CN202893440U - Discharge system of ball grinder - Google Patents
Discharge system of ball grinder Download PDFInfo
- Publication number
- CN202893440U CN202893440U CN 201220548841 CN201220548841U CN202893440U CN 202893440 U CN202893440 U CN 202893440U CN 201220548841 CN201220548841 CN 201220548841 CN 201220548841 U CN201220548841 U CN 201220548841U CN 202893440 U CN202893440 U CN 202893440U
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- Prior art keywords
- membrane pump
- grinding chamber
- slurry
- valve
- diaphragm pump
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Abstract
The utility model provides a discharge system of a ball grinder. The discharge system of the ball grinder comprises a grinding cavity, a feeding hole, and a diaphragm pump, wherein the feeding hole is formed in the upper part of the grinding cavity; the diaphragm pump is tightly connected with top and bottom pipelines of the grinding cavity; the grinding cavity, the diaphragm pump and the pipelines form a closed loop; a grinding cavity valve is arranged on the pipeline between the bottom part of the grinding cavity and the diaphragm pump; a circulating valve is arranged on the pipeline between the top part of the grinding cavity and the diaphragm pump; and a discharge device is arranged at the lower part of the circulating valve, and the discharge device discharges the slurry through the diaphragm pump. Compared with the prior art, the circulating valve and the discharge device are arranged on the pipeline between the top part of the grinding cavity and the diaphragm pump; and the grinded slurry is output by pressure effect of the diaphragm pump. Thus, the discharge speed is effectively improved; the blocking phenomenon generated when thicker pulp is discharged is avoided; and cyclic grinding and discharging processes of the slurry are achieved in a circulating loop, and the production efficiency is also improved.
Description
Technical field
The utility model relates to the grinding technique field, relates in particular to a kind of ball mill discharging system.
Background technology
Existing ball mill has disposed the circulation that a membrane pump is used for slurry.The ringing of membrane pump makes in the slurry after the grinding solid particle size more even, and has improved grinding efficiency.See also shown in Figure 1ly, it is the discharge system of ball mill in the prior art.As shown in Figure 1, described ball mill discharging system comprises grinding chamber 120, is positioned at charging aperture 110, the membrane pump 150 on grinding chamber 120 tops, described membrane pump 150 is tightly connected with top and the bottom pipe of described grinding chamber 120, described grinding chamber 120, membrane pump 150 consist of the closed-loop path with pipeline, be provided with grinding chamber valve 130 on the pipeline between wherein said grinding chamber 120 bottoms and the membrane pump 150, the bottom of described grinding chamber valve 130 is provided with discharging opening 140.Slurry enters grinding in the grinding chamber 120 by the charging aperture 110 on grinding chamber 120 tops, this moment, discharging opening 140 was closed, slurry in the grinding chamber 120 is transported in the grinding chamber 120 through the closed-loop path by the pressure-acting of membrane pump 150 again, so just consisted of circular grinding, after grinding end, close membrane pump 150, open discharging opening 140, the slurry in the grinding chamber 120 relies on the weight of self to flow out from discharging opening 140.
In the prior art, the slurry of grinding is thicker, only relies on the weight of self to be difficult to slurry in the grinding chamber is discharged fully, causes easily the discharge blockage problem, and production efficiency is reduced.
Therefore, be necessary further improvement is done by the ball mill discharging system of prior art.
The utility model content
The purpose of this utility model is to provide a kind of high efficiency, discharging to be easy to the ball mill discharging system.
For reaching aforementioned purpose, a kind of ball mill discharging of the utility model system, it comprises grinding chamber, be positioned at the charging aperture on grinding chamber top, membrane pump, top and the bottom pipe of described membrane pump and described grinding chamber are tightly connected, described grinding chamber, membrane pump and pipeline consist of the closed-loop path, be provided with the grinding chamber valve on the pipeline between described grinding chamber bottom and the membrane pump, on the pipeline between wherein said grinding chamber top and the membrane pump circulation valve is set, described circulation valve bottom is provided with drawing mechanism, and described drawing mechanism is discharged slurry by described membrane pump.
According to an embodiment of the present utility model, described ball mill discharging system, it further comprises agitator, described agitator bottom is provided with the agitator charging aperture, described agitator is used for holding the slurry of discharging from described outlet device, and described agitator charging aperture is connected with described membrane pump seal for pipe joints.
