CN203091042U - Powder material preparation device - Google Patents

Powder material preparation device Download PDF

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Publication number
CN203091042U
CN203091042U CN 201320108645 CN201320108645U CN203091042U CN 203091042 U CN203091042 U CN 203091042U CN 201320108645 CN201320108645 CN 201320108645 CN 201320108645 U CN201320108645 U CN 201320108645U CN 203091042 U CN203091042 U CN 203091042U
Authority
CN
China
Prior art keywords
powder concentrator
elevator
dynamic powder
material preparation
discharging opening
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.)
Expired - Fee Related
Application number
CN 201320108645
Other languages
Chinese (zh)
Inventor
李立华
曹酒毓
胡若美
张伟业
赵俊
陈幼荣
蒋晓臻
何剑毅
金利国
李坤和
尤炳松
吴云龙
陆永刚
朱方平
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.)
South Cement Co Ltd
Nanjing Kisen International Engineering Co Ltd
Original Assignee
South Cement Co Ltd
Nanjing Kisen International Engineering 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 South Cement Co Ltd, Nanjing Kisen International Engineering Co Ltd filed Critical South Cement Co Ltd
Priority to CN 201320108645 priority Critical patent/CN203091042U/en
Application granted granted Critical
Publication of CN203091042U publication Critical patent/CN203091042U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a powder material preparation device. The powder material preparation device comprises a conveyor, a dynamic powder concentrator, a vertical mill and a cyclone dust collector, wherein a material inlet of the conveyor is arranged at a charging port of the dynamic powder concentrator; a charging port of a first lifer is formed at a discharging port of the vertical mill; a discharging port of the first lifter is formed at a charging hole of the dynamic powder concentrator; a charging port of a second lifter is formed at a discharging port of the dynamic powder concentrator; the cyclone dust collector is arranged at a fine powder discharging port of the dynamic powder concentrator; and a discharging port of the second lifter is arranged at the charging port of the vertical mill.

Description

A kind of granular material preparation facilities
Technical field
The utility model relates to a kind of material preparation facilities and method thereof, particularly a kind of granular material preparation facilities and method thereof.
Background technology
In the process of cement or cement raw meal preparation, common employing tube mill mill cement or cement slurry, because tube mill ontological existence installed power height, noise is big, grinding efficiency is not high, causes the tube mill production system all to exist efficient low, the shortcoming that energy consumption is high.
The utility model content
In order to solve problems of the prior art, the purpose of this utility model is to provide a kind of energy-conservation, granular material preparation facilities and method thereof efficiently.
In order to achieve the above object, the utility model is by the following technical solutions: a kind of granular material preparation facilities, comprise conveyer, dynamic powder concentrator, Vertical Mill and rotoclone collector, the discharge end of described conveyer is located at the feeding mouth place of dynamic powder concentrator, described Vertical Mill the discharging opening place be provided with the charging aperture of first elevator, the discharging opening of described first elevator is located at the charging aperture place of dynamic powder concentrator, the meal discharging opening place of described dynamic powder concentrator is provided with the charging aperture of second elevator, the fine powder discharging opening place of described dynamic powder concentrator is provided with rotoclone collector, and the discharging opening of described second elevator is located at the charging aperture place of Vertical Mill.The feeding end of described conveyer is provided with tramp iron separator.
A kind of granular material preparation method, its step comprises:
1) material is delivered into device from the feeding end of conveyer, material carries out deironing through tramp iron separator to be handled, and execution in step 2 afterwards);
2) utilize dynamic powder concentrator to carry out grain thickness and separate, finished product directly choosing walks to enter rotoclone collector, and then this method finishes, and remaining coarse fodder enters second elevator;
3) utilize second elevator, coarse fodder enters and carries out grinding in the Vertical Mill, and execution in step 4 afterwards);
4) coarse fodder after utilizing first elevator with grinding is sent dynamic powder concentrator to, and execution in step 2 afterwards).
Adopt technique scheme, the utlity model has following beneficial effect: material enters dynamic powder concentrator through conveyer and carries out the grain thickness separation, the satisfactory finished product of fineness directly choosing is walked warehouse-in, remaining coarse fodder enters the Vertical Mill grinding, material behind the Vertical Mill grinding enters dynamic powder concentrator classification once more, so forms the circle streaming system.This material preparation system flow process is simple, and system equipment is few, and energy consumption is low, and Operation and Maintenance is simple, has improved production efficiency.
Description of drawings
Fig. 1 is the structural representation of a kind of granular material preparation facilities of the utility model.
Fig. 2 is a kind of granular material preparation method of the utility model schematic flow sheet.
Among the figure: 1, tramp iron separator; 2, conveyer; 3, dynamic powder concentrator; 4, second elevator; 5, rotoclone collector; 6, Vertical Mill; 7, first elevator.
The specific embodiment
Below in conjunction with accompanying drawing and example, the utility model is described in further detail.
As shown in Figure 1, a kind of granular material preparation facilities, comprise conveyer 2, dynamic powder concentrator 3, Vertical Mill 6 and rotoclone collector 5, the discharge end of described conveyer 2 is located at the feeding mouth place of dynamic powder concentrator 3, described Vertical Mill 6 the discharging opening place be provided with the charging aperture of first elevator 7, the discharging opening of described first elevator 7 is located at the charging aperture place of dynamic powder concentrator 3, the meal discharging opening place of described dynamic powder concentrator 3 is provided with the charging aperture of second elevator 4, the fine powder discharging opening place of described dynamic powder concentrator 3 is provided with rotoclone collector 5, and the discharging opening of described second elevator 4 is located at the charging aperture place of Vertical Mill 6.The feeding end of described conveyer 2 is provided with tramp iron separator 1.
As shown in Figure 2, a kind of granular material preparation method, its step comprises:
1) material is delivered into device from the feeding end of conveyer 2, material carries out deironing through tramp iron separator 1 to be handled, and execution in step 2 afterwards);
2) utilize dynamic powder concentrator 3 to carry out grain thickness and separate, finished product directly choosing walks to enter rotoclone collector 5, and then this method finishes, and remaining coarse fodder enters second elevator 4;
3) utilize second elevator 4, coarse fodder enters and carries out grinding in the Vertical Mill 6, and execution in step 4 afterwards);
4) utilize first elevator 7 to send the coarse fodder behind the grinding to dynamic powder concentrator 3, execution in step 2 afterwards).
In the said process, Vertical Mill 6 self does not drive attitude powder concentrator 3, and material enters in the mill, directly all discharges outside the mill after milling, and the material thickness grating after milling is reasonable, and the classification that more helps dynamic powder concentrator 3 is handled.Native system is avoided the tube mill that uses energy consumption the highest, can significantly reduce the energy consumption in the whole grinding process, is a kind of granular material preparation method of energy saving economy.

Claims (2)

1. granular material preparation facilities, comprise conveyer, dynamic powder concentrator, Vertical Mill and rotoclone collector, it is characterized in that the discharge end of described conveyer is located at the feeding mouth place of dynamic powder concentrator, described Vertical Mill the discharging opening place be provided with the charging aperture of first elevator, the discharging opening of described first elevator is located at the charging aperture place of dynamic powder concentrator, the meal discharging opening place of described dynamic powder concentrator is provided with the charging aperture of second elevator, the fine powder discharging opening place of described dynamic powder concentrator is provided with rotoclone collector, and the discharging opening of described second elevator is located at the charging aperture place of Vertical Mill.
2. a kind of granular material preparation facilities according to claim 1 is characterized in that the feeding end of described conveyer is provided with tramp iron separator.
CN 201320108645 2013-03-11 2013-03-11 Powder material preparation device Expired - Fee Related CN203091042U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320108645 CN203091042U (en) 2013-03-11 2013-03-11 Powder material preparation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320108645 CN203091042U (en) 2013-03-11 2013-03-11 Powder material preparation device

Publications (1)

Publication Number Publication Date
CN203091042U true CN203091042U (en) 2013-07-31

Family

ID=48842486

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320108645 Expired - Fee Related CN203091042U (en) 2013-03-11 2013-03-11 Powder material preparation device

Country Status (1)

Country Link
CN (1) CN203091042U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103127995A (en) * 2013-03-11 2013-06-05 南京凯盛国际工程有限公司 Powder material preparation device and method thereof
CN103750343A (en) * 2014-02-08 2014-04-30 张文墩 Zero-pollution preparation method and processing equipment for marine biological calcium powder product

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103127995A (en) * 2013-03-11 2013-06-05 南京凯盛国际工程有限公司 Powder material preparation device and method thereof
CN103750343A (en) * 2014-02-08 2014-04-30 张文墩 Zero-pollution preparation method and processing equipment for marine biological calcium powder product

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130731

Termination date: 20210311

CF01 Termination of patent right due to non-payment of annual fee