CN205851125U - Magnesium stearate aidr bells blast system - Google Patents

Magnesium stearate aidr bells blast system Download PDF

Info

Publication number
CN205851125U
CN205851125U CN201620858766.8U CN201620858766U CN205851125U CN 205851125 U CN205851125 U CN 205851125U CN 201620858766 U CN201620858766 U CN 201620858766U CN 205851125 U CN205851125 U CN 205851125U
Authority
CN
China
Prior art keywords
cyclone separator
magnesium stearate
connects
air outlet
flash distillation
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
Application number
CN201620858766.8U
Other languages
Chinese (zh)
Inventor
石文生
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anhui Furong Chinese Herbal Medicine Co Ltd
Original Assignee
Anhui Furong Chinese Herbal Medicine Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Anhui Furong Chinese Herbal Medicine Co Ltd filed Critical Anhui Furong Chinese Herbal Medicine Co Ltd
Priority to CN201620858766.8U priority Critical patent/CN205851125U/en
Application granted granted Critical
Publication of CN205851125U publication Critical patent/CN205851125U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Cyclones (AREA)

Abstract

This utility model relates to a kind of magnesium stearate aidr bells blast system, and including the flash distillation dryer for being dried magnesium stearate, the feeding mouth of flash distillation dryer connects with feed unit;The air outlet of flash distillation dryer connects with the charging aperture of cyclone separator, and cyclone separator has been arranged in series many groups, and the air outlet between adjacent cyclones separator connects with air inlet;Cyclone separator is the back taper tubular structure of vertical, be positioned at the lower end discharging opening of cyclone separator with charging aperture connect, vibration batch mixing sieve is provided with discharging opening;Cyclone separator is provided with air outlet and connects with the air inlet of cleaner unit.Above-mentioned cyclone separator has been arranged in series many groups, derive to cleaner unit it is thus possible to reduce magnesium stearate to the full extent from the air outlet of cyclone separator, and then avoid the blocking of dust removing units in cleaner unit, guarantee the rotating wind in cyclone separator, thus improve the preparation efficiency of magnesium stearate.

Description

Magnesium stearate aidr bells blast system
Technical field
This utility model relates to granular material dry wind selecting technology field, is specifically related to a kind of magnesium stearate aidr bells blast system.
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, runs Spill bigger dust often such that the filter element of cleaner unit blocks, and then have a strong impact on the filter effect of cleaner unit, due to The filter element blocking of cleaner unit, causes the rotating wind in cyclone separator to decline, and then further results in cyclone separator Dispersion effect to magnesium stearate, thus seriously reduce the preparation efficiency of magnesium stearate.
Utility model content
The purpose of this utility model is: provide a kind of magnesium stearate aidr bells blast system, it is ensured that the cyclone effect of cyclone separator While, it is to avoid with the blocking of the cleaner unit that the air outlet of cyclone separator connects, improve the preparation efficiency of magnesium stearate.
For achieving the above object, the technical solution adopted in the utility model is:
Magnesium stearate aidr bells blast system, 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.
This utility model there is also following characteristics:
Described cyclone separator is provided with two groups, the air outlet of described cleaner unit and the air inlet connection of the first blower fan, the The air outlet of one first blower fan and atmosphere.
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.
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 in cleaner unit, and then avoids the blocking of dust removing units in cleaner unit, it is ensured that in cyclone separator Rotating wind, thus improve the preparation efficiency of magnesium stearate.
Accompanying drawing explanation
Fig. 1 is the structural representation of magnesium stearate aidr bells blast system;
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.
Detailed description of the invention
In conjunction with Fig. 1 to Fig. 3, the utility model is further described:
Magnesium stearate aidr bells blast system, 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.
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, and then avoid the blocking of dust removing units in cleaner unit 40, it is ensured that the rotating wind in cyclone separator 20, Thus improve the preparation efficiency of magnesium stearate.
As preferred version of the present utility model, described cyclone separator 20 is provided with two groups, going out of described cleaner unit 40 Air port connects with the air inlet of the first blower fan 50, the air outlet of the one the first blower fans 50 and atmosphere.Two groups of above-mentioned whirlwind Separator 20 can realize the sedimentation to most of magnesium stearate material, thus greatly reduces the stearic acid of dust-like Magnesium granules enters in cleaner unit 40, and then guarantees the dust removing effects of cleaner unit 40, and the first blower fan 50 starts, and also serves as cyclonic separation The source of the interior rotary wind of device 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 Connect.Above-mentioned screen cloth 32 is arranged to pyramidal structure, and while guaranteeing material screening, the material after screening can all sink It is down to the low side of screen cloth 32, and then is derived by discharging opening 33.
For realizing the lock gas to cyclone separator 20, the lower end discharging opening of described cyclone separator 20 is provided with Blowing stopper 70。
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 (7)

1. magnesium stearate aidr bells blast system, 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).
Magnesium stearate aidr bells blast system the most according to claim 1, it is characterised in that described cyclone separator (20) is provided with Two groups, the air inlet connection of the air outlet of described cleaner unit (40) and the first blower fan (50), the air outlet of the first blower fan (50) with Atmosphere.
Magnesium stearate aidr bells blast system the most according to claim 1 and 2, it is characterised in that flash distillation dryer (10) is in vertical The tubular structure arranged, 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 pipe of flash distillation dryer (10) Mouthful, it is arranged above that described feed unit is positioned at the second blower fan (60) air outlet.
Magnesium stearate aidr bells blast system the most according to claim 3, 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 aidr bells blast system the most according to claim 4, 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 aidr bells blast system 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.
Magnesium stearate aidr bells blast system 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).
CN201620858766.8U 2016-08-09 2016-08-09 Magnesium stearate aidr bells blast system Expired - Fee Related CN205851125U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620858766.8U CN205851125U (en) 2016-08-09 2016-08-09 Magnesium stearate aidr bells blast system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620858766.8U CN205851125U (en) 2016-08-09 2016-08-09 Magnesium stearate aidr bells blast system

Publications (1)

Publication Number Publication Date
CN205851125U true CN205851125U (en) 2017-01-04

Family

ID=57657303

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620858766.8U Expired - Fee Related CN205851125U (en) 2016-08-09 2016-08-09 Magnesium stearate aidr bells blast system

Country Status (1)

Country Link
CN (1) CN205851125U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106766819A (en) * 2017-02-04 2017-05-31 河南佳尚农业科技发展有限公司 A kind of rosemary fat-soluble extract expansion drying system
CN107096653A (en) * 2017-06-19 2017-08-29 浦北县益广林工贸有限公司 A kind of cyclone separator of wood chip impurity elimination
CN109894286A (en) * 2019-02-21 2019-06-18 中国矿业大学 A kind of particulate mineral dry separation system based on solar energy and heat accumulation
CN114111223A (en) * 2021-11-23 2022-03-01 广州承兴生物科技有限公司 Particulate matter drying system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106766819A (en) * 2017-02-04 2017-05-31 河南佳尚农业科技发展有限公司 A kind of rosemary fat-soluble extract expansion drying system
CN107096653A (en) * 2017-06-19 2017-08-29 浦北县益广林工贸有限公司 A kind of cyclone separator of wood chip impurity elimination
CN109894286A (en) * 2019-02-21 2019-06-18 中国矿业大学 A kind of particulate mineral dry separation system based on solar energy and heat accumulation
CN109894286B (en) * 2019-02-21 2019-12-24 中国矿业大学 Particle mineral dry separation system based on solar energy and heat storage
CN114111223A (en) * 2021-11-23 2022-03-01 广州承兴生物科技有限公司 Particulate matter drying system

Similar Documents

Publication Publication Date Title
CN205851125U (en) Magnesium stearate aidr bells blast system
CN111317148B (en) Peanut full-flow production line and method
CN105849489A (en) Method and arrangement for drying particulate material and use of the method or of the arrangement
CN108224903A (en) Granule materials series classification screens pneumatic conveyer dryer
CN104406377A (en) Chemical fertilizer drying and screening machine
CN212035877U (en) Peanut processing assembly line
CN206173257U (en) Starch maize processes production system
CN206689051U (en) For sieving the tubular spiral vibration sieve of noble metal extraction material
CN105289818A (en) Waste material recovery environment-protection device special for architecture
CN104132523B (en) A kind of flash dryer
CN205851387U (en) Magnesium stearate pneumatic separation device
CN205570513U (en) Cellulose ether production is with wet system that smashes
CN207404379U (en) Ceramic pigment feed powder sieving conveying device
CN207641981U (en) A kind of workshop powder lot negative pressure absorption hierarchy system
US20170008033A1 (en) Rotating Suction Chamber Apparatus
JP2007075737A (en) Wood and bamboo sizing unit and wood and bamboo producing/sizing apparatus having the same
CN206056200U (en) Whirlwind flash drier
CN207894121U (en) Granule materials series classification screens pneumatic conveyer dryer
CN205995798U (en) A kind of raw grain winnower
CN215742371U (en) Be used for slight particle separation sieving mechanism
CN207357606U (en) A kind of sorting equipment of efficient bean-dregs feed pellet
CN113694624A (en) Be used for slight particle separation sieving mechanism
CN105499134B (en) A kind of automatic charging is classified blowing machine triumphantly
CN201704245U (en) Starch pneumatic conveying balancing system
CN203896795U (en) Secondary cleaning mechanism of combine harvester

Legal Events

Date Code Title Description
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: 20170104

Termination date: 20210809

CF01 Termination of patent right due to non-payment of annual fee