CN202893471U - Slurry ball-milling and sand-milling production system - Google Patents
Slurry ball-milling and sand-milling production system Download PDFInfo
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- CN202893471U CN202893471U CN 201220549801 CN201220549801U CN202893471U CN 202893471 U CN202893471 U CN 202893471U CN 201220549801 CN201220549801 CN 201220549801 CN 201220549801 U CN201220549801 U CN 201220549801U CN 202893471 U CN202893471 U CN 202893471U
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Abstract
The utility model provides a slurry ball-milling and sand-milling production system. The slurry ball-milling and sand-milling production system comprises a ball mill, a buffering barrel, a circulating tank, a sand mill and a first diaphragm pump connected with the sand mill, wherein the ball mill is in pipe connection with the buffering barrel, the circulating tank is in pipe connection with the sand mill, a second diaphragm pump is connected between the buffering barrel and the circulating tank, and the second diaphragm pump can convey the slurry in the buffering barrel to the circulating tank. In comparison with the prior art, according to the slurry ball-milling and sand-milling production system, one diaphragm pump is arranged between the buffering barrel and the circulating tank, and the diaphragm pump can directly convey the slurry in the buffering barrel to the circulating tank, so that the production continuity of ball milling and sand milling is guaranteed, since the whole production line is totally operated by equipment, manual transport is not needed, the production efficiency is improved.
Description
Technical field
The utility model relates to the grinding technique field, relates in particular to a kind of slurry ball milling sand milling production system.
Background technology
Conductive agent affects the performance of lithium ion battery largely as the important component part of lithium ion battery, Mn oxide, the materials such as phosphate.The electrical conductivity of these materials is all very low, but the service life that also will keep good high rate charge-discharge characteristic, grow.CNT is as a kind of novel fibrous conductive agent, can form complete three-dimensional conductive network structure, compare with conventional conductive agent such as conductive carbon black etc., CNT has higher electronic conductivity, institute's expense is also relatively low, is conducive to promote battery capacity, improves battery cycle life, is particularly advantageous in the high rate charge-discharge performance that improves battery.Make the carbon nanotube conducting agent and need to use first the ball mill ball milling to carry out sand milling again, at present in process of production, slurry needs manually to pour into circulating tank and carries out sand milling after ball milling is complete, and production efficiency is low, and waste of manpower.
Therefore, be necessary ball milling sand milling production system is done further improvement.
The utility model content
The purpose of this utility model is to provide the slurry ball milling sand milling continuous process system that a kind of production efficiency is high, save human resources.
For reaching aforementioned purpose, a kind of slurry ball milling of the utility model sand milling continuous process system, it comprises ball mill, buffer memory bucket, circulating tank, sand mill and the first membrane pump that is connected with sand mill, described ball mill is connected with described buffer memory bucket pipeline, described circulating tank is connected with described sand mill pipeline, wherein is provided with the second membrane pump between described buffer memory bucket and described circulating tank, and described the second membrane pump can be transported to the slurry in the described buffer memory bucket in the described circulating tank.
According to an embodiment of the present utility model, described buffer memory bucket is provided with upper port and lower port, and described upper port is connected with the discharging opening of described ball mill, and described lower port is connected with the import of the second membrane pump.
According to an embodiment of the present utility model, the upper shed one of described circulating tank is connected with described the second membrane pump, and the upper shed two of described circulating tank is connected with described sand mill, and the under shed of described circulating tank is connected with described the first membrane pump.
The beneficial effects of the utility model: compared with prior art, the utility model is by arranging a membrane pump between buffer memory bucket and circulating tank, this membrane pump can be delivered directly to the slurry in the buffer memory bucket in the circulating tank, that whole production line all operates by equipment, and do not need a dead lift, improved production efficiency.
Description of drawings
Fig. 1 is the utility model slurry ball milling sand milling operation system structure schematic diagram.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described in further detail.
See also shown in Figure 1ly, it is the utility model slurry ball milling sand milling operation system structure schematic diagram.As shown in Figure 1, the sand milling of ball milling described in figure production system comprises ball mill 1, buffer memory bucket 2, circulating tank 4, sand mill 5 and the first membrane pump 6 that is connected with sand mill 5 pipelines.The lower end of ball mill 1 is provided with discharging opening, and buffer memory bucket 2 is provided with upper port and lower port, and the discharging opening of described ball mill 1 lower end is connected by pipeline with the upper port of described buffer memory bucket 2.In order to guarantee the continuity of production line, be provided with the second membrane pump 3 between buffer memory bucket 2 and the circulating tank 4, the import of described the second membrane pump 3 is connected by pipeline with the lower port of described buffer memory bucket 2.
