CN203635340U - Super-micro-fine powder separator - Google Patents
Super-micro-fine powder separator Download PDFInfo
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- CN203635340U CN203635340U CN201320876955.4U CN201320876955U CN203635340U CN 203635340 U CN203635340 U CN 203635340U CN 201320876955 U CN201320876955 U CN 201320876955U CN 203635340 U CN203635340 U CN 203635340U
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- liquid
- seperator
- micropowders
- separator
- end cover
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Abstract
The utility model discloses a super-micro-fine powder separator. The super-micro-fine powder separator comprises a machine body, a control device, a driving device, a lower bearing device and a separating device. The control device is connected with the driving device. The driving device is connected with the separating device. The lower bearing device is located below the separating device. The separating device comprises a classifying device and an accumulated liquid collection device. The accumulated liquid collection device is used for collecting liquid mixtures and liquid separated out by the classifying device. The classifying device comprises a barrel body, a lower end cover and a particle size classifier. The barrel body is connected with the lower end cover. The particle size classifier is installed in the lower end cover. Solid particles separated by the super-micro-fine powder separator are superfine in particle size and uniform in distribution, and the super-micro-fine powder separator is reasonable in structure, free of grease pollution and convenient to maintain and dismantle.
Description
Technical field
The utility model relates to field of mechanical technique, relates in particular to a kind of micropowders seperator.
Background technology
Seperator is mainly used in the fields such as fine chemistry industry, new material, pottery, in the time that seperator is isolated the fine powder of micron grade or nano-scale from liquid mixture, the seperator of most does not reach the sizing specification of solid particle in fine powder, the main problem existing is, solid particle in fine powder is the phenomenon such as skewness in particle size range, does not reach desirable fine powder qualified products.
Utility model content
In view of current seperator above shortcomings, the utility model provides the micropowders seperator that a kind of particle diameter of solid particle is superfine, be evenly distributed.
For achieving the above object, embodiment of the present utility model adopts following technical scheme:
A kind of micropowders seperator, comprise control fuselage, device processed, drive unit, lower bearing equipment and separator, described control device is connected with drive unit, described drive unit is connected with separator, described lower bearing equipment is positioned at the below of separator, described separator comprises classifying equipoment and hydrops gathering-device, and described hydrops gathering-device is collected liquid mixture and the liquid that classifying equipoment is separated; Described classifying equipoment comprises cylindrical shell, bottom end cover and grain size grading device, and described cylindrical shell is connected with bottom end cover, and described grain size grading device is arranged in bottom end cover.
According to an aspect of the present utility model, the side of described bottom end cover is provided with particle outlet, and the side of described grain size grading device is provided with passage, and the position of described passage is corresponding with particle outlet; The side at described cylindrical shell top is provided with liquid outlet.
According to an aspect of the present utility model, described particle outlet comprises spray bar, spray sheet and locking nut, and described spray sheet is fixed on spray bar by locking nut, and the centre of described spray sheet is provided with spray film perforation.
According to an aspect of the present utility model, described classifying equipoment is isolated the solid particle of certain particle size range from liquid mixture, and described particle size range is micron grade or nano-scale; Described hydrops gathering-device comprises liquid collection part and liquid mixture collection part, described liquid collection part is positioned at the top of fuselage, fluid collection device is to collect water or the liquid that classifying equipoment is separated, within described liquid mixture is collected and is partly positioned at fuselage, it is to collect the liquid mixture that classifying equipoment is separated that liquid mixture is collected part.
According to an aspect of the present utility model, described particle size range is 1-10nm.
According to an aspect of the present utility model, described lower bearing equipment comprises liquid input device, step, bearing holder (housing, cover) and bearing, described step is fixed on the bottom of fuselage, described step is provided with liquid inlet, liquid outlet and passage correspondingly, described liquid inlet is connected with liquid input device by woven hose, and described liquid is water or free of contamination liquid.
According to an aspect of the present utility model, described woven hose is connected with the bottom of liquid input device, and described woven hose is or/and liquid outlet is provided with valve; The horizontal plane at the discharge outlet place of described liquid outlet is not less than the end face of bearing.
