CN205253323U - Spiral carousel grading plant - Google Patents
Spiral carousel grading plant Download PDFInfo
- Publication number
- CN205253323U CN205253323U CN201521122212.3U CN201521122212U CN205253323U CN 205253323 U CN205253323 U CN 205253323U CN 201521122212 U CN201521122212 U CN 201521122212U CN 205253323 U CN205253323 U CN 205253323U
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- Prior art keywords
- flow
- guiding channel
- fine powder
- slurry collector
- collector
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- 239000002002 slurry Substances 0.000 claims abstract description 74
- 239000007788 liquid Substances 0.000 claims abstract description 29
- 230000005540 biological transmission Effects 0.000 claims abstract description 9
- 239000000843 powder Substances 0.000 claims description 48
- 235000012054 meals Nutrition 0.000 claims description 41
- 239000011268 mixed slurry Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 3
- 238000000926 separation method Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 239000007791 liquid phase Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000005484 gravity Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The utility model provides a spiral carousel grading plant, including middlings thick liquids collector, farine thick liquids collector, still include the spiral carousel, spiral carousel transmission, the spiral carousel is including " spiral " guiding gutter, the water conservancy diversion passageway, the setting of " spiral " guiding gutter is the bottom in the water conservancy diversion passageway, spiral carousel transmission is connected with middlings thick liquids collector, 30~90 jiaos are personally submitted with the level to the water conservancy diversion passageway, middlings thick liquids collector includes middlings thick liquids collector body, mix slurry feed port, middlings thick liquids liquid outlet, farine thick liquids collector includes farine thick liquids collector body, farine slurry feed port, farine thick liquids liquid outlet. The utility model has the advantages of simple structure and novel design, can be simply, convenient, effectively with middlings and farine separation, reduce the manufacturing cost of enterprise, have very high use value.
Description
Technical field
The utility model belongs to powder liquid phase classification technique field, is specifically related to a kind of helix swiveling plate grading plant.
Background technology
Powder body material is an important branch of Material Field, in order to improve the various performances of material, is the target that people pursue by the elementary cell granular of composition material always. Superfine powder and densified be one of the study hotspot of Material Field, compared with conventional material, superfine powder has physics, chemistry and the surface and interface character of a series of excellences. Undressed superfine powder is often in a larger particle size distribution, and in the use of each industrial circle of modern times, often requires superfine powder product in certain particle size distribution, needs superfine powder to carry out classification processing.
Existing classification technique is mainly divided into gas phase classification and liquid phase classification technique etc., and topmost method is liquid phase cyclone classification technology in liquid phase classification technique, because liquid phase eddy flow need to first be well dispersed in powder in solvent, re-use after high-pressure pump supercharging, from cyclone, enter and form high-speed rotary fluid, under centrifugal effect, meal is separated with fine powder, and discharge and collect from different discharging openings, the method is higher to equipment requirement, cyclone needs higher making precision and difficulty, booster pump is because carrying the slurry that also supercharging contains superfine powder very easily to damage.
Utility model content
The problem existing for above-mentioned prior art, the utility model provides a kind of helix swiveling plate grading plant of processing powdery pulp, can effectively and simply carry out classification to powder, makes powder can reach the product that uses required each specification.
Technical solution of the present utility model:
A kind of helix swiveling plate grading plant, comprise meal slurry collector, fine powder slurry collector, it is characterized in that: also comprise helix swiveling plate, helix swiveling plate transmission device, described helix swiveling plate comprises " spirality " guiding gutter, flow-guiding channel, " spirality " guiding gutter is arranged on flow-guiding channel inner bottom part, helix swiveling plate transmission device is connected with meal slurry collector, described flow-guiding channel is horizontal by 30～90 ° of angles, meal slurry collector comprises meal slurry collector body, be arranged on the mixed slurry charging aperture of meal slurry collector bodies top, be arranged on the meal slurry liquid outlet of meal slurry collector body bottom, fine powder slurry collector comprises fine powder slurry collector body, be arranged on the fine powder slurry feed mouth of fine powder slurry collector bodies top, be arranged on the fine powder slurry liquid outlet of fine powder slurry collector body bottom.
Described flow-guiding channel is two groups, comprises the first flow-guiding channel, the second flow-guiding channel, and the first flow-guiding channel, the second flow-guiding channel are symmetricly set on meal slurry collector both sides.
Described fine powder slurry collector is two groups, is connected respectively by the first flow-guiding channel, the second flow-guiding channel with meal slurry collector.
The groove depth of described " spirality " guiding gutter is not more than 1/2nd of flow-guiding channel gap thickness.
Liquid level line height in described meal slurry collector is higher than liquid level line height in fine powder slurry collector.
The beneficial effects of the utility model: the utility model is simple in structure, novel in design, can be simply, convenient, effectively meal is separated with fine powder, reduce enterprise's production cost, there is very high use value.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is " spirality " guiding gutter distributing line in the utility model.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described further.
As Fig. 1, shown in Fig. 2, a kind of helix swiveling plate grading plant, comprise meal slurry collector, fine powder slurry collector, also comprise helix swiveling plate, helix swiveling plate transmission device, helix swiveling plate comprises " spirality " guiding gutter, flow-guiding channel, " spirality " guiding gutter is arranged on flow-guiding channel inner bottom part, helix swiveling plate transmission device is connected with meal slurry collector, flow-guiding channel is horizontal by 30～90 ° of angles, meal slurry collector comprises meal slurry collector body, be arranged on the mixed slurry charging aperture of meal slurry collector bodies top, be arranged on the meal slurry liquid outlet of meal slurry collector body bottom, fine powder slurry collector comprises fine powder slurry collector body, be arranged on the fine powder slurry feed mouth of fine powder slurry collector bodies top, be arranged on the fine powder slurry liquid outlet of fine powder slurry collector body bottom, flow-guiding channel is two groups, comprise the first flow-guiding channel, the second flow-guiding channel, the first flow-guiding channel, the second flow-guiding channel is symmetricly set on meal slurry collector both sides, fine powder slurry collector is two groups, respectively by the first flow-guiding channel, the second flow-guiding channel is connected with meal slurry collector, the groove depth of " spirality " guiding gutter is not more than 1/2nd of flow-guiding channel gap thickness, liquid level line height in meal slurry collector is higher than liquid level line height in fine powder slurry collector.
Concrete use procedure: the mixed slurry that contains the uneven powder of thickness, enter meal slurry collector body from the mixed slurry charging aperture of meal slurry collector bodies top, the mixed slurry of high liquid level, by the flow-guiding channel horizontal by 30～90 ° of angles, flows in the fine powder slurry collector body of low liquid level; Horizontal by the flow-guiding channel at 30～90 ° of angles under the driving of helix swiveling plate transmission device, the equidirectional rotation of dispersing by helical form guiding gutter, along with the helical form guiding gutter of rotating disk operation, the turbid liquid that makes to be positioned at the meal slurry that flow-guiding channel bottom forms because of gravity and centrifugal force flows along the downward landing of direction of rotation, constantly, to being arranged on the bottom enrichment of meal slurry collector body, meal slurry is taken out by meal slurry liquid outlet; In flow-guiding channel, gravity and centrifugal action that in mixed slurry, fine powder is subject to are less, and the liquid resistance of the slurry inside being subject to is larger, along with mobile slurry upwards moves and enters in fine powder slurry collector body along flow-guiding channel, finally taken out by the fine powder slurry liquid outlet of fine powder slurry collector body bottom. The tapering of flow-guiding channel is 30-90 degree (the flow-guiding channel conical surface and horizontal sextant angle), guarantee that gravity and centrifugal force that in flow-guiding channel, mobile meal is subject to are greater than the slurry resistance being subject to, and the gravity that fine powder is subject to and magnetic force are less than the slurry resistance being subject to, thereby realize separating of meal and fine powder. Flow-guiding channel inwall and spiral stream guidance groove should keep good smoothness, to ensure meal landing and do not stop up flow-guiding channel smoothly.
To sum up, the utility model produces a desired effect.
Claims (5)
1. a helix swiveling plate grading plant, comprise meal slurry collector, fine powder slurry collector, it is characterized in that: also comprise helix swiveling plate, helix swiveling plate transmission device, described helix swiveling plate comprises " spirality " guiding gutter, flow-guiding channel, " spirality " guiding gutter is arranged on flow-guiding channel inner bottom part, helix swiveling plate transmission device is connected with meal slurry collector, described flow-guiding channel is horizontal by 30～90 ° of angles, meal slurry collector comprises meal slurry collector body, be arranged on the mixed slurry charging aperture of meal slurry collector bodies top, be arranged on the meal slurry liquid outlet of meal slurry collector body bottom, fine powder slurry collector comprises fine powder slurry collector body, be arranged on the fine powder slurry feed mouth of fine powder slurry collector bodies top, be arranged on the fine powder slurry liquid outlet of fine powder slurry collector body bottom.
2. a kind of helix swiveling plate grading plant as claimed in claim 1, is characterized in that: described flow-guiding channel is two groups, comprise the first flow-guiding channel, the second flow-guiding channel, the first flow-guiding channel, the second flow-guiding channel are symmetricly set on meal slurry collector both sides.
3. a kind of helix swiveling plate grading plant as claimed in claim 1, is characterized in that: described fine powder slurry collector is two groups, is connected respectively by the first flow-guiding channel, the second flow-guiding channel with meal slurry collector.
4. a kind of helix swiveling plate grading plant as claimed in claim 1, is characterized in that: the groove depth of described " spirality " guiding gutter is not more than 1/2nd of flow-guiding channel gap thickness.
5. a kind of helix swiveling plate grading plant as claimed in claim 1, is characterized in that: the liquid level line height in described meal slurry collector is higher than liquid level line height in fine powder slurry collector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521122212.3U CN205253323U (en) | 2015-12-31 | 2015-12-31 | Spiral carousel grading plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521122212.3U CN205253323U (en) | 2015-12-31 | 2015-12-31 | Spiral carousel grading plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205253323U true CN205253323U (en) | 2016-05-25 |
Family
ID=55994875
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521122212.3U Active CN205253323U (en) | 2015-12-31 | 2015-12-31 | Spiral carousel grading plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205253323U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106108660A (en) * | 2016-08-24 | 2016-11-16 | 北京婴萌科技有限公司 | There is the powder infusing device of guiding gutter |
| CN112452525A (en) * | 2020-11-05 | 2021-03-09 | 青海昆仑种业集团有限公司 | Device that numerous kind of rape was used |
-
2015
- 2015-12-31 CN CN201521122212.3U patent/CN205253323U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106108660A (en) * | 2016-08-24 | 2016-11-16 | 北京婴萌科技有限公司 | There is the powder infusing device of guiding gutter |
| CN112452525A (en) * | 2020-11-05 | 2021-03-09 | 青海昆仑种业集团有限公司 | Device that numerous kind of rape was used |
| CN112452525B (en) * | 2020-11-05 | 2022-06-21 | 青海昆仑种业集团有限公司 | Device that numerous kind of rape was used |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 223800 Suqian province high tech Development Zone, Jiangshan Road, No. 23, No. Patentee after: Jiangsu Bo move new materials Limited by Share Ltd Address before: 223800 Huashan Road, Suyu Economic Development Zone, Jiangsu, No. 109, No. Patentee before: Jiangsu Boqian New Materials Co., Ltd. |