CN205914222U - Superfine miropowder grinds machine - Google Patents
Superfine miropowder grinds machine Download PDFInfo
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- CN205914222U CN205914222U CN201620909976.5U CN201620909976U CN205914222U CN 205914222 U CN205914222 U CN 205914222U CN 201620909976 U CN201620909976 U CN 201620909976U CN 205914222 U CN205914222 U CN 205914222U
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- cyclosizer
- grinding
- main frame
- host computer
- slip
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Abstract
The utility model discloses a superfine miropowder grinds machine, include: grinding the host computer, being equipped with host computer feed inlet and host computer discharge gate on the grinding host computer, host computer feed inlet department is equipped with first valve, material oar jar, ground paste are irritated and are linked together with the host computer discharge gate through grinding the back flow, and the discharge gate department that the ground paste was irritated is equipped with the second valve, cyclosizer, cyclosizer are equipped with feed inlet, overflow mouth and underflow opening, and the discharge gate that cyclosizer's feed inlet was irritated through first conveying pipe and ground paste is linked together, is equipped with the shurry pump on first conveying pipe, and cyclosizer's underflow opening is linked together through second conveying pipe and host computer feed inlet, and cyclosizer's overflow mouth is irritated with the ground paste through whirl feed back pipe and is linked together. The utility model discloses a mode that superfine miropowder grinds machine ground through hierarchical circulation for grinding speed, improved the grinding efficiency, reduced the energy resource consumption, simultaneously, effectively solved the kibbling problem of crossing.
Description
Technical field
This utility model is related to milling apparatus technical field, specifically, is a kind of super fine grinder.
Background technology
At present, the micropowder processing within one micron of super fine, especially granularity typically adopts wet recycle to grind, that is,
Slip after grinding main frame and grinding, after the discharging opening grinding main frame flows out, is mixed with the slip not ground, then leads to again
The charging aperture crossing grinding main frame returns in grinding main frame, thus in grinding initial stage, because the fineness ratio of micropowder is larger, grinding rate
Hurry up, efficiency high, but in latter stage, due to the reduction of powder size, there is considerable fraction of micropowder to reach the granularity of regulation,
Lead to micropowder grinding rate slow, efficiency is low, big energy-consuming, worse super fine crosses pulverizing seriously.
Content of the invention
Technical problem to be solved in the utility model is: provide a kind of grinding rate fast, grinding efficiency is high, power consumption is few,
It can be avoided that crossing the super fine grinder pulverized.
For solving above-mentioned technical problem, the technical solution of the utility model is:
Super fine grinder, comprising: grind main frame, described grinding main frame is provided with main frame charging aperture and main frame discharging
Mouthful, it is provided with the first valve at described main frame charging aperture；Material oar tank, described slip fills by grinding return duct and described main frame discharging
Mouth is connected, and the discharge outlet that described slip fills is provided with the second valve；Cyclosizer, described cyclosizer is provided with charging
Mouthful, overfall and underflow opening, the discharging opening phase that the charging aperture of described cyclosizer is filled with described slip by the first feed pipe
Connection, is provided with shurry pump on described first feed pipe, the underflow opening of described cyclosizer pass through the second feed pipe with described
Main frame charging aperture is connected, and the overfall of described cyclosizer is passed through eddy flow feed back pipe and is connected with the filling of described slip.
After employing technique scheme, the beneficial effects of the utility model are:
Main frame discharging opening and slip due to grinding main frame fill and are connected, the discharging opening that slip fills and with cyclosizer
Charging aperture is connected, and the overfall of cyclosizer is connected with material oar tank, the underflow opening of cyclosizer and main frame charging aperture
It is connected；During grinding, the slip after grinding enters slip filling from main frame discharging opening, mixes with the slip not ground, Ran Houjin
Enter in cyclosizer, be classified according to granularity in cyclosizer, the slip reaching designated size is entered by overfall
In pan feeding oar tank, will not enter in grinding main frame and be ground, the slip being only not reaching to designated size passes through cyclone classification
The underflow opening of machine, main frame charging aperture enter and grind main frame, being ground, thus accelerating grinding rate, improve grinding efficiency,
Reduce energy resource consumption, meanwhile, solve the problems, such as that super fine crosses pulverizing serious.
Brief description
Fig. 1 is the structural representation of super fine grinder of the present utility model；
In figure: 1- grinds main frame；1a- main frame charging aperture；1b- main frame discharging opening；2- grinds feed back pipe；3- expects oar tank；4-
First feed pipe；5- shurry pump；6- second feed pipe；7- cyclosizer；71- overfall；72- underflow opening；8- eddy flow feed back
Pipe；9- first valve；10- second valve.
Specific embodiment
In order that the purpose of this utility model, technical scheme and advantage become more apparent, below in conjunction with accompanying drawing and enforcement
Example, is further elaborated to this utility model.It should be appreciated that specific embodiment described herein is only in order to explain
This utility model, and it is not used in restriction this utility model.