Wherein, the top of described circulating tank 4 is provided with the first charging aperture and the second charging aperture, circulating tank 4 bottoms are provided with the 3rd discharging opening, described the first charging aperture is connected by the outlet of pipeline with described the second membrane pump 3, described the second charging aperture is connected with described sand mill 5 by pipeline, and described the 3rd discharging opening is connected by the import of pipeline with described the first membrane pump 6.
Please continue to consult shown in Figure 1, arrow points is the throughput direction of slurry among the figure.Slurry enters storage in the buffer memory bucket 2 by discharging opening after ball milling is finished in ball mill 1, then the slurry of the High Rotation Speed by the second membrane pump 3 after with ball milling in the buffer memory bucket 2 directly is transported in the circulating tank 4, slurry in the circulating tank 4 is transported to by the first membrane pump 6 and carries out sand milling in the sand mill 5, and then finishes the ball milling of slurry and the series-operation of sand milling.
The utility model leads to a membrane pump is set between buffer memory bucket and circulating tank, this membrane pump can be delivered directly to the slurry in the buffer memory bucket in the circulating tank, guaranteed the continuity that ball milling and sand milling operation are produced, whole production line is moved by computation equipment, and do not need a dead lift, 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. slurry ball milling sand milling production system, it comprises ball mill, buffer memory bucket, circulating tank, sand mill and the first membrane pump that is connected with sand mill, described ball mill is connected with described buffer memory bucket pipeline, described circulating tank is connected with described sand mill pipeline, it is characterized in that: be provided with the second membrane pump between described buffer memory bucket and described circulating tank, described the second membrane pump can be transported to the slurry in the described buffer memory bucket in the described circulating tank.
2. slurry ball milling sand milling production system according to claim 1, it is characterized in that: described buffer memory bucket is provided with upper port and lower port, and described upper port is connected with the discharging opening of described ball mill, and described lower port is connected with the import of the second membrane pump.
3. slurry ball milling sand milling production system according to claim 1, it is characterized in that: the upper shed one of described circulating tank is connected with described the second membrane pump, the upper shed two of described circulating tank is connected with described sand mill, and the under shed of described circulating tank is connected with described the first membrane pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220549801 CN202893471U (en) | 2012-10-24 | 2012-10-24 | Slurry ball-milling and sand-milling production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220549801 CN202893471U (en) | 2012-10-24 | 2012-10-24 | Slurry ball-milling and sand-milling production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202893471U true CN202893471U (en) | 2013-04-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220549801 Expired - Fee Related CN202893471U (en) | 2012-10-24 | 2012-10-24 | Slurry ball-milling and sand-milling production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202893471U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032580A (en) * | 2015-06-03 | 2015-11-11 | 安徽省铜陵县牛山矿业有限责任公司 | Continuous grinding device for mineral extender |
| 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 |
| CN106179688A (en) * | 2016-08-31 | 2016-12-07 | 无锡东恒新能源科技有限公司 | A kind of slurry production line with real-time traffic control function |
| 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 |
| CN106215785A (en) * | 2016-08-31 | 2016-12-14 | 无锡东恒新能源科技有限公司 | A kind of carbon nano tube paste preparation system based on stirred tank |
| 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 |
| CN106345353A (en) * | 2016-08-31 | 2017-01-25 | 无锡东恒新能源科技有限公司 | Carbon nanotube paste stirring reactor |
| 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 |
| CN108339649A (en) * | 2017-01-23 | 2018-07-31 | 临沂春光磁业有限公司 | A kind of novel nano sand mill circulatory system of high uniformity |
-
2012
- 2012-10-24 CN CN 201220549801 patent/CN202893471U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032580A (en) * | 2015-06-03 | 2015-11-11 | 安徽省铜陵县牛山矿业有限责任公司 | Continuous grinding device for mineral extender |
| 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 |
| CN106179688A (en) * | 2016-08-31 | 2016-12-07 | 无锡东恒新能源科技有限公司 | A kind of slurry production line with real-time traffic control function |
| 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 |
| CN106215785A (en) * | 2016-08-31 | 2016-12-14 | 无锡东恒新能源科技有限公司 | A kind of carbon nano tube paste preparation system based on stirred tank |
| 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 |
| CN106345353A (en) * | 2016-08-31 | 2017-01-25 | 无锡东恒新能源科技有限公司 | Carbon nanotube paste stirring reactor |
| 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 |
| CN108339649A (en) * | 2017-01-23 | 2018-07-31 | 临沂春光磁业有限公司 | A kind of novel nano sand mill circulatory system of high uniformity |
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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: 20150119 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150119 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 |
Granted publication date: 20130424 Termination date: 20181024 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |