CN207785970U - Highspeedcentrifugingandsprayingdrier - Google Patents
Highspeedcentrifugingandsprayingdrier Download PDFInfo
- Publication number
- CN207785970U CN207785970U CN201721773372.3U CN201721773372U CN207785970U CN 207785970 U CN207785970 U CN 207785970U CN 201721773372 U CN201721773372 U CN 201721773372U CN 207785970 U CN207785970 U CN 207785970U
- Authority
- CN
- China
- Prior art keywords
- spray drying
- drying chamber
- cyclone separator
- bag filter
- rewinding
- 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
- 238000001694 spray drying Methods 0.000 claims abstract description 61
- 239000000463 material Substances 0.000 claims abstract description 25
- 239000012141 concentrate Substances 0.000 claims abstract description 14
- 239000002737 fuel gas Substances 0.000 claims abstract description 14
- 238000009690 centrifugal atomisation Methods 0.000 claims abstract description 8
- 230000008676 import Effects 0.000 claims description 8
- 239000000428 dust Substances 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 4
- 241000282326 Felis catus Species 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 3
- 239000000567 combustion gas Substances 0.000 claims description 3
- 210000002381 plasma Anatomy 0.000 abstract description 12
- 210000000601 blood cell Anatomy 0.000 abstract description 11
- 238000001035 drying Methods 0.000 abstract description 10
- 239000000843 powder Substances 0.000 abstract description 10
- 239000007787 solid Substances 0.000 abstract description 5
- 239000007921 spray Substances 0.000 description 4
- 230000037237 body shape Effects 0.000 description 2
- 238000000703 high-speed centrifugation Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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- Cyclones (AREA)
Abstract
The utility model discloses a kind of Highspeedcentrifugingandsprayingdriers, vibrator is installed on inclined-plane on the outside of the cone of the spray drying chamber lower end, the high speed centrifugal atomization device is installed on the air inlet of the spray drying chamber top, pressure fan, the imitative direct fuel gas hot-blast stove of McKesson formula and the hot air duct are erect located on a straight line, the spray drying chamber side is equipped with the cyclone separator, the discharge pipe gradient is consistent with the spray drying chamber lower end cone bevel angle, the cyclone separator side is equipped with the bag filter, the bag filter is internally provided with two material bags, connection setting side by side between the material bag, the bag filter input terminal, which is equipped with, concentrates rewinding wind turbine, the bag filter output end is equipped with the concentration rewinding cyclone separator.By the above-mentioned means, the utility model can be exclusively used in the drying process of blood cell, blood plasma, discharge in solid state powder state after blood cell, blood plasma dry materials.
Description
Technical field
The utility model is related to drying machine fields, more particularly to a kind of Highspeedcentrifugingandsprayingdrier.
Background technology
Spray dryer can spray into the material of solution state in spray drying tower, be in solid powder state after dry materials
Discharging, the pressure of feed pump, the size of flow, nozzle can also be adjusted by technological requirement, obtain required ratio being sized
The spheric granules of example, majority are used for the drying of biological pesticide, medicine, food microorganisms, but traditional spray dryer treatment fluid
It is not thorough enough when being dried when state material, have sticky the drying cylinder inner wall situations such as, and liquid material drying is in chalk object
It cannot unify quickly extraction screening separation after material, reduce powder material quality.
Utility model content
The utility model can be exclusively used in blood mainly solving the technical problems that provide a kind of Highspeedcentrifugingandsprayingdrier
The drying process of ball, blood plasma is discharged in solid state powder state after blood cell, blood plasma dry materials.
