CN206535218U - A kind of Highspeedcentrifugingandsprayingdrier - Google Patents
A kind of Highspeedcentrifugingandsprayingdrier Download PDFInfo
- Publication number
- CN206535218U CN206535218U CN201720259300.0U CN201720259300U CN206535218U CN 206535218 U CN206535218 U CN 206535218U CN 201720259300 U CN201720259300 U CN 201720259300U CN 206535218 U CN206535218 U CN 206535218U
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- CN
- China
- Prior art keywords
- air
- spray drying
- centrifugal spray
- highspeedcentrifugingandsprayingdrier
- centrifugal
- 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
- 238000001035 drying Methods 0.000 claims abstract description 33
- 238000010438 heat treatment Methods 0.000 claims abstract description 32
- 238000001694 spray drying Methods 0.000 claims abstract description 25
- 238000005507 spraying Methods 0.000 claims description 19
- 239000000463 material Substances 0.000 claims description 17
- 238000007664 blowing Methods 0.000 claims description 16
- 238000005485 electric heating Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 230000006978 adaptation Effects 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 4
- 239000011344 liquid material Substances 0.000 abstract description 2
- 239000003814 drug Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 230000005611 electricity Effects 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000000703 high-speed centrifugation Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
Abstract
The utility model provides a kind of Highspeedcentrifugingandsprayingdrier, which solve existing drying machine drying efficiency low, converted products quality is unstable, product adhesion, equipment inner wall is accumulated in be difficult to discharge and remove, equipment occupation space is big, operation, maintenance is not easy, air mode of heating is single, it is unable to the technical problems such as flexible adaptation production requirement, it is provided with centrifugal spray drying device, air filter, air heating apparatus, feeding device, cyclone separator, sack cleaner and blower fan, air cleaner is connected with air heating apparatus, the intake stack connection of air heating apparatus and centrifugal spray drying device, centrifugal spray drying device and cyclone separator, cyclone separator is connected with sack cleaner, sack cleaner is connected with blower fan, feeding device is connected with centrifugal spray drying device.The utility model can be widely applied to medicine, drying for the liquid material of chemical field and process.
Description
Technical field
The utility model is related to a kind of drying machine, more particularly to a kind of Highspeedcentrifugingandsprayingdrier.
Background technology
Existing drying machine drying efficiency is low, and converted products quality is unstable, product adhesion, accumulate in equipment inner wall be difficult row
Go out and remove, equipment occupation space is big, operation, maintenance are not easy, and air mode of heating is single, it is impossible to which flexible adaptation production is needed
Ask.
The content of the invention
The utility model is low for existing drying machine drying efficiency, and converted products quality is unstable, product adhesion, accumulates in
Equipment inner wall is difficult to discharge and removed, and equipment occupation space is big, and operation, maintenance are not easy, and air mode of heating is single, it is impossible to spirit
The living technical problem for adapting to production requirement is high there is provided a kind of drying efficiency, converted products stay in grade, product adhesion, accumulates in
Equipment inner wall is easy to discharge and removed, and equipment occupation space is small, and operation, maintenance are easy, and air mode of heating is various, can flexibly fit
Answer the Highspeedcentrifugingandsprayingdrier of production requirement.
Therefore, the utility model, which is provided with, includes centrifugal spray drying device, air cleaner, air heating apparatus, feed
Device, cyclone separator, sack cleaner and blower fan, air cleaner are connected with air heating apparatus, air heating apparatus with
The intake stack connection of centrifugal spray drying device, centrifugal spray drying device is connected with cyclone separator, cyclone separator and
Sack cleaner is connected, and sack cleaner is connected with blower fan, and feeding device is connected with centrifugal spray drying device.
Preferably, air heating apparatus is provided with heating compartment, and heating compartment is interior to be added provided with steam heater block and electricity simultaneously
Thermal part.
Preferably, centrifugal spray drying device is provided with drying tower, and drying tower inner chamber is provided with centrifugal spraying disk, centrifugal spraying disk
With centrifugal spraying disk motor connection, drying tower top is provided with intake stack, and the circular cone lateral surface of drying tower bottom shakes provided with pneumatic
Dynamic hammer.
Preferably, cyclone separator lower end connection material storing box, material storing box lower end is provided with Blowing stopper, Blowing stopper and Blowing stopper electricity
Machine is connected, and the material storing box lower end outside conical surface is hammered into shape provided with pneumatic vibration.
Preferably, two material-falling hoppers are installed in sack cleaner lower end.