According to an aspect of the present utility model, described drive unit comprises drive apparatus, head and pinch roller, and described drive apparatus is connected with head by driving-belt, and described head is connected with separator, and described pinch roller is adjacent to the outside of driving-belt.
According to an aspect of the present utility model, described head is made up of housing, high-speed wheel, cross axle sleeve, lateral pin, hollow shaft, hanging axis and hanging axis coupling nut, described drive apparatus drives high-speed wheel rotation, described cross axle sleeve is fixed on high-speed wheel, described hollow shaft is fixed on housing by bearing, the upper end of described hanging axis is enclosed within hollow shaft, and be fixed on cross axle by lateral pin and put, described hanging axis coupling nut is fixed on the lower end of hanging axis, and described hanging axis is connected with separator respectively with hanging axis coupling nut.Pinch roller is made up of bent axle and shell, and described shell is fixed on bent axle by bearing.
According to an aspect of the present utility model, described cylindrical shell is connected with bottom end cover by screw or bolt, and described mixture is metal mixture or non-metal mixture.
The advantage that the utility model is implemented: because separator of the present utility model comprises classifying equipoment and hydrops gathering-device, described hydrops gathering-device is collected liquid mixture and the liquid that classifying equipoment is separated, described classifying equipoment comprises cylindrical shell, bottom end cover and grain size grading device, described cylindrical shell is connected with bottom end cover, described grain size grading device is arranged in bottom end cover, mixture is injected and in separator, is carried out separating treatment from the jet pipe of lower bearing equipment, apply cleverly seperator centrifugal force, the principle of tractive force, the diverse location that more short grained solid particle is drawn to cylinder inboard wall separates with oarse-grained solid particle, therefore the particle diameter of the solid particle of the micropowders seperator described in this practicality is superfine, be evenly distributed, rational in infrastructure, without grease contamination, intelligent degree is high, maintenance and convenient disassembly.
Brief description of the drawings
In order to be illustrated more clearly in the technical scheme in the utility model embodiment, to the accompanying drawing of required use in embodiment be briefly described below, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skill in the art, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is the schematic diagram of a kind of micropowders seperator described in the utility model;
Fig. 2 is the schematic diagram of the lower bearing equipment of a kind of micropowders seperator described in the utility model;
Fig. 3 is the schematic diagram of the head of a kind of micropowders seperator described in the utility model;
Fig. 4 is the schematic diagram of the classifying equipoment of a kind of micropowders seperator described in the utility model;
Fig. 5 is the schematic diagram of the particle outlet of a kind of micropowders seperator described in the utility model.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, Figure 2, shown in Fig. 3, Fig. 4, Fig. 5, a kind of micropowders seperator, comprise fuselage 1, control device 17, drive unit, lower bearing equipment 22 and separator, control device 17 is connected with drive unit, drive unit is connected with separator, lower bearing equipment 22 is positioned at the below of separator, and described separator comprises classifying equipoment 21 and hydrops gathering-device, and hydrops gathering-device is collected liquid mixture and the liquid that classifying equipoment 21 is separated; Described classifying equipoment 21 comprises cylindrical shell 12, bottom end cover 15 and grain size grading device 16, and cylindrical shell 12 is connected with bottom end cover 15, and grain size grading device 16 is arranged in bottom end cover 15.
In actual applications, as shown in Figure 2, lower bearing equipment 22 comprises liquid input device 7, step 2, bearing holder (housing, cover) 3 and bearing 4, step 2 is fixed on the bottom of fuselage 1, step 2 is provided with liquid inlet 5, liquid outlet 8 and path 10 correspondingly, liquid inlet 5 is connected with liquid input device 7 by woven hose 6, and liquid is selected water or free of contamination liquid.In order farthest to reduce the friction of bearing 4, the horizontal plane at the discharge outlet place of liquid outlet 8 is not less than the end face of bearing 4, that is to say when bearing 4 turns round and must all invade bubble having in water or free of contamination liquid, can not have the phenomenon of lack of water or free of contamination liquid, woven hose 6 is connected with the bottom of liquid input device 7, woven hose 6 is or/and liquid outlet 8 is provided with valve, valve is selected magnetic valve or conventional valve, the in-built full water of liquid input device 7 or free of contamination liquid, in order farthest to save cost, liquid is selected water, in order to facilitate the replacing of lower bearing equipment 22 spare and accessory parts, clean, save the operating time, strengthen operating efficiency, lower bearing equipment 22 also comprises bearing cap, stage clip, locking nut and gland, bearing cap is arranged on the surface of bearing holder (housing, cover) 3, stage clip is arranged between gland and bearing holder (housing, cover) 3, locking nut is connected with step 2 respectively by screw thread with gland, the replacing of spare and accessory parts like this, clean very convenient.
In actual applications, as shown in Figure 4, classifying equipoment 21 is made up of cylindrical shell 12, bottom end cover 15 and grain size grading device 16, cylindrical shell 12 is connected with bottom end cover 15 by screw or bolt, classifying equipoment 21 is isolated the solid particle of certain particle size range from liquid mixture, Gu particle is tiny solid particle, Gu the particle size range of particle can reach micron grade or nano-scale, minimum grain size scope can reach 1-10nm, the side of bottom end cover 15 is provided with four particle outlets 14 equably, and the side of grain size grading device 16 is provided with four passages 13 equably, and the position of passage 13 is corresponding with particle outlet 14, and the side at cylindrical shell 12 tops is provided with four liquid outlets 11 equably, as shown in Figure 5, particle outlet 14 comprises spray bar 36, spray sheet 37 and locking nut 34, spray sheet 37 is fixed on spray bar 36 by locking nut 34, the centre of spray sheet 37 is provided with spray film perforation 35, so admittedly, the large I of the particle diameter of particle is regulated and controled by the size of spraying film perforation 35, thereby reach the needed ideal product of client, when classifying equipoment 21 is in the situation that work is turned round, mixture liquid is processed by the grain size grading device 16 of classifying equipoment 21 inside under centrifugal action, oarse-grained solid particle is penetrated by spray film perforation 35 after grain size grading device 16 is processed, short grained solid particle is at centrifugal force, the top that enters cylindrical shell 12 with liquid under the forcing of tractive force separates, tiny solid particle is attached on the inwall of cylindrical shell 12, unnecessary liquid flows out from four liquid outlets 11 at cylindrical shell 12 tops, mixture can be metal mixture or non-metal mixture, and the particle size range of mixture can be micron grade or nano-scale.
In actual applications, drive unit comprises drive apparatus 18, head 19 and pinch roller, drive apparatus 18 is connected with head 19 by driving-belt, head 19 is connected with separator, pinch roller is adjacent to the outside of driving-belt, degree of tightness to driving-belt regulates, separator comprises classifying equipoment 21 and hydrops gathering-device, hydrops gathering-device comprises liquid collection part 20 and liquid mixture collection part 38, liquid collection part 20 is positioned at the top of fuselage 1, fluid collection device 20 is to collect water or the liquid that classifying equipoment is separated, within liquid mixture collection part 38 is positioned at fuselage 1, it is to collect the liquid mixture that classifying equipoment is separated that liquid mixture is collected part 38, as shown in Figure 3, head 19 is by housing 29, high-speed wheel 23, cross axle sleeve 24, lateral pin 25, hollow shaft 31, hanging axis 32 and hanging axis coupling nut 33 form, drive apparatus 18 drives high-speed wheel 23 to rotate by driving-belt, cross axle sleeve 24 is fixed on high-speed wheel 23, hollow shaft 31 is fixed on housing 29 by bearing arrangement, bearing arrangement comprises bearing 1, gland 1, outer bearing sleeve 28, internal bearing sleeve 30, the upper end of hanging axis 32 is enclosed within hollow shaft 31, and be fixed on cross axle sleeve 24 by lateral pin 25, hanging axis coupling nut 33 is fixed on the lower end of hanging axis 32, hanging axis 32 is connected with classifying equipoment 21 respectively with hanging axis coupling nut 33, head 19 can drive classifying equipoment 21 to rotate like this, classifying equipoment 21 is in the situation of running up, material is by dividing solid and liquid layered to leave in classifying equipoment 21 inside under the effect of centrifugal force, the solid particle of fine particle is evenly distributed on cylindrical shell 12 inwalls of classifying equipoment 21, oarse-grained solid particle is discharged by spray film perforation 35 after grain size grading device 16 is processed.