According to an embodiment of the present utility model, described drawing mechanism comprises discharging opening and discharging opening valve, and described discharging opening valve is used for the switching of control discharging opening, described discharging opening valve open, described circulation valve is closed, and by described membrane pump slurry is transported in the described agitator.
The beneficial effects of the utility model: compared with prior art, the pipeline of the utility model between grinding chamber top and membrane pump arranges circulation valve and drawing mechanism, utilize the pressure-acting of membrane pump with the slurry output of grinding, Effective Raise discharging speed, and produce clogging when having avoided thicker slurry discharging; In a closed circuit, realize circular grinding and the discharging process of slurry, improved production efficiency.
Description of drawings
Fig. 1 is the structural representation of ball mill discharging system in the prior art;
Fig. 2 is the utility model ball mill discharging system structural representation in one embodiment;
Fig. 3 is the feed state schematic diagram of the utility model ball mill discharging system.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described in further detail.
See also shown in Figure 2ly, it is the utility model ball mill discharging system structural representation in one embodiment.As shown in Figure 2, described ball mill discharging system, it comprises grinding chamber 220, be positioned at the charging aperture 210 on grinding chamber 220 tops, membrane pump 240, described membrane pump 240 is tightly connected with top and the bottom pipe of described grinding chamber 220, described grinding chamber 220, membrane pump 240 consists of the closed-loop path with pipeline, be provided with grinding chamber valve 230 on the pipeline between described grinding chamber 220 bottoms and the membrane pump 240, on the pipeline between wherein said grinding chamber 220 tops and the membrane pump 240 circulation valve 250 is set, described circulation valve 250 bottoms are provided with drawing mechanism 260, drawing mechanism 260 is communicated with the top entrance of agitator 270, and ground slurry directly is transported in the agitator 270 by membrane pump 240.
Wherein, drawing mechanism 260 comprises discharging opening and discharging opening valve, and the discharging opening valve is used for the switching of control discharging opening, when the output slurry, the discharging opening valve open of drawing mechanism 260, circulation valve 250 is closed, and by membrane pump 240 slurry is transported in the agitator 270.Wherein, described agitator 270 bottoms are provided with agitator valve openings 280, be used for the discharge of control agitator 270 slurries, described agitator valve openings 280 can be connected with membrane pump 240, by membrane pump 240 slurry in the agitator 270 is transported to again and carries out circular grinding in the grinding chamber 220.
See also shown in Figure 3ly, it is the discharging view of the utility model feeding of ball mill system, and arrow points is the throughput direction of slurry among the figure.As shown in Figure 3, the discharging opening of drawing mechanism 260 is connected the entrance of agitator 270, open grinding chamber valve 230, close simultaneously circulation valve 250, open the gas source switch of membrane pump 240, the pressure-acting by membrane pump 240 is input to slurry in the agitator 270 from grinding chamber 220.
The pipeline of the utility model between grinding chamber top and membrane pump arranges circulation valve and drawing mechanism, and the pressure-acting that utilizes membrane pump is the slurry output of grinding, Effective Raise discharging speed, and produce clogging when having avoided thicker slurry discharging; In a closed circuit, realize circular grinding and the discharging process of slurry, improved production efficiency.
Above-mentioned explanation has fully disclosed the specific embodiment of the present utility model.It is pointed out that and be familiar with the scope that any change that the person skilled in art does the specific embodiment of the present utility model does not all break away from claims of the present utility model.Correspondingly, the scope of claim of the present utility model also is not limited only to previous embodiment.
Claims (3)
1. ball mill discharging system, it comprises grinding chamber, is positioned at the charging aperture on grinding chamber top, membrane pump, top and the bottom pipe of described membrane pump and described grinding chamber are tightly connected, described grinding chamber, membrane pump and pipeline consist of the closed-loop path, be provided with the grinding chamber valve on the pipeline between described grinding chamber bottom and the membrane pump, it is characterized in that: on the pipeline between described grinding chamber top and the membrane pump circulation valve is set, described circulation valve bottom is provided with drawing mechanism, and described drawing mechanism is discharged slurry by described membrane pump.
2. ball mill discharging according to claim 1 system, it is characterized in that: it further comprises agitator, described agitator bottom is provided with the agitator charging aperture, described agitator is used for holding the slurry of discharging from described outlet device, and described agitator charging aperture is connected with described membrane pump seal for pipe joints.
3. ball mill discharging according to claim 1 system, it is characterized in that: described drawing mechanism comprises discharging opening and discharging opening valve, described discharging opening valve is used for the switching of control discharging opening, described discharging opening valve open, described circulation valve is closed, and by described membrane pump slurry is transported in the described agitator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220548841 CN202893440U (en) | 2012-10-24 | 2012-10-24 | Discharge system of ball grinder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220548841 CN202893440U (en) | 2012-10-24 | 2012-10-24 | Discharge system of ball grinder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202893440U true CN202893440U (en) | 2013-04-24 |
Family
ID=48114162
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220548841 Expired - Fee Related CN202893440U (en) | 2012-10-24 | 2012-10-24 | Discharge system of ball grinder |
Country Status (1)
| Country | Link |
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| CN (1) | CN202893440U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105417170A (en) * | 2015-11-20 | 2016-03-23 | 上海凯伟电气设备有限公司 | Quantitative and cyclic feeding device |
| CN106179057A (en) * | 2016-08-31 | 2016-12-07 | 无锡东恒新能源科技有限公司 | A kind of high viscosity carbon nano tube paste stirred tank |
| CN106179093A (en) * | 2016-08-31 | 2016-12-07 | 无锡东恒新能源科技有限公司 | High viscosity carbon nano tube paste preparation system based on hot type premix stirring device |
| CN106237907A (en) * | 2016-08-31 | 2016-12-21 | 无锡东恒新能源科技有限公司 | A kind of hot type high viscosity carbon nano tube paste premix stirring device |
| CN106390817A (en) * | 2016-08-31 | 2017-02-15 | 无锡东恒新能源科技有限公司 | Stirring kettle-based high-viscosity carbon nanotube slurry preparation system |
| CN106621946A (en) * | 2016-08-31 | 2017-05-10 | 无锡东恒新能源科技有限公司 | High-viscosity carbon nanotube slurry premixing device |
| CN112759956A (en) * | 2021-01-05 | 2021-05-07 | 深圳市领英新材料科技有限公司 | Diatom mud coating and processing system |
-
2012
- 2012-10-24 CN CN 201220548841 patent/CN202893440U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105417170A (en) * | 2015-11-20 | 2016-03-23 | 上海凯伟电气设备有限公司 | Quantitative and cyclic feeding device |
| CN106179057A (en) * | 2016-08-31 | 2016-12-07 | 无锡东恒新能源科技有限公司 | A kind of high viscosity carbon nano tube paste stirred tank |
| CN106179093A (en) * | 2016-08-31 | 2016-12-07 | 无锡东恒新能源科技有限公司 | High viscosity carbon nano tube paste preparation system based on hot type premix stirring device |
| CN106237907A (en) * | 2016-08-31 | 2016-12-21 | 无锡东恒新能源科技有限公司 | A kind of hot type high viscosity carbon nano tube paste premix stirring device |
| CN106390817A (en) * | 2016-08-31 | 2017-02-15 | 无锡东恒新能源科技有限公司 | Stirring kettle-based high-viscosity carbon nanotube slurry preparation system |
| CN106621946A (en) * | 2016-08-31 | 2017-05-10 | 无锡东恒新能源科技有限公司 | High-viscosity carbon nanotube slurry premixing device |
| CN112759956A (en) * | 2021-01-05 | 2021-05-07 | 深圳市领英新材料科技有限公司 | Diatom mud coating and processing system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: WUXI DONGHENG NEW ENERGY TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: WUXI DONGHENG NEW ENERGY MATERIAL CO., LTD. Effective date: 20150116 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150116 Address after: 214000, 29-30, Jinshan Science Park, Jianghai West Road, Wuxi, Jiangsu Patentee after: Wuxi Dongheng New Energy Technology Co., Ltd. Address before: 214000 No. 29-30 Industrial Park, Jinshan north science and technology, Jianghai West Road, Jiangsu, Wuxi Patentee before: Wuxi Dongheng New Energy Materials Co.,Ltd. |
|
| 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: 20130424 Termination date: 20181024 |