Preferably, feeding device includes agitator and screw pump, and agitator is connected by valve with screw pump arrival end, spiral shell
Bar pump discharge end is connected with the centrifugal spraying disk of drying tower inner chamber, and screw pump is connected with screw drive motor.
The utility model beneficial effect is, due to provided with including centrifugal spray drying device, air cleaner, air heating
Device, feeding device, cyclone separator, sack cleaner and blower fan, air cleaner are connected with air heating apparatus, and air adds
The intake stack connection of thermal and centrifugal spray drying device, centrifugal spray drying device is connected with cyclone separator, whirlwind
Separator is connected with sack cleaner, and sack cleaner is connected with blower fan, and feeding device is connected with centrifugal spray drying device.It is empty
Gas heater is provided with heating compartment, heating compartment simultaneously provided with steam heater block and electric heating element.Air heating side
Formula is various, the Highspeedcentrifugingandsprayingdrier of energy flexible adaptation production requirement.Centrifugal spray drying device is provided with drying tower, dries
Tower inner chamber is provided with the top of centrifugal spraying disk, centrifugal spraying disk and centrifugal spraying disk motor connection, drying tower and is provided with intake stack, does
The circular cone lateral surface of dry tower bottom is hammered into shape provided with pneumatic vibration.Drying efficiency is high, converted products stay in grade, product adhesion, accumulation
It is easy to discharge and removes in equipment inner wall.Cyclone separator lower end connects material storing box, and material storing box lower end is provided with Blowing stopper, Blowing stopper
With Blowing stopper motor connection, the material storing box lower end outside conical surface is hammered into shape provided with pneumatic vibration.Material can interval, be automatically brought into operation, be not required to people
Work processing, product adhesion, accumulates in equipment inner wall and is easy to discharge and removes.Sack cleaner lower end is installed by two material-falling hoppers.Equipment
Occupy little space, operate, overhaul easily.Feeding device includes agitator and screw pump, and agitator is pumped into by valve with screw rod
Mouth end connection, the screw pump port of export is connected with the centrifugal spraying disk of drying tower inner chamber, and screw pump is connected with screw drive motor.For
Material is stable, uniform, it is ensured that product processing quality.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment.
Symbol description in figure：
1. air；2. filter motor；3. air cleaner；4. electric heating element；5. steam heater block；6. heater box
Body；7. centrifugal spray drying device；8. centrifugal spraying disk；9. centrifugal spray coil motor；10. intake stack；11. screw pump；12.
Screw drive motor；13. valve；14. agitator；15. feeding device；16. pneumatic vibration is hammered into shape；17. cyclone separator；18. storage
Hopper；19. Blowing stopper；20. Blowing stopper motor；21. sack cleaner；22. material-falling hopper；23. blower fan；24. blower motor；25.
Drying tower；26. air heating apparatus.
Embodiment
The utility model is described further with reference to embodiment.
As shown in figure 1, being a kind of embodiment of the present utility model, provided with including centrifugal spray drying device 7, air filtration
Device 3, air heating apparatus 26, feeding device 15, cyclone separator 17, sack cleaner 21 and blower fan 23, air cleaner 3 with
Air heating apparatus 26 is connected, and air heating apparatus 26 is connected with the intake stack 10 of centrifugal spray drying device 7, centrifugal spray
Drying device 7 is connected with cyclone separator 17, and cyclone separator 17 is connected with sack cleaner 21, sack cleaner 21 and blower fan
23 connections, feeding device 15 is connected with centrifugal spray drying device 7.Air heating apparatus 26 is provided with heating compartment 6, heating compartment
Simultaneously provided with steam heater block 5 and electric heating element 4 in 6.Air mode of heating is various, can flexible adaptation production requirement.From
Heart spray-drying installation 7 is provided with drying tower 25, and the inner chamber of drying tower 25 is provided with centrifugal spraying disk 8, centrifugal spraying disk 8 and centrifugal spray
Coil motor 9 is connected, and the top of drying tower 25 is provided with intake stack 10, and the circular cone lateral surface of the bottom of drying tower 25 is hammered into shape provided with pneumatic vibration
16.Drying efficiency is high, converted products stay in grade, product adhesion, accumulates in equipment inner wall and is easy to discharge and removes.Cyclonic separation
The lower end of device 17 connects material storing box 18, and the lower end of material storing box 18 is provided with Blowing stopper 19, and Blowing stopper 19 is connected with Blowing stopper motor 20, storing
The lower end outside conical surface of case 18 is provided with pneumatic vibration hammer 16.Material can interval, be automatically brought into operation, be not required to artificial treatment, product adhesion, accumulate
It is easy to discharge and removes in equipment inner wall.The lower end of sack cleaner 21 is installed by two material-falling hoppers 22.Equipment occupation space is small, behaviour
Make, overhaul easy.Feeding device 15 includes agitator 14 and screw pump 11, and agitator 14 passes through valve 13 and the entrance of screw pump 11
End connection, the port of export of screw pump 11 is connected with the centrifugal spraying disk 8 of the inner chamber of drying tower 25, screw pump 11 and screw drive motor 12
Connection.Feed is stable, uniform, it is ensured that product processing quality.