In order to solve the above technical problems, the technical solution that the utility model uses is：A kind of high speed centrifugation spray is provided
Mist drying machine, including spray drying chamber, high speed centrifugal atomization device, the direct fuel gas hot-blast stove of imitative McKesson formula, cyclone separator, cloth
Bag dust collector and rewinding cyclone separator, the spray drying chamber upper end is concentrated to be set as cylinder, under the spray drying chamber
It holds and is set as cone, vibrator, the spray drying chamber are installed on inclined-plane on the outside of the cone of the spray drying chamber lower end
Both ends offer air inlet and air outlet and inside or more and are connected to setting respectively, are installed on the air inlet of the spray drying chamber top
There is the high speed centrifugal atomization device, is also connected on the air inlet of the spray drying chamber top and imports hot wind tube body, the hot blast pipe
The connection of body one end imports the spray drying interior, and the hot wind tube body other end is connected into the imitative direct combustion gas of McKesson formula
In hot-blast stove, the imitative direct fuel gas hot-blast stove lower end of McKesson formula is connected with pressure fan, the pressure fan, the imitative McKesson
In on a straight line, the spray drying chamber side is equipped with the rotation for the direct fuel gas hot-blast stove of formula and hot wind tube body erection position
Wind separator, is connected with discharge pipe between the spray drying chamber and the cyclone separator, described discharge pipe one end is connected to
On the air outlet of the spray drying chamber bottom, the discharge pipe other end tilts upward export and is connected to the cyclone separator
Interior, the discharge pipe gradient is consistent with the spray drying chamber lower end cone bevel angle, the cyclone separator side
The bag filter is installed, is connected by connecting tube between the cyclone separator and the bag filter, the cloth
Bag dust collector is internally provided with two material bags, is connected to setting side by side between the material bag, the bag filter input terminal is equipped with
Concentrate rewinding wind turbine, the bag filter output end that the concentration rewinding cyclone separator is installed.
In one preferred embodiment of the utility model, the concentration rewinding cyclone separator and the bag filter it
Between air-introduced machine is installed, concentration rewinding cyclone separator end is equipped with Blowing stopper.
In one preferred embodiment of the utility model, the cyclone separator bottom end is equipped with double-layer pneumatic valve.
In one preferred embodiment of the utility model, the spray drying chamber top, stage casing cylinder and the cloth bag remove
Cat ladder frame is connected and installed between dirt device.
The utility model has the beneficial effects that：The utility model can be exclusively used in the drying process of blood cell, blood plasma, blood cell,
It discharges in solid state powder state after blood plasma dry materials, the utility model selects spray drying chamber according to the characteristics of blood cell, blood plasma
Top cylinder body lower cone body shape designs, and vibrator is arranged on spray drying chamber's bottom cone lateral wall dried
Exciting is handled in journey, avoids in adhesion to spray drying chamber interior, blood cell, blood plasma is allowed preferably to be dried, and bag-type dust
Device designs two material bag processing, and bag filter rear end is provided with and concentrates rewinding wind turbine and concentrate rewinding cyclone separator etc.
Powder screen is carried out from obtaining the powder material of more preferable quality.
Description of the drawings
It is required in being described below to embodiment in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
Attached drawing to be used is briefly described, it should be apparent that, the accompanying drawings in the following description is only some realities of the utility model
Example is applied, it for those of ordinary skill in the art, without creative efforts, can also be according to these attached drawings
Other attached drawings are obtained, wherein：
Fig. 1 is the structural schematic diagram of one preferred embodiment of the utility model Highspeedcentrifugingandsprayingdrier；
Fig. 2 is the vertical view of one preferred embodiment of the utility model Highspeedcentrifugingandsprayingdrier；
Fig. 3 is the process flow chart of one preferred embodiment of the utility model Highspeedcentrifugingandsprayingdrier；
The label of each component is as follows in attached drawing：1, spray drying chamber；2, high speed centrifugal atomization device；3, it is straight to imitate McKesson formula
Connect fuel gas hot-blast stove；4, cyclone separator；5, bag filter；6, rewinding cyclone separator is concentrated；7, vibrator； 8、
Hot wind tube body；9, pressure fan；10, discharge pipe；11, material bag；12, rewinding wind turbine is concentrated；13, air-introduced machine；14, Guan Feng
Machine；15, double-layer pneumatic valve.
Specific implementation mode
Below by the technical scheme in the utility model embodiment is clearly and completely described, it is clear that described
Embodiment is only a part of the embodiment of the utility model, instead of all the embodiments.Based on the implementation in the utility model
Example, all other embodiment obtained by those of ordinary skill in the art without making creative efforts belong to
The range of the utility model protection.
