CN204234166U - A kind of efficient pulverizing system - Google Patents

A kind of efficient pulverizing system Download PDF

Info

Publication number
CN204234166U
CN204234166U CN201420702507.7U CN201420702507U CN204234166U CN 204234166 U CN204234166 U CN 204234166U CN 201420702507 U CN201420702507 U CN 201420702507U CN 204234166 U CN204234166 U CN 204234166U
Authority
CN
China
Prior art keywords
charger
air
filter
batch charger
tail gas
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
CN201420702507.7U
Other languages
Chinese (zh)
Inventor
王海勇
王仲明
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.)
Jiangsu Bo Move New Materials Ltd By Share Ltd
Original Assignee
Jiangsu Boqian New Materials Co Ltd
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 Jiangsu Boqian New Materials Co Ltd filed Critical Jiangsu Boqian New Materials Co Ltd
Priority to CN201420702507.7U priority Critical patent/CN204234166U/en
Application granted granted Critical
Publication of CN204234166U publication Critical patent/CN204234166U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

The utility model discloses a kind of efficient pulverizing system, comprise charger, magazine-less system, air nozzle, airflow milling and tail gas collection system, charger is oscillating batch charger, and oscillating batch charger discharging opening is provided with filter.The utility model passes through the lattice-shaped filter increasing certain size at oscillating batch charger discharging end, to remove the large powder ball of part in metal powder.Adopt new-type oscillating batch charger to realize stable charging, ensure that production stability.This system also carries out cascade filtration, a part of qualified discharge to the air of discharge, recycling in another part air circulating vehicle, has and supplements air to either inside and reduce wetness action.

Description

A kind of efficient pulverizing system
Technical field
The utility model relates to a kind of crushing system with the various material of ultra-fine grinding and dispersing nanometer powder reuniting particle.
Technical background
In prior art, airflow milling crushing technology is conventional superfine technique, is widely used in the ultra-fine grinding of nonmetallic mineral, nano-powder and industrial chemicals.
Its operation principle is that material charger evenly feeds in raw material to airflow milling charging aperture, and magazine-less system afterbody is provided with air nozzle, is connected and ejects compressed air with compressed air.According to venturi injection principle, in charging aperture, material is compressed suction feed introduction, and is mixed to form with compressed air the crushing chamber that airflow milling is spurted in logistics.After logistics is entered crushing chamber by injection, be subject to being located at crushing chamber surrounding and pulverize repeatedly repeatedly the clashing into of the supersonic airstream that nozzle tangentially sprays, shear, and collide with the chamber wall of crushing chamber and upper and lower covers, rub, reach the object of pulverizing.In crushing process, the particle of different fineness, in swirling eddy, produce different centrifugal force, coarse granule is thrown toward periphery because suffered centrifugal force is greater than the active force of centripetal air-flow, continues to pulverize; By exhaust airstream band to discharging opening, entering collector by pipeline carries out gas solid separation because the active force of centripetal air-flow is greater than centrifugal force for the particle of qualified fineness, thus obtains finished product.Tail gas is drained through filter collector again.
Because of dried Nano metal powder exist larger powder ball, such large powder ball easily blocks airflow milling charging aperture affects charging, and if it directly enters in air-flow mill chamber, can not finally being affected product dispersiveness by disperseing completely, causing product defective.
Utility model content
The utility model object is the efficient pulverizing system providing a kind of automation, solves airflow milling charging aperture and is easily caused the problem of regurgitating by foreign matter or big particle blocking, provides stable feed system to realize balanced feeding in raw material and ensure that production stability.
A kind of efficient pulverizing system, comprises charger, magazine-less system, air nozzle, airflow milling and tail gas collection system, it is characterized in that: described charger is oscillating batch charger, and oscillating batch charger discharging opening is provided with filter.
Described oscillating batch charger controllable silicon halfwave rectifier is powered, and realizes the centralized Control of production process and automatically controls.
Described filter adopts lattice-shaped structure, sieves material.
Described tail gas collection system adopts two-stage filter, filters to reach the object that purifies air to tail gas, and system, by a part of tail gas supply workshop after purification, is supplemented and caused production scene lack of air because venturi injection causes and present negative pressure appearance.
The utility model beneficial effect:
The utility model passes through the lattice-shaped filter increasing certain size at oscillating batch charger discharging end, to remove the large powder ball of part in metal powder.Adopt new-type oscillating batch charger to realize stable charging, ensure that production stability.This system also carries out cascade filtration, a part of qualified discharge to the air of discharge, recycling in another part air circulating vehicle, has and supplements air to either inside and reduce wetness action.
Accompanying drawing explanation
Fig. 1 is the utility model structural front view.
In figure: 1, hopper, 2, oscillating batch charger, 3, filter, 4, air nozzle, 5, magazine-less system, 6, airflow milling, 7, crushing chamber, 8, dust-precipitator, 9, air-introduced machine, 10, filter collector, 11, filter collector, 12, muffler, 13, evacuated tube.
Detailed description of the invention
Below in conjunction with Fig. 1, the utility model is described further.
The utility model is the crushing system of the various material of a kind of ultra-fine grinding and dispersing nanometer powder reuniting particle, comprise: hopper 1, air-introduced machine 9, filter collector 10, filter collector 11, muffler 12, evacuated tube 13, filter 3 to be welded on oscillating batch charger on 2, air nozzle 4 is installed in magazine-less system 5, it is inner that crushing chamber 7 is positioned at airflow milling 6, and airflow milling discharging opening is connected on dust-precipitator 8 by pipeline.
Working method is that material is evenly fed in raw material to airflow milling 6 charging aperture from hopper by oscillating batch charger 2, and in charging aperture, material is compressed suction feed introduction, and is mixed to form with compressed air the crushing chamber 7 that airflow milling is spurted in logistics.After logistics is entered crushing chamber 7 by injection, be subject to being located at crushing chamber surrounding and pulverize repeatedly repeatedly the clashing into of the supersonic airstream that nozzle tangentially sprays, shear, and collide with the chamber wall of crushing chamber 7 and upper and lower covers, rub, reach the object of pulverizing.By exhaust airstream band to discharging opening, entering dust-precipitator by pipeline carries out gas solid separation because the active force of centripetal air-flow is greater than centrifugal force for the particle of qualified fineness, thus obtains finished product.Tail gas is again through filter collector dedusting emptying.
Oscillating batch charger 2 adopts Near resonance oscillating principle, powers by controllable silicon halfwave rectifier, in use infinitely can regulate feeding coal, achieves the centralized Control of production process and automatically controls.It also has the plurality of advantages such as volume is little, lightweight, operating cost is low.
Oscillating batch charger 2 feed opening adopts lattice-shaped structure to make, and grid size can make according to comminuting matter granular size.Have and sieving actoion is carried out to material, foreign matter or big particle are separated in trash receptacle, prevent its blocking airflow milling charging aperture, and to product, there is certain impurity removal function.
Native system adopts two-stage filter to exhaust collection, and secondary filter can adopt PE-M bag filter or clapboard type filter to tail gas filtering to reach the object that purifies air.

Claims (4)

1. an efficient pulverizing system, comprises charger, magazine-less system, air nozzle, airflow milling and tail gas collection system, it is characterized in that: described charger is oscillating batch charger, and oscillating batch charger discharging opening is provided with filter.
2. the system as claimed in claim 1, is characterized in that: described oscillating batch charger controllable silicon halfwave rectifier is powered, and realizes the centralized Control of production process and automatically controls.
3. the system as claimed in claim 1, is characterized in that: described filter adopts lattice-shaped structure, sieves material.
4. the system as claimed in claim 1, it is characterized in that: described tail gas collection system adopts two-stage filter, filter to reach the object that purifies air to tail gas, system, by a part of tail gas supply workshop after purification, is supplemented and is caused production scene lack of air because venturi injection causes and present negative pressure appearance.
CN201420702507.7U 2014-11-21 2014-11-21 A kind of efficient pulverizing system Active CN204234166U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420702507.7U CN204234166U (en) 2014-11-21 2014-11-21 A kind of efficient pulverizing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420702507.7U CN204234166U (en) 2014-11-21 2014-11-21 A kind of efficient pulverizing system

Publications (1)

Publication Number Publication Date
CN204234166U true CN204234166U (en) 2015-04-01

Family

ID=52763722

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420702507.7U Active CN204234166U (en) 2014-11-21 2014-11-21 A kind of efficient pulverizing system

Country Status (1)

Country Link
CN (1) CN204234166U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018051474A (en) * 2016-09-29 2018-04-05 日立金属株式会社 Dry pulverizer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018051474A (en) * 2016-09-29 2018-04-05 日立金属株式会社 Dry pulverizer

Similar Documents

Publication Publication Date Title
CN201988430U (en) Fluidized bed jet mill grader
CN204866103U (en) Novel high -efficient air current is broken device
CN208944323U (en) A kind of graphene Jet Mill
CN205236121U (en) Fluidized bed jet milling device
CN204412703U (en) Grain dust removal machine is inhaled in industry
CN208407160U (en) A kind of efficient micronizer
CN104826721B (en) System for preparing straw micro powder
CN102814222B (en) Continuous dry ball milling device
CN206935535U (en) A kind of complete milling device of silicon carbide ultrafine powder
CN208852994U (en) It is a kind of for producing the airslide disintegrating mill of pesticide
CN203304057U (en) Crushing production line with double dedusting
CN204710715U (en) A kind of ultra micro rice gas flow sizing machine being applied to dust removing
CN204234166U (en) A kind of efficient pulverizing system
CN202447180U (en) Material smashing device
CN210022402U (en) Air flow crushing device protected by gas
CN208894380U (en) A kind of medicinal herb grinder group
CN202962558U (en) Non-metallic mineral dry-process grinding and purification integrated machine
CN208527019U (en) A kind of catalyst fines classification recyclable device
CN102836766A (en) Circulating type jet mill and milling system thereof
CN105772197B (en) A kind of ultra tiny roller mill equipment production flow
CN206030304U (en) A device is smashed to old and useless rubber for reclaimed rubber processes usefulness
CN203209149U (en) Crushing production line with dual dedusting function
CN209061335U (en) Wet face head recovery system
CN103599858A (en) Pebble coal sorting and recycling system
CN103100494A (en) Spherical graphite superfine classifier

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP03 Change of name, title or address

Address after: 223800 Suqian province high tech Development Zone, Jiangshan Road, No. 23, No.

Patentee after: Jiangsu Bo move new materials Limited by Share Ltd

Address before: 223801 Huashan Road, Suyu Economic Development Zone, Jiangsu, No. 109, No.

Patentee before: Jiangsu Boqian New Materials Co., Ltd.