Its workflow is：Air 1 enters heating compartment 6 under the driving of filter motor 2 by air cleaner 3,
Heated air enters the inner chamber of drying tower 25 by intake stack 10, and the liquid material uniformly provided by feeding device 15 enters
The centrifugal spraying disk 8 of the inner chamber of drying tower 25, rotates the high speed centrifugation produced by the high speed of centrifugal spraying disk 8 and acts on, liquids
Material throws away to form vaporific from centrifugal spraying disk 8, and the effect through hot-air forms powdery or granular solids, under drying tower 25
End discharge, is separated, most of solid material falls into material storing box 18 through cyclone separator 17, under the driving of Blowing stopper motor 20, Gu
Body material is regularly discharged by Blowing stopper 19, and when the air for being mixed with a small amount of granular material enters sack cleaner 21, granular material falls
Enter material-falling hopper 22 to reclaim, air is then strongly discharged under the drive of blower motor 24 by blower fan 23.
Only as described above, only specific embodiment of the utility model, when the utility model can not be limited with this
The scope of implementation, therefore the displacement of its equivalent assemblies, or the equivalent variations made according to the utility model scope of patent protection and modification,
It all should still belong to the category that the utility model claims are covered.
Claims (6)
1. a kind of Highspeedcentrifugingandsprayingdrier, including centrifugal spray drying device, air cleaner, air heating apparatus, confession
Expect device, cyclone separator, sack cleaner and blower fan, it is characterized in that：The air cleaner is connected with air heating apparatus,
The intake stack connection of the air heating apparatus and centrifugal spray drying device, the centrifugal spray drying device and whirlwind point
From device connection, the cyclone separator is connected with sack cleaner, and the sack cleaner is connected with blower fan, the feeding device
It is connected with centrifugal spray drying device.
2. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that：The air heating apparatus, which is provided with, to be added
Simultaneously provided with steam heater block and electric heating element in hot tank body, the heating compartment.
3. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that：The centrifugal spray drying device is set
There is drying tower, the drying tower inner chamber is provided with centrifugal spraying disk, the centrifugal spraying disk and centrifugal spraying disk motor connection, described
Intake stack is provided with the top of drying tower, the circular cone lateral surface of the drying tower bottom is hammered into shape provided with pneumatic vibration.
4. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that：The cyclone separator lower end connection
Material storing box, the material storing box lower end is provided with Blowing stopper, the Blowing stopper and Blowing stopper motor connection, the material storing box lower end outside
The conical surface is hammered into shape provided with pneumatic vibration.
5. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that：Install the sack cleaner lower end
Two material-falling hoppers.
6. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that：The feeding device includes agitator
And screw pump, the agitator is connected by valve with screw pump arrival end, the screw pump port of export and drying tower inner chamber
Centrifugal spraying disk is connected, and the screw pump is connected with screw drive motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720259300.0U CN206535218U (en) | 2017-03-16 | 2017-03-16 | A kind of Highspeedcentrifugingandsprayingdrier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720259300.0U CN206535218U (en) | 2017-03-16 | 2017-03-16 | A kind of Highspeedcentrifugingandsprayingdrier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206535218U true CN206535218U (en) | 2017-10-03 |
Family
ID=59942636
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720259300.0U Expired - Fee Related CN206535218U (en) | 2017-03-16 | 2017-03-16 | A kind of Highspeedcentrifugingandsprayingdrier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206535218U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107823900A (en) * | 2017-12-19 | 2018-03-23 | 无锡市尚德干燥设备有限公司 | Highspeedcentrifugingandsprayingdrier |
-
2017
- 2017-03-16 CN CN201720259300.0U patent/CN206535218U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107823900A (en) * | 2017-12-19 | 2018-03-23 | 无锡市尚德干燥设备有限公司 | Highspeedcentrifugingandsprayingdrier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171003 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |