CN205851387U - Magnesium stearate pneumatic separation device - Google Patents
Magnesium stearate pneumatic separation device Download PDFInfo
- Publication number
- CN205851387U CN205851387U CN201620858794.XU CN201620858794U CN205851387U CN 205851387 U CN205851387 U CN 205851387U CN 201620858794 U CN201620858794 U CN 201620858794U CN 205851387 U CN205851387 U CN 205851387U
- Authority
- CN
- China
- Prior art keywords
- magnesium stearate
- cyclone separator
- connects
- air outlet
- separation device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 title claims abstract description 126
- 235000019359 magnesium stearate Nutrition 0.000 title claims abstract description 63
- 238000000926 separation method Methods 0.000 title claims abstract description 18
- 238000007701 flash-distillation Methods 0.000 claims abstract description 31
- 238000007599 discharging Methods 0.000 claims abstract description 21
- 238000002156 mixing Methods 0.000 claims abstract description 12
- 239000011148 porous material Substances 0.000 claims abstract description 8
- 239000004744 fabric Substances 0.000 claims description 20
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical group C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 2
- 239000002699 waste material Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 description 11
- 239000000463 material Substances 0.000 description 11
- 238000002360 preparation method Methods 0.000 description 6
- 238000012216 screening Methods 0.000 description 4
- 230000008676 import Effects 0.000 description 3
- DKXULEFCEORBJK-UHFFFAOYSA-N magnesium;octadecanoic acid Chemical compound [Mg].CCCCCCCCCCCCCCCCCC(O)=O DKXULEFCEORBJK-UHFFFAOYSA-N 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- DCXXMTOCNZCJGO-UHFFFAOYSA-N tristearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
Landscapes
- Cyclones (AREA)
Abstract
nullThis utility model relates to a kind of magnesium stearate pneumatic separation device，Feeding mouth including flash distillation dryer connects with feed unit，The air outlet of flash distillation dryer connects with the charging aperture of cyclone separator，Cyclone separator has been arranged in series many groups，The lower end discharging opening being positioned at cyclone separator connects with vibration batch mixing sieve charging aperture，Cyclone separator is provided with air outlet and connects with the air inlet of cleaner unit，The dividing plate that cleaner unit is arranged in including Xiang Ke inner cavity chamber，Case shell is divided into two chambers of above-below direction by dividing plate，It is positioned on dividing plate and is provided with intercommunicating pore，It is provided with dust-removal cloth-bag in chamber above，The opening of dust-removal cloth-bag is fixed on intercommunicating pore，The blind end of dust-removal cloth-bag is fixed on oscillating deck，Above-mentioned cyclone separator has been arranged in series many groups，Magnesium stearate can be reduced derive to cleaner unit from the air outlet of cyclone separator，By mobile oscillating deck，The magnesium stearate put aside in dust-removal cloth-bag is shaken off down，The waste of magnesium stearate in minimizing device.
Description
Technical field
This utility model relates to granular material dry wind selecting technology field, is specifically related to a kind of magnesium stearate pneumatic separation device.
Background technology
Magnesium stearate is relatively broad in field application such as pharmacy, cosmetics, stabilizer and lubricants, dried stearic acid
Magnesium is powder, and magnesium stearate is during preparation, and needs are dried, sorting etc. operates can prepare dry powder
Shape magnesium stearate particles.Existing magnesium stearate is during preparation, first with flash dryer, by moistening stearic acid
Magnesium is dried, and then utilizes cyclone separator that the magnesium stearate of preliminarily dried is carried out rotation and breaks up, at cyclone separator
It is provided with the batch mixing sieve of vibrations below discharging opening, utilizes the vibrations that batch mixing sieves, thus filter out the stearic acid of different grain size size
Magnesium, during above-mentioned magnesium stearate preparation, above-mentioned cyclone separator is only provided with one group, in the process of actual sorting
In, the air outlet of cyclone separator there is also a certain amount of for sedimentation under magnesium stearate particles and taken out of by rotary wind, cause
Magnesium stearate, during preparation, occurs that larger amount of race leaks phenomenon, and the air outlet of cyclone separator is connected with cleaner unit, leads
Accumulating substantial amounts of magnesium stearate in causing cleaner unit, the powder stearic acid magnesium under filtering cannot be received by existing cleaner unit
Collection, in turn results in the waste of substantial amounts of magnesium stearate, and runs the dust spilt often such that the filter element of cleaner unit blocks,
And then have a strong impact on the filter effect of cleaner unit, owing to the filter element of cleaner unit blocks, cause the rotation in cyclone separator
Wind-force declines, and then further results in the cyclone separator dispersion effect to magnesium stearate, thus seriously reduces magnesium stearate
Preparation efficiency.
Utility model content
The purpose of this utility model is: provides a kind of magnesium stearate pneumatic separation device, not only guarantees the whirlwind of cyclone separator
Effect, and the magnesium stearate put aside in cleaner unit can be collected, it is to avoid while magnesium stearate waste, improve tristearin
The preparation efficiency of acid magnesium.
For achieving the above object, the technical solution adopted in the utility model is:
Magnesium stearate pneumatic separation device, including the flash distillation dryer for magnesium stearate is dried, described flash distillation dryer
Feeding mouth connects with feed unit；
Cyclone separator, the air outlet of flash distillation dryer connects with the charging aperture of cyclone separator, described cyclone separator
Being arranged in series many groups, the air outlet between adjacent cyclones separator connects with air inlet；
Described cyclone separator is the back taper tubular structure of vertical, be positioned at cyclone separator lower end discharging opening and
Charging aperture connects, and vibration batch mixing sieve is provided with discharging opening；
Described cyclone separator is provided with air outlet and connects with the air inlet of cleaner unit；
Described cleaner unit includes case shell, is provided with the dividing plate of plate face level in described Xiang Ke inner cavity chamber, and described dividing plate is by case
Shell is divided into two chambers of above-below direction, is positioned on dividing plate and is provided with intercommunicating pore, is provided with dust removing cloth in chamber above
Bag, the opening of described dust-removal cloth-bag is fixed on intercommunicating pore, and the blind end of dust-removal cloth-bag is fixed on oscillating deck, described oscillating deck
Slidingtype is arranged on case shell.
This utility model there is also following characteristics:
The upper face of described dividing plate is provided with connecting tube, and the opening of described dust-removal cloth-bag is pricked and is located in connecting tube, described every
The lower section of plate is provided with collecting bin, the inverted cone-shaped structure that the upper end open of described collecting bin is big, lower end is little, and the lower end of collecting bin sets
Being equipped with discharge gate, described lower chamber is provided with the opening air outlet with cyclone separator by pipeline connection, chamber, described top
Room is provided with the air inlet connection of opening and the first blower fan, the air outlet of the first blower fan and atmosphere.
Described cyclone separator is provided with two groups.
Flash distillation dryer is the tubular structure of vertical, and the lower end mouth of pipe being positioned at flash distillation dryer is provided with the second wind
Machine, the air inlet of described second blower fan connects with xeothermic wind regime, and the air outlet of described second blower fan points under flash distillation dryer
The end mouth of pipe, it is arranged above that described feed unit is positioned at the second fan outlet.
Described feed unit includes feeder sleeve, and one end mouth of pipe of described feeder sleeve connects with the tube chamber of flash distillation dryer,
The tube chamber being positioned at feeder sleeve is provided with spiral conveyor rod, and one end of spiral conveyor rod connects with the rotation of the first motor, is positioned at
Being provided with feed hopper on feeder sleeve, the lower end of described feed hopper connects with feeder sleeve.
Described second blower fan includes outer housing, is provided with blade, the drive shaft of described blade and the second motor in described outer housing
Be rotationally connected.
Described vibration batch mixing sieve case, the upper end of described case is arranged to the lower end discharging opening of charging aperture and cyclone separator
Connection, the vertical direction in case is provided with multilayer screen cloth, and the mesh diameter of described screen cloth from top to bottom tapers into, and screen cloth sets
Being set to up-small and down-big pyramidal structure, the case outer wall at the low side place being positioned at screen cloth is provided with discharging opening, is positioned under case
End arranges gripper shoe, described gripper shoe and rod hinge connection, and the other end of connecting rod is hinged with the eccentric segment of eccentric, the wheel of eccentric
Core and the 3rd motor connect, and the lower section of described gripper shoe is provided with spring, and the upper end of described spring is solid with the lower face of gripper shoe
Calmly, the lower end of spring is fixed with the cylinder of fixing cylinder.
Being provided with clasp between described multilayer screen cloth, described clasp is provided with opening, and one end of described opening is hinged to be set
Being equipped with fastening bolt, described fastening bolt passes the opening other end outer wall of clasp and is provided with clamp nut.
The lower end discharging opening of described cyclone separator is provided with Blowing stopper.
Compared with prior art, the technique effect that this utility model possesses is: magnesium stearate to be dried is by feed unit
Put into, import in flash distillation dryer under the effect of feed unit, thus implement material to be dried, at the spiral shell of cyclone separator
Under rotation wind action, the magnesium stearate material being dried in flash distillation dryer enters in cyclone separator, the rotation of cyclone separator
Turn wind so that dry magnesium stearate separates and breaks up, and magnesium stearate is settled down to cyclone separator under the effect of self gravitation
Discharging opening position, lower end, and imported vibration batch mixing sieve by lower end discharging opening, thus realize the magnesium stearate material to different-grain diameter
Screening, above-mentioned cyclone separator has been arranged in series many groups such that it is able to the full extent reduce magnesium stearate divide from whirlwind
Air outlet from device is derived to cleaner unit, when the amount of the magnesium stearate imported in cleaner unit is too much, by mobile oscillating deck,
So that dust-removal cloth-bag is in the state rocked, and then the magnesium stearate put aside in dust-removal cloth-bag being shaken off down, it is right to complete
The collection of the magnesium stearate of savings in cleaner unit, the waste of magnesium stearate in minimizing device.
Accompanying drawing explanation
Fig. 1 is the structural representation of magnesium stearate pneumatic separation device；
Fig. 2 is flash distillation dryer and the second blower fan attachment structure generalized section；
Fig. 3 is the generalized section of vibration batch mixing sieve；
Fig. 4 is the generalized section of cleaner unit；
Fig. 5 is the structural representation of clasp.
Detailed description of the invention
In conjunction with Fig. 1 to Fig. 5, the utility model is further described:
Magnesium stearate pneumatic separation device, including the flash distillation dryer 10 for being dried magnesium stearate, described flash distillation dryer
The feeding mouth of 10 connects with feed unit；
Cyclone separator 20, the air outlet of flash distillation dryer 10 connects with the charging aperture of cyclone separator 20, described whirlwind
Separator 20 has been arranged in series many groups, and the air outlet between adjacent cyclones separator 20 connects with air inlet；
The described cyclone separator 20 back taper tubular structure in vertical, is positioned at the lower end discharging opening of cyclone separator 20
With charging aperture connect, vibration batch mixing sieve 30 is provided with discharging opening；
Described cyclone separator 20 is provided with air outlet and connects with the air inlet of cleaner unit 40；
Described cleaner unit 40 includes case shell 41, is provided with the dividing plate 42 of plate face level in described Xiang Ke 41 inner cavity chamber, described
Case shell 41 is divided into two chambers of above-below direction by dividing plate 42, is positioned on dividing plate 42 and is provided with intercommunicating pore 421, chamber above
Indoor are provided with dust-removal cloth-bag 43, and the opening of described dust-removal cloth-bag 43 is fixed on intercommunicating pore 411, the closing of dust-removal cloth-bag 43
End is fixed on oscillating deck 44, and described oscillating deck 44 slidingtype is arranged on case shell 41.
Shown in Fig. 1, magnesium stearate to be dried is put into by feed unit, imports flash distillation under the effect of feed unit
In exsiccator 10, thus implement material to be dried, under the spiral wind action of cyclone separator 20, in flash distillation dryer 10
The magnesium stearate material being dried enter in cyclone separator 20, the rotary wind of cyclone separator 20 makes the magnesium stearate being dried
Separation is broken up, and magnesium stearate is settled down to the discharging opening position, lower end of cyclone separator 20 under the effect of self gravitation, and by under
End discharging opening imports vibration batch mixing sieve 30, thus realizes the screening of the magnesium stearate material to different-grain diameter, and above-mentioned whirlwind divides
Many groups have been arranged in series it such that it is able to reducing magnesium stearate to the full extent derives from the air outlet of cyclone separator 20 from device 20
To cleaner unit 40 such that it is able to reducing magnesium stearate to the full extent derives to cleaner unit from the air outlet of cyclone separator 20
In 40, when the amount of the magnesium stearate imported in cleaner unit 40 is too much, by mobile oscillating deck 44, so that dust-removal cloth-bag 43
It is in the state rocked, and then the magnesium stearate of savings in dust-removal cloth-bag 43 is shaken off down, complete savings in cleaner unit 40
The collection of magnesium stearate, reduce the waste of magnesium stearate in device.
As preferred version of the present utility model, shown in Fig. 4, for convenience of installation to dust-removal cloth-bag 43, described every
The upper face of plate 42 is provided with connecting tube 422, and the opening of described dust-removal cloth-bag 43 is pricked and is located in connecting tube 422, for convenience of to removing
The magnesium stearate shaken off down in dirt cloth bag 43 is collected, and the lower section of described dividing plate 42 is provided with collecting bin 45, described in gather materials
The inverted cone-shaped structure that the upper end open in storehouse 45 is big, lower end is little, the lower end of collecting bin 45 is provided with discharge gate 451, chamber, described lower section
Room is provided with the air outlet of opening and cyclone separator and passes through pipeline connection, and described upper chambers is provided with opening and the first blower fan
The air inlet connection of 50, the air outlet of the first blower fan 50 and atmosphere.
Further, described cyclone separator 20 is provided with two groups, the air outlet of described cleaner unit 40 and the first blower fan
The air inlet connection of 50, two groups of above-mentioned cyclone separator 20 can realize the sedimentation to most of magnesium stearate material,
Thus the magnesium stearate particles greatly reducing dust-like enters in cleaner unit 40, and then guarantee the dedusting effect of cleaner unit 40
Really, the first blower fan 50 starts, and also serves as the source of the interior rotary wind of cyclone separator 20.
Further, the flash distillation dryer 10 tubular structure in vertical, it is positioned at the lower end mouth of pipe of flash distillation dryer 10
Being provided with the second blower fan 60, the air inlet of described second blower fan 60 connects with xeothermic wind regime, the air outlet of described second blower fan 60
Pointing to the lower end mouth of pipe of flash distillation dryer 10, it is arranged above that described feed unit is positioned at the second blower fan 60 air outlet.Doing at this
Hot air source can be to be steam heating or electrically heated mode, it is possible to provides the hot blast being dried i.e. to the tube chamber of flash distillation dryer 10
Can, under the wind-force effect of the second blower fan 60, the dried magnesium stearate of flash distillation dryer 10 is imported cyclone separator 20
In.
Specifically, described feed unit includes feeder sleeve 11, one end mouth of pipe of described feeder sleeve 11 and flash distillation dryer
The tube chamber connection of 10, the tube chamber being positioned at feeder sleeve 11 is provided with spiral conveyor rod 12, one end of spiral conveyor rod 12 and first
The rotation connection of motor 13, is positioned on feeder sleeve 11 and is provided with feed hopper 14, and the lower end of described feed hopper 14 is with feeder sleeve 11 even
Logical.
Further, shown in Fig. 2, described second blower fan 60 includes outer housing 61, is provided with leaf in described outer housing 61
Sheet 62, the drive shaft of described blade 62 is rotationally connected with the second motor 63.Under the effect of the second motor 63,62 turns of blade
Dynamic, thus realize the magnesium stearate material in flash distillation dryer 10 is dried.
More specifically, shown in Fig. 3, described vibration batch mixing sieves 30 cases 31, and the upper end of described case 31 is arranged to
Charging aperture connects with the lower end discharging opening of cyclone separator 20, and the vertical direction in case 31 is provided with multilayer screen cloth 32, described
The mesh diameter of screen cloth 32 from top to bottom tapers into, and screen cloth 32 is arranged to up-small and down-big pyramidal structure, is positioned at screen cloth 32
Case 31 outer wall at low side place is provided with discharging opening 33, and the lower end being positioned at case 31 arranges gripper shoe 34, described gripper shoe 34
Hinged with connecting rod 35, the other end of connecting rod 35 is hinged with the eccentric segment of eccentric 36, the core wheel of eccentric 36 and the 3rd motor 37
Connecting, the lower section of described gripper shoe 34 is provided with spring 39, and the upper end of described spring 39 is fixed with the lower face of gripper shoe 34, bullet
The cylinder of the lower end of spring 39 and fixing cylinder 391 is fixed.Above-mentioned screen cloth 32 is arranged to pyramidal structure, is guaranteeing material screening
Meanwhile, the material after screening can all be settled down to the low side of screen cloth 32, and then is derived by discharging opening 33.
For convenience of realizing the installation to screen cloth 32 and fixing, shown in Fig. 5, being provided with between described multilayer screen cloth 32
Clasp 38, described clasp 38 is provided with opening, the hinged fastening bolt 381 that is provided with in one end of described opening, described fastening bolt
381 through the opening other end outer walls of clasp 38 and are provided with clamp nut.
It is obvious to a person skilled in the art that this utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of without departing substantially from spirit or essential attributes of the present utility model, it is possible to realize this practicality in other specific forms new
Type.Therefore, no matter from the point of view of which point, all should regard embodiment as exemplary, and be nonrestrictive, this practicality is new
The scope of type is limited by claims rather than described above, it is intended that by the containing of equivalency in claim that fall
All changes in justice and scope are included in this utility model.Should not be considered as any reference in claim limiting
Involved claim.
Although moreover, it will be appreciated that this specification is been described by according to embodiment, but the most each embodiment only wraps
Containing an independent technical scheme, this narrating mode of description is only that for clarity sake those skilled in the art should
Description can also be formed those skilled in the art through appropriately combined as an entirety, the technical scheme in each embodiment
May be appreciated other embodiments.
Claims (9)
1. magnesium stearate pneumatic separation device, it is characterised in that include the flash distillation dryer (10) for magnesium stearate is dried, described
The feeding mouth of flash distillation dryer (10) connects with feed unit；
Cyclone separator (20), the air outlet of flash distillation dryer (10) connects with the charging aperture of cyclone separator (20), described rotation
Wind separator (20) has been arranged in series many groups, and the air outlet between adjacent cyclones separator (20) connects with air inlet；
The described cyclone separator (20) the back taper tubular structure in vertical, is positioned at the lower end discharging opening of cyclone separator (20)
With charging aperture connect, vibration batch mixing sieve (30) be provided with discharging opening；
Described cyclone separator (20) is provided with air outlet and connects with the air inlet of cleaner unit (40)；
Described cleaner unit (40) includes case shell (41), is provided with the dividing plate (42) of plate face level in described case shell (41) inner cavity chamber,
Case shell (41) is divided into two chambers of above-below direction by described dividing plate (42), is positioned on dividing plate (42) and is provided with intercommunicating pore
(421), being provided with dust-removal cloth-bag (43) in chamber above, the opening of described dust-removal cloth-bag (43) is fixed on intercommunicating pore
(421) on, the blind end of dust-removal cloth-bag (43) is fixed on oscillating deck (44), and described oscillating deck (44) slidingtype is arranged on case shell
(41) on.
Magnesium stearate pneumatic separation device the most according to claim 1, it is characterised in that the upper face of described dividing plate (42) is arranged
Having connecting tube (422), the opening of described dust-removal cloth-bag (43) is pricked and is located in connecting tube (422), and the lower section of described dividing plate (42) sets
It is equipped with collecting bin (45), the inverted cone-shaped structure that upper end open is big, lower end is little of described collecting bin (45), the lower end of collecting bin (45)
Being provided with discharge gate (451), described lower chamber is provided with the air outlet of opening and cyclone separator and passes through pipeline connection, described
Upper chambers is provided with the air inlet connection of opening and the first blower fan (50), the air outlet of the first blower fan (50) and atmosphere.
Magnesium stearate pneumatic separation device the most according to claim 1 and 2, it is characterised in that described cyclone separator (20) sets
It is equipped with two groups.
Magnesium stearate pneumatic separation device the most according to claim 3, it is characterised in that flash distillation dryer (10) is in vertical
Tubular structure, the lower end mouth of pipe being positioned at flash distillation dryer (10) is provided with the second blower fan (60), described second blower fan (60)
Air inlet connects with xeothermic wind regime, and the air outlet of described second blower fan (60) points to the lower end mouth of pipe of flash distillation dryer (10), institute
Stating feed unit, to be positioned at the second blower fan (60) air outlet arranged above.
Magnesium stearate pneumatic separation device the most according to claim 4, it is characterised in that described feed unit includes feeder sleeve
(11), one end mouth of pipe of described feeder sleeve (11) connects with the tube chamber of flash distillation dryer (10), is positioned at the tube chamber of feeder sleeve (11)
Inside being provided with spiral conveyor rod (12), one end of spiral conveyor rod (12) connects with the rotation of the first motor (13), is positioned at feed
Being provided with feed hopper (14) on pipe (11), the lower end of described feed hopper (14) connects with feeder sleeve (11).
Magnesium stearate pneumatic separation device the most according to claim 5, it is characterised in that described second blower fan (60) includes outer housing
(61), being provided with blade (62) in described outer housing (61), the drive shaft of described blade (62) connects with the rotation of the second motor (63)
Connect.
Magnesium stearate pneumatic separation device the most according to claim 1, it is characterised in that described vibration batch mixing sieve (30) case
(31), the upper end of described case (31) is arranged to charging aperture and connects with the lower end discharging opening of cyclone separator (20), case (31)
Interior vertical direction is provided with multilayer screen cloth (32), and the mesh diameter of described screen cloth (32) from top to bottom tapers into, screen cloth
(32) being arranged to up-small and down-big pyramidal structure, case (31) outer wall at the low side place being positioned at screen cloth (32) is provided with discharging opening
(33), the lower end being positioned at case (31) arranges gripper shoe (34), and described gripper shoe (34) is hinged with connecting rod (35), connecting rod (35)
The other end is hinged with the eccentric segment of eccentric (36), and the core wheel of eccentric (36) and the 3rd motor (37) connect, described gripper shoe
(34) lower section is provided with spring (39), and the lower face of the upper end of described spring (39) and gripper shoe (34) is fixed, spring (39)
The cylinder of lower end and fixing cylinder (391) fix.
Magnesium stearate pneumatic separation device the most according to claim 7, it is characterised in that setting between described multilayer screen cloth (32)
Being equipped with clasp (38), described clasp (38) is provided with opening, and one end of described opening is hinged is provided with fastening bolt (381), institute
State fastening bolt (381) and through the opening other end outer wall of clasp (38) and be provided with clamp nut.
Magnesium stearate pneumatic separation device the most according to claim 1, it is characterised in that the lower end of described cyclone separator (20)
Discharging opening is provided with Blowing stopper (70).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620858794.XU CN205851387U (en) | 2016-08-09 | 2016-08-09 | Magnesium stearate pneumatic separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620858794.XU CN205851387U (en) | 2016-08-09 | 2016-08-09 | Magnesium stearate pneumatic separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205851387U true CN205851387U (en) | 2017-01-04 |
Family
ID=57657423
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620858794.XU Expired - Fee Related CN205851387U (en) | 2016-08-09 | 2016-08-09 | Magnesium stearate pneumatic separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205851387U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112958257A (en) * | 2021-04-07 | 2021-06-15 | 北辰先进循环科技(青岛)有限公司 | Waste lithium ion power battery protection crushing process equipment |
| CN117299551A (en) * | 2023-06-26 | 2023-12-29 | 重庆聚购科技发展有限公司 | Integrated equipment and method for preparing and screening siliceous quartz micropowder for fracturing proppant |
-
2016
- 2016-08-09 CN CN201620858794.XU patent/CN205851387U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112958257A (en) * | 2021-04-07 | 2021-06-15 | 北辰先进循环科技(青岛)有限公司 | Waste lithium ion power battery protection crushing process equipment |
| CN117299551A (en) * | 2023-06-26 | 2023-12-29 | 重庆聚购科技发展有限公司 | Integrated equipment and method for preparing and screening siliceous quartz micropowder for fracturing proppant |
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