CN205253293U - Super powder production system - Google Patents
Super powder production system Download PDFInfo
- Publication number
- CN205253293U CN205253293U CN201521017758.2U CN201521017758U CN205253293U CN 205253293 U CN205253293 U CN 205253293U CN 201521017758 U CN201521017758 U CN 201521017758U CN 205253293 U CN205253293 U CN 205253293U
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- CN
- China
- Prior art keywords
- ball mill
- grader
- collector
- elevator
- production system
- 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
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- Crushing And Grinding (AREA)
- Disintegrating Or Milling (AREA)
Abstract
The utility model provides a super powder production system, a serial communication port, include through the consecutive following part of conveyer belt: breaker (1): be used for carrying out the breakage with the material, lifting machine (2): a ball mill is delivered to to the material for inciting somebody to action it is broken good, ball mill (3): be used for grinding the material and smash, discharging material silo (4), a material for storing grind and smash, grader (5): be used for carrying out the fractional separation with the material, collector (6): be used for collecting qualified material, wherein, grader (5) lower extreme and ball mill (3) link to each other for again, grind unqualified material. The utility model discloses a super powder production system can prepare the high -purity super powder, but its high productivity, with low costs.
Description
Technical field
The utility model relates to a kind of system for producing micropowder, belongs to crushing material technical field.
Background technology
While utilizing powder compacting manufacture component, powder reaches ultra-fine degree often makes parts have very good characteristic. For example manufacture high temperature resistant, to have high intensity chemical tool (as cutter, turbo blade), need to adopt superfine powder to carry out sintering after moulding. A kind of formulation of powdery commercial dye. Its particle is very tiny evenly. Claim again pigment pad dyeing fine powder. Finger can be directly used in the reducing dye kind of pigment pad dyeing technique.
Superfine powder can be divided into comminuting method and the large class of synthetic method two. Comminuting method is by the melt atomization of large volume or fine particles (airflow milling pulverizing), synthetic method is to form particle by atom or molecule nucleation and growth process, wherein evaporation gasification one condensation method is the main method of preparing high-purity superfine powder, but its productivity ratio is low, cost is high.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art part, and a kind of system for producing micropowder is provided.
System for producing micropowder of the present utility model, comprise be connected successively by conveyer belt as lower component:
Disintegrating machine (1): for material is carried out to fragmentation;
Elevator (2): for the good material of fragmentation is delivered to ball mill;
Ball mill (3): for material is ground;
Discharge bin (4); For storing the material grinding;
Grader (5): for material is carried out to classification separation;
Collector (6): for collecting qualified material;
Wherein, described grader (5) lower end is connected with ball mill (3), for underproof material is re-started to grinding.
Preferably,
Described disintegrating machine (1) is jaw crusher;
Described elevator (2) is bucket elevator;
Described ball mill (3) is ultra-fine ball mill;
Described grader (5) is shunting micro powder sorting machine;
Described collector (6) is cyclone collector.
The utility model course of work is as follows: material is through after disintegrating machine (1) fragmentation, enter ball mill (3) by elevator (2), ball mill (3) carries out impact comminution and grinds material, material after pulverizing enters grader (5) through discharge bin (4) and separates, realize the separation of thickness powder, qualifiedly collected by collector (6), underproofly reenter ball mill (3) by grader (5) lower end and pulverize.
System for producing micropowder of the present utility model can be prepared high-purity superfine powder, but its productivity ratio is high, cost is low.
Brief description of the drawings
Fig. 1 is structure chart of the present utility model.
Wherein, 1 is disintegrating machine, and 2 is elevator, and 3 is ball mill, and 4 is discharge bin, and 5 is grader, and 6 is collector.
Detailed description of the invention
As shown in Figure 1, system for producing micropowder of the present utility model, comprise be connected successively by conveyer belt as lower component:
Disintegrating machine (1): for material is carried out to fragmentation;
Elevator (2): for the good material of fragmentation is delivered to ball mill;
Ball mill (3): for material is ground;
Discharge bin (4); For storing the material grinding;
Grader (5): for material is carried out to classification separation;
Collector (6): for collecting qualified material;
Wherein, described grader (5) lower end is connected with ball mill (3), for underproof material is re-started to grinding.
Described disintegrating machine (1) is jaw crusher;
Described elevator (2) is bucket elevator;
Described ball mill (3) is ultra-fine ball mill;
Described grader (5) is shunting micro powder sorting machine;
Described collector (6) is cyclone collector.
The utility model course of work is as follows: material is through after disintegrating machine (1) fragmentation, enter ball mill (3) by elevator (2), ball mill (3) carries out impact comminution and grinds material, material after pulverizing enters grader (5) through discharge bin (4) and separates, realize the separation of thickness powder, qualifiedly collected by collector (6), underproofly reenter ball mill (3) by grader (5) lower end and pulverize.
Claims (2)
1. a system for producing micropowder, is characterized in that, comprise be connected successively by conveyer belt as lower component:
Disintegrating machine (1): for material is carried out to fragmentation;
Elevator (2): for the good material of fragmentation is delivered to ball mill;
Ball mill (3): for material is ground;
Discharge bin (4); For storing the material grinding;
Grader (5): for material is carried out to classification separation;
Collector (6): for collecting qualified material;
Wherein, described grader (5) lower end is connected with ball mill (3), for underproof material is re-started to grinding.
2. system for producing micropowder according to claim 1, is characterized in that,
Described disintegrating machine (1) is jaw crusher;
Described elevator (2) is bucket elevator;
Described ball mill (3) is ultra-fine ball mill;
Described grader (5) is shunting micro powder sorting machine;
Described collector (6) is cyclone collector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521017758.2U CN205253293U (en) | 2015-12-10 | 2015-12-10 | Super powder production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521017758.2U CN205253293U (en) | 2015-12-10 | 2015-12-10 | Super powder production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205253293U true CN205253293U (en) | 2016-05-25 |
Family
ID=55994845
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521017758.2U Expired - Fee Related CN205253293U (en) | 2015-12-10 | 2015-12-10 | Super powder production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205253293U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106111532A (en) * | 2016-06-28 | 2016-11-16 | 四川省汉源化工总厂 | A kind of stage division of feed-level calcium biphosphate |
| CN106220274A (en) * | 2016-07-25 | 2016-12-14 | 南京百阳垦生物技术有限责任公司 | Pure natural plant growth propellant and preparation method thereof |
-
2015
- 2015-12-10 CN CN201521017758.2U patent/CN205253293U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106111532A (en) * | 2016-06-28 | 2016-11-16 | 四川省汉源化工总厂 | A kind of stage division of feed-level calcium biphosphate |
| CN106220274A (en) * | 2016-07-25 | 2016-12-14 | 南京百阳垦生物技术有限责任公司 | Pure natural plant growth propellant and preparation method thereof |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160525 Termination date: 20171210 |