In addition, in order to improve the intelligent degree of micropowders seperator, control device 17 comprises PLC controller, frequency converter, relay, power supply and man-machine interface display, relay is connected with power supply, PLC controller is connected with relay, frequency converter and man-machine interface display respectively, frequency converter is connected with drive unit correspondingly, realize like this speed whether control device 17 accessory drives rotate and rotate, by installing control device 17 additional, can realize speed any rotating speed between 0-20000 rev/min of classifying equipoment 21.
Operation principle of the present utility model: opening power, start control device 17 associated button, drive apparatus 18 rotates, drive apparatus 18 drives high-speed wheel 23 to rotate by driving-belt, high-speed wheel 23 drives hanging axis 32 to rotate, because hanging axis coupling nut 33 is fixed on the lower end of hanging axis 32, hanging axis 32 is connected with classifying equipoment 21 respectively with hanging axis coupling nut 33, head 19 can drive classifying equipoment 21 to produce High Rotation Speed like this, classifying equipoment 21 is in the situation of running up, liquid mixture is injected and in classifying equipoment 21, is carried out classification processing by the jet pipe 9 in lower bearing equipment 22, oarse-grained solid particle is penetrated by spray film perforation 35 after grain size grading device 16 is processed, entering into liquid mixture collects in part 38, be discharged in cell therefor by pipeline, the top that short grained solid particle enters cylindrical shell 12 with liquid under the forcing of centrifugal force, tractive force separates, tiny solid particle is attached on the inwall of cylindrical shell 12, unnecessary liquid flows out from the liquid outlet 11 at cylindrical shell 12 tops, enter in liquid collection part 20, be discharged in cell therefor by pipeline, lower bearing equipment 22 adopts water to be lubricated, the inside that water enters step 2 by woven hose 6 from liquid inlet 5 is lubricated, namely to being lubricated between bearing holder (housing, cover) 3 and step 2, reduce the frictional dissipation of seperator bearing 4 in the time running up, last water is discharged from liquid outlet 8, lubricated without increasing other device, compact conformation, realize solid particle material without grease contamination, break through the grease atomization that cannot solve existence in the middle of industry routine and polluted, the product quality various factors that waits not up to standard.Therefore the particle diameter of micropowders seperator of the present utility model superfine, be evenly distributed, rational in infrastructure, high, simple to operate without grease contamination, intelligent degree, maintenance and convenient disassembly.
The above; it is only detailed description of the invention of the present utility model; but protection domain of the present utility model is not limited to this; the technical staff of any skilled is in the disclosed technical scope of the utility model; the variation that can expect easily or replacement, within all should being encompassed in protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of described claim.
Claims (10)
1. a micropowders seperator, comprise fuselage, control device, drive unit, lower bearing equipment and separator, described control device is connected with drive unit, described drive unit is connected with separator, described lower bearing equipment is positioned at the below of separator, it is characterized in that: described separator comprises classifying equipoment and hydrops gathering-device, described hydrops gathering-device is collected liquid mixture and the liquid that classifying equipoment is separated; Described classifying equipoment comprises cylindrical shell, bottom end cover and grain size grading device, and described cylindrical shell is connected with bottom end cover, and described grain size grading device is arranged in bottom end cover.
2. according to micropowders seperator described in claim 1, it is characterized in that: the side of described bottom end cover is provided with particle outlet, the side of described grain size grading device is provided with passage, and the position of described passage is corresponding with particle outlet; The side at described cylindrical shell top is provided with liquid outlet.
3. according to micropowders seperator described in claim 2, it is characterized in that: described particle outlet comprises spray bar, spray sheet and locking nut, described spray sheet is fixed on spray bar by locking nut, and the centre of described spray sheet is provided with spray film perforation.
4. according to micropowders seperator described in claim 1, it is characterized in that: described classifying equipoment is isolated the solid particle of certain particle size range from liquid mixture, described particle size range is micron grade or nano-scale; Described hydrops gathering-device comprises liquid collection part and liquid mixture collection part, described liquid collection part is positioned at the top of fuselage, fluid collection device is to collect water or the liquid that classifying equipoment is separated, within described liquid mixture is collected and is partly positioned at fuselage, it is to collect the liquid mixture that classifying equipoment is separated that liquid mixture is collected part.
5. according to micropowders seperator described in claim 4, it is characterized in that: described particle size range is 1-10nm.
6. according to micropowders seperator described in claim 1, it is characterized in that: described lower bearing equipment comprises liquid input device, step, bearing holder (housing, cover) and bearing, described step is fixed on the bottom of fuselage, described step is provided with liquid inlet, liquid outlet and passage correspondingly, described liquid inlet is connected with liquid input device by woven hose, and described liquid is water or free of contamination liquid.
7. according to micropowders seperator described in claim 6, it is characterized in that: described woven hose is connected with the bottom of liquid input device, and described woven hose is or/and liquid outlet is provided with valve; The horizontal plane at the discharge outlet place of described liquid outlet is not less than the end face of bearing.
8. according to micropowders seperator described in claim 1, it is characterized in that, described drive unit comprises drive apparatus, head and pinch roller, and described drive apparatus is connected with head by driving-belt, described head is connected with separator, and described pinch roller is adjacent to the outside of driving-belt.
9. according to micropowders seperator described in claim 8, it is characterized in that: described head is by housing, high-speed wheel, cross axle sleeve, lateral pin, hollow shaft, hanging axis and hanging axis coupling nut composition, described drive apparatus drives high-speed wheel rotation, described cross axle sleeve is fixed on high-speed wheel, described hollow shaft is fixed on housing by bearing, the upper end of described hanging axis is enclosed within hollow shaft, and be fixed on cross axle by lateral pin and put, described hanging axis coupling nut is fixed on the lower end of hanging axis, described hanging axis is connected with separator respectively with hanging axis coupling nut, pinch roller is made up of bent axle and shell, described shell is fixed on bent axle by bearing.
10. according to the arbitrary described micropowders seperator of claim 1 to 9, it is characterized in that: described cylindrical shell is connected with bottom end cover by screw or bolt, and described mixture is metal mixture or non-metal mixture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320876955.4U CN203635340U (en) | 2013-12-27 | 2013-12-27 | Super-micro-fine powder separator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320876955.4U CN203635340U (en) | 2013-12-27 | 2013-12-27 | Super-micro-fine powder separator |
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| CN203635340U true CN203635340U (en) | 2014-06-11 |
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| CN201320876955.4U Expired - Fee Related CN203635340U (en) | 2013-12-27 | 2013-12-27 | Super-micro-fine powder separator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689925A (en) * | 2015-03-09 | 2015-06-10 | 彭建国 | Multistage classifier and classification method of superfine diamond micro-powder particles |
| CN108285476A (en) * | 2018-04-17 | 2018-07-17 | 河南工业大学 | A kind of eddy flow extrusion separator |
-
2013
- 2013-12-27 CN CN201320876955.4U patent/CN203635340U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689925A (en) * | 2015-03-09 | 2015-06-10 | 彭建国 | Multistage classifier and classification method of superfine diamond micro-powder particles |
| CN108285476A (en) * | 2018-04-17 | 2018-07-17 | 河南工业大学 | A kind of eddy flow extrusion separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhou Yi Inventor before: Zhou Yi Inventor before: Zhou Jun |
|
| CB03 | Change of inventor or designer information | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170420 Address after: 201699 Shanghai City, Songjiang District song No. 2 building 13 room 214 meters Patentee after: Shanghai Jiayi liquid separation technology Co., Ltd. Address before: 201502 Jinshan District Fengjing town Shanghai City Xing Fang Road No. 565 building 3 room 129 Patentee before: Good firm (Shanghai) plant equipment Co., Ltd |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140611 Termination date: 20191227 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |