CN205253338U - Magnetic force track grading plant - Google Patents
Magnetic force track grading plant Download PDFInfo
- Publication number
- CN205253338U CN205253338U CN201521122211.9U CN201521122211U CN205253338U CN 205253338 U CN205253338 U CN 205253338U CN 201521122211 U CN201521122211 U CN 201521122211U CN 205253338 U CN205253338 U CN 205253338U
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- China
- Prior art keywords
- magnetic force
- slurry
- fine powder
- container
- mixed slurry
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- 239000002002 slurry Substances 0.000 claims abstract description 61
- 239000011268 mixed slurry Substances 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 239000000843 powder Substances 0.000 claims description 60
- 235000012054 meals Nutrition 0.000 claims description 16
- 239000000463 material Substances 0.000 claims description 14
- 239000000696 magnetic material Substances 0.000 claims description 4
- 239000000615 nonconductor Substances 0.000 claims description 4
- 230000035699 permeability Effects 0.000 claims description 4
- 230000005484 gravity Effects 0.000 abstract description 8
- 239000006247 magnetic powder Substances 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 4
- 239000000203 mixture Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 239000007791 liquid phase Substances 0.000 description 5
- 238000007599 discharging Methods 0.000 description 2
- 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
- 239000006185 dispersion Substances 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
- 238000001179 sorption measurement Methods 0.000 description 1
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The utility model provides a magnetic force track grading plant, including the mixed slurry container, the container is collected to the farine thick liquids, the water conservancy diversion passageway, the magnetic force track, magnetic force crawler track device, magnetic force track parallel arrangement is in water conservancy diversion passageway below, the mixed slurry container includes the mixed slurry vessel, mix slurry feed port, middlings thick liquids liquid outlet, the farine thick liquids are collected the container and are included farine thick liquids collection vessel, farine slurry feed port, farine thick liquids liquid outlet, the mixed slurry container is collected the container with the farine thick liquids and is linked together through the water conservancy diversion passageway. The utility model discloses can be simple and convenient will have good dispersibility and have grading of magnetic powder thick liquids, 30 -90 degree angle is personally submitted to water conservancy diversion passageway and level for gravity and magnetic force that the middlings received are greater than the thick liquids resistance that receives, and the gravity that the farine received is less than the thick liquids resistance that receives with magnetic force, thereby realize the separation of middlings and farine, 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 magnetic force crawler belt 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 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 research and design a kind of magnetic force crawler belt grading plant, its object is: provide one effectively and simply to carry out classification to magnetic powder, make powder can reach the grading plant of the product that uses required each specification.
Technical solution of the present utility model:
A kind of magnetic force crawler belt grading plant, comprise mixed slurry container, fine powder slurry collection container, it is characterized in that: also comprise flow-guiding channel, magnetic force crawler belt, magnetic force caterpillar driving device, described flow-guiding channel and horizontal plane angle are 30-90 ° of angle, magnetic force crawler belt is set in parallel in flow-guiding channel below, described mixed slurry container comprises mixed slurry vessel, be arranged on the mixed slurry charging aperture of mixed slurry container top, be arranged on the meal slurry liquid outlet of mixed slurry container bottom, described fine powder slurry collection container comprises fine powder slurry collection container body, be arranged on the fine powder slurry feed mouth of fine powder slurry collection container bodies top, be arranged on the fine powder slurry liquid outlet of fine powder slurry collection container body bottom, mixed slurry container is connected by flow-guiding channel with fine powder slurry collection container.
Described mixed slurry container be shaped as taper.
Described fine powder slurry collection container be shaped as taper.
Described flow-guiding channel material is the permeability magnetic material that itself does not have or retain magnetic.
The material of described meal slurry liquid outlet and fine powder slurry collection container is the non-conductor material of magnetic.
In described mixed slurry container, the liquid level of mixed slurry is higher than the liquid level of fine powder slurry in fine powder slurry collector.
The beneficial effects of the utility model: the utility model is simple in structure, novel in design, can the classification of good dispersion and magnetic powdery pulp will be had simply and easily, flow-guiding channel is arranged to horizontal by 30-90 degree angle, guarantee that gravity and magnetic 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, there is very high use value.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Wherein: 1, mixed slurry vessel, 1-1, mixed slurry charging aperture, 1-2, meal slurry liquid outlet, 2, fine powder slurry collection container body, 2-1, fine powder slurry feed mouth, 2-2, fine powder slurry liquid outlet, 3, flow-guiding channel, 4, magnetic force crawler belt, magnetic force caterpillar driving device 5.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described further.
As shown in Figure 1, a kind of magnetic force crawler belt grading plant, comprise mixed slurry container, fine powder slurry collection container, also comprise flow-guiding channel 3, magnetic force crawler belt 4, magnetic force caterpillar driving device 5, flow-guiding channel 3 is 30-90 ° of angle with horizontal plane angle, magnetic force crawler belt 4 is set in parallel in flow-guiding channel 3 belows, mixed slurry container comprises mixed slurry vessel 1, be arranged on the mixed slurry charging aperture 1-1 of mixed slurry container top, be arranged on the meal slurry liquid outlet 1-2 of mixed slurry container bottom, fine powder slurry collection container comprises fine powder slurry collection container body 2, be arranged on the fine powder slurry feed mouth 2-1 of fine powder slurry collection container bodies top, be arranged on the fine powder slurry liquid outlet 2-2 of fine powder slurry collection container body bottom, mixed slurry container is connected by flow-guiding channel 3 with fine powder slurry collection container, mixed slurry container be shaped as taper, fine powder slurry collection container be shaped as taper, flow-guiding channel 3 materials are the permeability magnetic material that itself does not have or retain magnetic, the material of meal slurry liquid outlet and fine powder slurry collection container is the non-conductor material of magnetic, in mixed slurry container, the liquid level of mixed slurry is higher than the liquid level of fine powder slurry in fine powder slurry collector.
Concrete use procedure:
The mixed slurry of the magnetic powder that contains thickness inequality, add in mixed slurry container from the mixed slurry charging aperture 1-1 of mixed slurry container top, the mixed slurry of high liquid level, by there being the flow-guiding channel 3 of constant slope, flows in the fine powder slurry collector of low liquid level, there iing magnetic force crawler belt below the flow-guiding channel 3 of constant slope under the driving of magnetic force caterpillar driving device, from up to down move near flow-guiding channel one side, along with the magnetic-adsorption of magnetic force crawler belt operation the magnetic powder in mobile mixed slurry in flow-guiding channel, the magneticaction being subject to because of meal is stronger, and it is larger to be subject to Action of Gravity Field, can be along with the downward landing of direction of magnetic force crawler belt operation, constantly, to the bottom enrichment of mixed slurry container, the slurry of enrichment meal can be taken out by the meal slurry liquid outlet of container below, gravity and magneticaction that fine powder in flow-guiding channel in mixed slurry 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 collection container along flow-guiding channel, take out from the fine powder slurry discharging opening of fine powder slurry collection container bottom, flow-guiding channel and horizontal plane angle are 30-90 degree, guarantee that gravity and magnetic 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 is not had by itself or the permeability magnetic material that retains magnetic is made, to ensure that the magnetic force on magnetic force crawler belt better acts on the mobile magnetic powder in flow-guiding channel, flow-guiding channel inwall should keep good smoothness, to ensure meal landing and do not stop up flow-guiding channel smoothly, mixed slurry collector and fine powder collector are that the non-conductor of magnetic is made, in order to avoid be subject to the magneticaction of magnetic force crawler belt, affect the feeding of liquid outlet.
To sum up, the utility model produces a desired effect.
Claims (7)
1. a magnetic force crawler belt grading plant, comprise mixed slurry container, fine powder slurry collection container, it is characterized in that: also comprise flow-guiding channel, magnetic force crawler belt, magnetic force caterpillar driving device, described magnetic force crawler belt is set in parallel in flow-guiding channel below, described mixed slurry container comprises mixed slurry vessel, be arranged on the mixed slurry charging aperture of mixed slurry container top, be arranged on the meal slurry liquid outlet of mixed slurry container bottom, described fine powder slurry collection container comprises fine powder slurry collection container body, be arranged on the fine powder slurry feed mouth of fine powder slurry collection container bodies top, be arranged on the fine powder slurry liquid outlet of fine powder slurry collection container body bottom, mixed slurry container is connected by flow-guiding channel with fine powder slurry collection container.
2. a kind of magnetic force crawler belt grading plant as claimed in claim 1, is characterized in that: described flow-guiding channel and horizontal plane angle are 30-90 ° of angle.
3. a kind of magnetic force crawler belt grading plant as claimed in claim 1, is characterized in that: described mixed slurry container be shaped as taper.
4. a kind of magnetic force crawler belt grading plant as claimed in claim 1, is characterized in that: described fine powder slurry collection container be shaped as taper.
5. a kind of magnetic force crawler belt grading plant as claimed in claim 1, is characterized in that: described flow-guiding channel material is the permeability magnetic material that itself does not have or retain magnetic.
6. a kind of magnetic force crawler belt grading plant as claimed in claim 1, is characterized in that: the material of described meal slurry liquid outlet and fine powder slurry collection container is the non-conductor material of magnetic.
7. a kind of magnetic force crawler belt grading plant as claimed in claim 1, is characterized in that: in described mixed slurry container, the liquid level of mixed slurry is higher than the liquid level of fine powder slurry in fine powder slurry collector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521122211.9U CN205253338U (en) | 2015-12-31 | 2015-12-31 | Magnetic force track grading plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521122211.9U CN205253338U (en) | 2015-12-31 | 2015-12-31 | Magnetic force track grading plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205253338U true CN205253338U (en) | 2016-05-25 |
Family
ID=55994890
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521122211.9U Active CN205253338U (en) | 2015-12-31 | 2015-12-31 | Magnetic force track grading plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205253338U (en) |
-
2015
- 2015-12-31 CN CN201521122211.9U patent/CN205253338U/en active Active
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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. |