24 2011-10-05 太平洋水泥株式会社 Centrifugal air classification machine
CN101524659B (en) * 2008-03-03 2012-10-24 深圳市易宝通粉煤灰科技发展有限公司 Pipe gas flow crushing device
CN101524658B (en) * 2008-03-03 2012-10-24 深圳市易宝通粉煤灰科技发展有限公司 Fly ash pipe gas flow crushing process
CN104368528A (en) * 2014-11-17 2015-02-25 王树波 Separator capable of controlling particle size distribution in high-precision mode
CN107837923A (en) * 2017-10-24 2018-03-27 廊坊新龙立机械制造有限公司 A kind of fluidized bed air flow crusher and airflow pulverization method
CN109013036A (en) * 2018-07-23 2018-12-18 湖北冯家山硅纤有限公司 A kind of silicon fibre feed separation processing method
CN114247542A (en) * 2021-12-24 2022-03-29 西华大学 Superfine slay miropowder equipment

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1295020C (en) * 2004-03-05 2007-01-17 昆山密友实业有限公司 Ultra micro air flow pulverizer set with inert gas shielded
CN101370600B (en) * 2006-02-24 2011-10-05 太平洋水泥株式会社 Centrifugal air classification machine
CN101524659B (en) * 2008-03-03 2012-10-24 深圳市易宝通粉煤灰科技发展有限公司 Pipe gas flow crushing device
CN101524658B (en) * 2008-03-03 2012-10-24 深圳市易宝通粉煤灰科技发展有限公司 Fly ash pipe gas flow crushing process
CN104368528A (en) * 2014-11-17 2015-02-25 王树波 Separator capable of controlling particle size distribution in high-precision mode
CN107837923A (en) * 2017-10-24 2018-03-27 廊坊新龙立机械制造有限公司 A kind of fluidized bed air flow crusher and airflow pulverization method
CN109013036A (en) * 2018-07-23 2018-12-18 湖北冯家山硅纤有限公司 A kind of silicon fibre feed separation processing method
CN114247542A (en) * 2021-12-24 2022-03-29 西华大学 Superfine slay miropowder equipment
CN114247542B (en) * 2021-12-24 2023-02-03 西华大学 Superfine slay miropowder equipment

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C19 Lapse of patent right due to non-payment of the annual fee
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