CN201676740U - Synthetic mica step-by-step separation device - Google Patents
Synthetic mica step-by-step separation device Download PDFInfo
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- CN201676740U CN201676740U CN2010201663150U CN201020166315U CN201676740U CN 201676740 U CN201676740 U CN 201676740U CN 2010201663150 U CN2010201663150 U CN 2010201663150U CN 201020166315 U CN201020166315 U CN 201020166315U CN 201676740 U CN201676740 U CN 201676740U
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- sedimentation basin
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Abstract
A synthetic mica step-by-step separation device adopts the structure that a gate or a water pump is mounted between a mixed solution inlet and a mixed solution outlet, the gate is connected with a driving mechanism used for controlling the on-off of the gate, and the driving mechanism or the water pump is connected with a control circuit used for controlling the on-off time of the driving mechanism or the water pump. The synthetic mica step-by-step separation device utilizes the different required settling periods of mica with different thicknesses and granularities in water to conduct several times of settlement in sequence for further subdividing the grades of mica, consumes less raw material and energy because the waste water can be recycled, and has the advantages of simple structure, convenient operation, low cost and favorable economic benefit and social benefit.
Description
Technical field
The utility model relates to a kind of mica production equipment, is specifically related to a kind of artificial synthetic mica separator step by step.
Background technology
Artificial synthetic mica is with industrial chemicals such as potassium fluosilicate, silica flour, fused magnesite, aluminium oxide and potash, the high-temperature insulation material of making through the high-temperature fusion calcining.Mica after the calcining need be pulverized, and adopts wet method to the variable grain degree then, and the mica that different sheets are thick sieves.Be used to separate the variable grain degree in the prior art, the main method of different sheet degree micas is to adopt the different filter screen of various order numbers to sieve.Though this ten minutes method is fast, the grade that screening is come out is fewer, and is relatively more rough, and energy resource consumption is bigger, and the waste to material in the screening process is more serious.Therefore thinner for the rank of mica powder being got, energy consumes still less, and material is wasted still less, is necessary the screening mode of existing mica powder is improved.
The utility model content
The purpose of this utility model is to overcome defective of the prior art, has designed a kind of artificial synthetic mica separator step by step, and this device can get the ranking score of mica powder thinner, more, and its energy-output ratio is very little, makes the wastage of raw material also can be seldom.
For achieving the above object, the technical solution of the utility model is to adopt a kind of artificial synthetic mica separator step by step, it is characterized in that, described device comprises that several connect sedimentation basin successively, on described sedimentation basin, be respectively equipped with the mixed liquor import and the mixture export of mica and water, between described mixed liquor import and mixture export, gate or water pump are housed, described gate is connected with driving mechanism, described driving mechanism is used to control the keying of described gate, described driving mechanism or water pump are connected with control circuit again, and described control circuit is used to control the time of the closure or openness of described driving mechanism or water pump.
Wherein, the stepped arrangement of the described sedimentation basin that several connect successively, and described gate is arranged between the mixed liquor import of the mixture export of upper level sedimentation basin and next stage sedimentation basin, and the sedimentation basin that is positioned at stepped the top is first sedimentation basin.
Wherein, on described first sedimentation basin, only be provided with mixture export and water inlet, and in described first sedimentation basin, be provided with agitator.
Wherein, the described sedimentation basin that several connect is successively arranged at grade, and the sedimentation basin that is positioned at several sedimentation basin one ends is first sedimentation basin.
Wherein, on described first sedimentation basin, only be provided with mixture export and water inlet, in described first sedimentation basin, be provided with agitator.
Wherein, between the mixed liquor import of the mixture export of described sedimentation basins at different levels and next stage sedimentation basin, be connected with water pump by pipeline.
Advantage of the present utility model and beneficial effect are: this device utilizes the variable grain degree, the thick mica of different sheets precipitates the difference of needed sedimentation time in water, after mica powder can being precipitated a period of time in first sedimentation basin, again unprecipitated mixed liquor is discharged into second sedimentation basin, and then second after sedimentation basin precipitates a period of time again, again unprecipitated mixed liquor is discharged into the 3rd sedimentation basin, carrying out the several times post precipitation successively just can get the ranking score of mica thinner, more, and its energy-output ratio is very little, can also be recycled with the water of crossing, the consumption that can make the raw material and the energy seldom.This apparatus structure is simple, and is easy to operate, and with low cost have good economic benefit and a social benefit.
Description of drawings
Fig. 1 is the utility model mica structural representation of separator embodiment 2 step by step;
Fig. 2 is the utility model mica structural representation of separator embodiment 3 step by step.
Among the figure: 1, sedimentation basin; 1-1, first sedimentation basin; 2, mixed liquor import; 3, mixed liquor import; 4, gate; 5, water pump; 6, driving mechanism; 7, water inlet; 8, agitator.
The specific embodiment
Below in conjunction with drawings and Examples, the specific embodiment of the present utility model is further described.Following examples only are used for the technical solution of the utility model more clearly is described, and can not limit protection domain of the present utility model with this.
As accompanying drawing 1, shown in Figure 2, the concrete technical scheme of implementing of the utility model is:
A kind of artificial synthetic mica is separator step by step, this device comprises that several connect sedimentation basin 1 successively, on described sedimentation basin, be respectively equipped with the mixed liquor import 2 and mixture export 3 of mica and water, gate 4 or water pump 5 are housed between described mixed liquor import and mixture export, described gate is connected with driving mechanism 6, described driving mechanism 6 is used to control the keying of described gate 4, described driving mechanism 6 or water pump 5 are connected with control circuit again, and described control circuit is used to control the time of the closure or openness of described driving mechanism 6 or water pump 5.
On the basis of embodiment 1, the embodiment of the utility model the best is, with 4 sedimentation basin 1 stepped arrangements that connect successively, and gate 4 is installed between the mixed liquor import 2 of the mixture export 3 of upper level sedimentation basin 1 and next stage sedimentation basin 1, the sedimentation basin 1 that wherein is positioned at stepped the top is the first sedimentation basin 1-1.On the first sedimentation basin 1-1, only be provided with mixture export 3 and water inlet 7, and in the first sedimentation basin 1-1, agitator 8 be housed.
On the basis of embodiment 1, the utility model has also designed preferable embodiment, and 4 sedimentation basins that connect successively 1 are arranged at grade, and the sedimentation basin that wherein is positioned at 4 sedimentation basin 1 one ends is the first sedimentation basin 1-1.On the first sedimentation basin 1-1, only be provided with mixture export 3 and water inlet 7, agitator 8 is housed in first sedimentation basin.Between the mixed liquor import 2 of the mixture export 3 of sedimentation basins 1 at different levels and next stage sedimentation basin 1, be connected with water pump 5 by pipeline.
When practical operation by control circuit or Artificial Control is arranged, at first mica powder is added in the first sedimentation basin 1-1, in the first sedimentation basin 1-1, add water by water inlet 7 then, when water add to be set at after, start agitator 8 mica powder and water are stirred into uniform mixed liquor, close agitator 8 then.Open gate 4 or water pump 5 between the first precipitation 1-1 pond and second sedimentation basin after 20 minutes, gate 4 after 2 hours between unlatching second sedimentation basin and the 3rd sedimentation basin or water pump are opened gate 4 or the water pump 5 between the 3rd sedimentation basin and the 4th sedimentation basin after 5,6 hours.After the mixed liquor in first sedimentation basin is put only, the mica of precipitation can be cleared and add mica powder and water wait stirring next time again.After the mixed liquor in second sedimentation basin is put only, the mica of precipitation can be cleared and wait for the adding of mixed liquor next time, after the mixed liquor in the 3rd sedimentation basin is put only, the mica of precipitation can be cleared and wait for the adding of mixed liquor next time, after the mixed liquor in the 4th sedimentation basin is put only, the mica of precipitation can be cleared and wait for the adding of mixed liquor next time.The aforesaid operations process can continuously be carried out, and the water of discharging in the 4th sedimentation basin can be added in first sedimentation basin again, and water can be recycled like this, and each moisture that only need additional lose on a small quantity is just passable.Said process can increase or reduce the quantity of sedimentation basin according to actual needs, and adjusts the needed time of precipitation.
The above only is a preferred implementation of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (6)
1. artificial synthetic mica separator step by step, it is characterized in that, described device comprises that several connect sedimentation basin successively, on described sedimentation basin, be respectively equipped with the mixed liquor import and the mixture export of mica and water, between described mixed liquor import and mixture export, gate or water pump are housed, described gate is connected with driving mechanism, described driving mechanism is used to control the keying of described gate, described driving mechanism or water pump are connected with control circuit again, and described control circuit is used to control the time of the closure or openness of described driving mechanism or water pump.
2. artificial synthetic mica according to claim 1 is separator step by step, it is characterized in that, the stepped arrangement of the described sedimentation basin that several connect successively, and described gate is arranged between the mixed liquor import of the mixture export of upper level sedimentation basin and next stage sedimentation basin, and the sedimentation basin that is positioned at stepped the top is first sedimentation basin.
3. artificial synthetic mica according to claim 2 is separator step by step, it is characterized in that, only is provided with mixture export and water inlet on described first sedimentation basin, and is provided with the agitator stirring in described first sedimentation basin.
4. artificial synthetic mica according to claim 1 is separator step by step, it is characterized in that, the described sedimentation basin that several connect is successively arranged at grade, and the sedimentation basin that is positioned at several sedimentation basin one ends is first sedimentation basin.
5. artificial synthetic mica according to claim 4 is separator step by step, it is characterized in that, only is provided with mixture export and water inlet on described first sedimentation basin, is provided with agitator in described first sedimentation basin.
6. artificial synthetic mica according to claim 5 is separator step by step, it is characterized in that, is connected with water pump by pipeline between the mixed liquor import of the mixture export of described sedimentation basins at different levels and next stage sedimentation basin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201663150U CN201676740U (en) | 2010-04-22 | 2010-04-22 | Synthetic mica step-by-step separation device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201663150U CN201676740U (en) | 2010-04-22 | 2010-04-22 | Synthetic mica step-by-step separation device |
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| CN201676740U true CN201676740U (en) | 2010-12-22 |
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| CN2010201663150U Expired - Fee Related CN201676740U (en) | 2010-04-22 | 2010-04-22 | Synthetic mica step-by-step separation device |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103069961A (en) * | 2013-01-21 | 2013-05-01 | 昆山益谊现代农业科技有限公司 | Three-level separating biogas slurry drip-irrigation fertilization system |
| CN103338867A (en) * | 2011-06-02 | 2013-10-02 | 新东工业株式会社 | Classification device, and classification method, blast machining device provided with this classification device, and blast machining method |
| CN103736580A (en) * | 2013-11-13 | 2014-04-23 | 江苏凯特汽车部件有限公司 | Washing device for residual aluminum recycle |
| CN104069668A (en) * | 2014-06-09 | 2014-10-01 | 陆辰钊 | Efficient sewage filtering control system |
| CN108165773A (en) * | 2018-01-24 | 2018-06-15 | 攀钢集团攀枝花钢钒有限公司 | Hot carbide slag granulation and grain slag separation method |
-
2010
- 2010-04-22 CN CN2010201663150U patent/CN201676740U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103338867A (en) * | 2011-06-02 | 2013-10-02 | 新东工业株式会社 | Classification device, and classification method, blast machining device provided with this classification device, and blast machining method |
| CN103338867B (en) * | 2011-06-02 | 2015-07-08 | 新东工业株式会社 | Classification device, and classification method, blast machining device provided with this classification device, and blast machining method |
| CN103069961A (en) * | 2013-01-21 | 2013-05-01 | 昆山益谊现代农业科技有限公司 | Three-level separating biogas slurry drip-irrigation fertilization system |
| CN103069961B (en) * | 2013-01-21 | 2015-11-25 | 昆山益谊现代农业科技有限公司 | A kind of three grades of separate type natural pond drip irrigation fertilization systems |
| CN103736580A (en) * | 2013-11-13 | 2014-04-23 | 江苏凯特汽车部件有限公司 | Washing device for residual aluminum recycle |
| CN103736580B (en) * | 2013-11-13 | 2016-03-02 | 江苏凯特汽车部件有限公司 | A kind of residual alum recovery water washing device |
| CN104069668A (en) * | 2014-06-09 | 2014-10-01 | 陆辰钊 | Efficient sewage filtering control system |
| CN108165773A (en) * | 2018-01-24 | 2018-06-15 | 攀钢集团攀枝花钢钒有限公司 | Hot carbide slag granulation and grain slag separation method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101222 Termination date: 20180422 |
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| CF01 | Termination of patent right due to non-payment of annual fee |