As shown in figure 1, a kind of super fine grinder, including grinding main frame 1, grind main frame 1 and be provided with main frame charging aperture
1a and main frame discharging opening 1b, is provided with the first valve 9 at main frame charging aperture 1a；
Material oar tank 3, slip is filled 3 and is connected with main frame discharging opening 1b by grinding return duct 2, and slip fills 3 discharge outlet
It is provided with the second valve 10；
Cyclosizer 7, cyclosizer 7 is provided with charging aperture, overfall 71 and underflow opening 72, the entering of cyclosizer 7
Material mouth is connected by the discharging opening that the first feed pipe 4 fills 3 with slip, is provided with shurry pump 5, eddy flow divides on the first feed pipe 4
The underflow opening 72 of level machine 7 is connected with main frame charging aperture 1b by the second feed pipe 6, and the overfall 71 of cyclosizer 7 passes through
Eddy flow feed back pipe 8 fills 3 with slip and is connected.
Carry out super fine attrition process when, especially for grinding of nonmetallic and silicon carbide super micro powder
When, first the super fine got ready slip is injected in material oar tank 3, and adds appropriate abrasive media by grinding in main frame 1,
It is then turned on the first valve 9, shurry pump 5, the second valve 10 and grind main frame 1, when the slip in material oar tank 3 flows through shurry pump 5,
Flow in cyclosizer 7 after shurry pump 5 pressurization speed-raising, according to grading in cyclosizer 7, reach regulation grain
The slip of degree passes through overfall 71 and eddy flow feed back pipe 8 flow in material oar tank 3, and the slip being not reaching to designated size passes sequentially through
The underflow opening 72 of cyclosizer 7 lower end, the second feed pipe 6, the second valve 10 and main frame charging aperture 1a flow to grinding main frame 1
In, the slip after ground main frame 1 grinding passes sequentially through main frame discharging opening 1b and grinding feed back pipe 2 flow in material oar tank 3, so that
In carrying out reclassification, grinding, so after the grinding of multiple circulation classification, the slip in material oar tank 3 entirely reaches regulation
Granularity.
Due to, during circular grinding each time, after slip is classified by cyclosizer 7, being only not reaching to regulation grain
The slip of degree flow in grinding main frame 1, thus accelerating grinding rate, improve grinding efficiency, reducing energy loss, with
When, effectively prevent the generation of the situation of pulverizing, and improve the qualification rate of product, reduce cost, especially for 0.5 micron
To 1 micron of product, it is possible to increase more than one times of grinding efficiency.
Super fine grinder of the present utility model is applied to the attrition process of carborundum, nonmetallic micropowder and powder body.
In sum, super fine grinder of the present utility model, by way of classification cycle is ground, accelerates grinding
Speed, improves grinding efficiency, meanwhile, efficiently solves the problems, such as to pulverize.
The above is the citing of this utility model preferred forms, and the part wherein do not addressed in detail is this area
The common knowledge of those of ordinary skill.Protection domain of the present utility model is defined by the content of claim, any based on this reality
The equivalent transformation being carried out with new technology enlightenment, also within protection domain of the present utility model.
Claims (1)
1. super fine grinder is it is characterised in that include:
Grind main frame, described grinding main frame is provided with main frame charging aperture and main frame discharging opening, at described main frame charging aperture, be provided with the
One valve；
Material oar tank, described slip is filled and is connected with described main frame discharging opening by grinding return duct, the discharging opening that described slip fills
Place is provided with the second valve；
Cyclosizer, described cyclosizer is provided with charging aperture, overfall and underflow opening, the charging aperture of described cyclosizer
It is connected by the discharging opening that the first feed pipe is filled with described slip, described first feed pipe is provided with shurry pump, described rotation
The underflow opening of current classifier is connected with described main frame charging aperture by the second feed pipe, and the overfall of described cyclosizer leads to
Overwinding is flowed back to expects pipe and is filled with described slip and is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620909976.5U CN205914222U (en) | 2016-08-19 | 2016-08-19 | Superfine miropowder grinds machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620909976.5U CN205914222U (en) | 2016-08-19 | 2016-08-19 | Superfine miropowder grinds machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205914222U true CN205914222U (en) | 2017-02-01 |
Family
ID=57871808
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620909976.5U Active CN205914222U (en) | 2016-08-19 | 2016-08-19 | Superfine miropowder grinds machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205914222U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107601708A (en) * | 2017-10-10 | 2018-01-19 | 成都信息工程大学 | A kind of Multi-functional effluent treatment unit |
| CN107640855A (en) * | 2017-10-10 | 2018-01-30 | 成都信息工程大学 | A kind of novel sewage treatment unit |
-
2016
- 2016-08-19 CN CN201620909976.5U patent/CN205914222U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107601708A (en) * | 2017-10-10 | 2018-01-19 | 成都信息工程大学 | A kind of Multi-functional effluent treatment unit |
| CN107640855A (en) * | 2017-10-10 | 2018-01-30 | 成都信息工程大学 | A kind of novel sewage treatment unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170303 Address after: 262500 Shandong, Shandong, Qingzhou Phoenix Road, No. 969, No. Patentee after: Qingzhou Yuxin Ceramic Material Co., Ltd. Address before: 262500 Shandong city of Weifang province Qingzhou City Linglong Mountain Road No. 4139 Patentee before: Yang Tianyu |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Super fine grinder Effective date of registration: 20170410 Granted publication date: 20170201 Pledgee: Qingzhou Shandong rural commercial bank Limited by Share Ltd Pledgor: Qingzhou Yuxin Ceramic Material Co., Ltd. Registration number: 2017990000285 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20200813 Granted publication date: 20170201 Pledgee: Qingzhou Shandong rural commercial bank Limited by Share Ltd. Pledgor: QINGZHOU YUXIN CERAMIC MATERIAL Co.,Ltd. Registration number: 2017990000285 |