It please refers to Fig.1, Fig. 2 and Fig. 3, the utility model embodiment include：
A kind of Highspeedcentrifugingandsprayingdrier, including spray drying chamber 1, high speed centrifugal atomization device 2, imitative McKesson formula are direct
Fuel gas hot-blast stove 3, cyclone separator 4, bag filter 5 and concentration rewinding cyclone separator 6,1 upper end of the spray drying chamber
It is set as cylinder, 1 lower end of the spray drying chamber is set as cone, the outer skew back of 1 lower end cone of the spray drying chamber
Vibrator 7 is installed, 1 both ends of the spray drying chamber offer air inlet and air outlet respectively and internal upper and lower be connected to sets on face
Set, the high speed centrifugal atomization device 2 be installed on 1 top air inlet of the spray drying chamber, 1 top of the spray drying chamber into
It is also connected on air port and imports hot wind tube body 8,8 one end of hot wind tube body connection imports in the spray drying chamber 1, the hot wind
8 other end of tube body connects in the direct fuel gas hot-blast stove of the imitative McKesson formula 3, the imitative direct fuel gas hot-blast stove of McKesson formula
3 lower ends are connected with pressure fan 9, and the pressure fan 9, the imitative direct fuel gas hot-blast stove 3 of McKesson formula and the hot wind tube body 8 are perpendicular
Vertical located on a straight line, 1 side of the spray drying chamber is equipped with the cyclone separator 4, the spray drying chamber 1 with it is described
Discharge pipe 10 is connected between cyclone separator 4,10 one end of the discharge pipe is connected to 1 bottom air outlet of the spray drying chamber
On, 10 other end of the discharge pipe tilts upward export and is connected in the cyclone separator 4,10 gradient of the discharge pipe with
1 lower end cone bevel angle of the spray drying chamber is consistent, and 4 side of the cyclone separator is equipped with the bag filter
5, it is connected by connecting tube between the cyclone separator 4 and the bag filter 5, the bag filter 5 is internally provided with
Two material bags 11, connection setting side by side between the material bag 11,5 input terminal of the bag filter, which is equipped with, concentrates rewinding wind turbine
12,5 output end of the bag filter is equipped with the concentration rewinding cyclone separator 6.
In addition, air-introduced machine 13 is installed between the concentration rewinding cyclone separator 6 and the bag filter 5, it is described
Concentrate 6 end of rewinding cyclone separator that Blowing stopper 14 is installed.
In addition, 4 bottom end of the cyclone separator is equipped with double-layer pneumatic valve 15.
In addition, being connected and installed with cat ladder between 1 top of the spray drying chamber, stage casing cylinder and the bag filter 5
Frame.
The operation principle of the utility model is that 1 upper end of spray drying chamber is set as cylinder, the setting of 1 lower end of spray drying chamber
For cone, vibrator 7 is installed on inclined-plane on the outside of 1 lower end cone of spray drying chamber, 1 both ends of spray drying chamber open up respectively
There are air inlet and air outlet and inside or more to be connected to setting, high speed centrifugation atomization is installed on 1 top air inlet of spray drying chamber
Device 2.
It is also connected on 1 top air inlet of spray drying chamber and imports hot wind tube body 8, the connection of 8 one end of hot wind tube body imports spraying
In hothouse 1,8 other end of hot wind tube body connects in the direct fuel gas hot-blast stove of imitative McKesson formula 3, imitates the direct combustion gas of McKesson formula
3 lower end of hot-blast stove is connected with pressure fan 9, and pressure fan 9, the direct fuel gas hot-blast stove 3 of imitative McKesson formula and the setting of hot wind tube body 8 are located at
On one straight line, 1 side of spray drying chamber is equipped with cyclone separator 4, and 4 bottom end of cyclone separator is equipped with double-layer pneumatic valve
15, discharge pipe 10 is connected between spray drying chamber 1 and cyclone separator 4,10 one end of discharge pipe is connected to 1 bottom of spray drying chamber
On portion's air outlet, 10 other end of discharge pipe tilts upward export and is connected in cyclone separator 4,10 gradient of discharge pipe and spraying
1 lower end cone bevel angle of hothouse is consistent, and 4 side of cyclone separator is equipped with bag filter 5, and spray drying chamber 1 is pushed up
It is connected and installed with cat ladder frame between end, stage casing cylinder and bag filter 5, is passed through between cyclone separator 4 and bag filter 5
Connecting tube connects, and bag filter 5 is internally provided with two material bags 11, is connected to setting side by side between material bag 11, bag filter 5 is defeated
Enter end and concentration rewinding wind turbine 12 is installed, concentrates 12 input terminal of rewinding wind turbine to be equipped with and concentrate rewinding cyclone separator 6, concentrate and receive
Air-introduced machine 13 is installed between material cyclone separator 6 and bag filter 5, concentrates the 6 end installation of rewinding cyclone separator related
Wind turbine 14, the utility model can be exclusively used in the drying process of blood cell, blood plasma, be in solid state powder after blood cell, blood plasma dry materials
State discharges, and the utility model selects 1 top cylinder body lower cone body shape of spray drying chamber to set according to the characteristics of blood cell, blood plasma
Meter, and the exciting processing in the drying process of vibrator 7 is set on 1 bottom cone lateral wall of spray drying chamber, avoid adhesion
Onto 1 inside of spray drying chamber, blood cell, blood plasma is allowed preferably to be dried, and bag filter 5 designs at two material bags 11
Reason, and 5 rear end of bag filter be provided with concentrate rewinding wind turbine 12 and concentrate the equal progress Powder screen of rewinding cyclone separator 6 from
Obtain the powder material of more preferable quality.
The above description is only the embodiments of the present invention, and it does not limit the scope of the patent of the present invention, every
Using equivalent structure or equivalent flow shift made by the utility model description, it is applied directly or indirectly in other phases
The technical field of pass, is equally included in the patent within the scope of the utility model.
Claims (4)
1. a kind of Highspeedcentrifugingandsprayingdrier, including spray drying chamber, high speed centrifugal atomization device, the direct combustion gas of imitative McKesson formula
Hot-blast stove, cyclone separator, bag filter and concentration rewinding cyclone separator, which is characterized in that in the spray drying chamber
End is set as cylinder, and the spray drying chamber lower end is set as cone, the outer skew back of spray drying chamber lower end cone
Vibrator is installed, the spray drying chamber both ends offer air inlet and air outlet respectively and internal upper and lower be connected to sets on face
It sets, the high speed centrifugal atomization device, the spray drying chamber top air inlet is installed on the air inlet of the spray drying chamber top
It is also connected on mouthful and imports hot wind tube body, the connection of hot wind tube body one end imports the spray drying interior, the hot wind tube body
The other end connects in the imitative direct fuel gas hot-blast stove of McKesson formula, and the imitative direct fuel gas hot-blast stove lower end of McKesson formula connects
It is connected to pressure fan, the pressure fan, the imitative direct fuel gas hot-blast stove of McKesson formula and hot wind tube body erection position are in always
On line, the spray drying chamber side is equipped with the cyclone separator, the spray drying chamber and the cyclone separator it
Between be connected with discharge pipe, described discharge pipe one end is connected on the air outlet of the spray drying chamber bottom, and the discharge pipe is another
End tilts upward export and is connected in the cyclone separator, the discharge pipe gradient and spray drying chamber lower end circular cone
Body bevel angle is consistent, and the cyclone separator side is equipped with the bag filter, the cyclone separator and the cloth
It is connected by connecting tube between bag dust collector, the bag filter is internally provided with two material bags, connects side by side between the material bag
Logical setting, the bag filter input terminal, which is equipped with, concentrates rewinding wind turbine, and the bag filter output end is equipped with described
Concentrate rewinding cyclone separator.
2. Highspeedcentrifugingandsprayingdrier according to claim 1, which is characterized in that the concentration rewinding cyclone separator
Air-introduced machine is installed between the bag filter, concentration rewinding cyclone separator end is equipped with Blowing stopper.
3. Highspeedcentrifugingandsprayingdrier according to claim 1, which is characterized in that the cyclone separator bottom end peace
Equipped with double-layer pneumatic valve.
4. Highspeedcentrifugingandsprayingdrier according to claim 1, which is characterized in that the spray drying chamber top, in
It is connected and installed with cat ladder frame between section cylinder and the bag filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721773372.3U CN207785970U (en) | 2017-12-19 | 2017-12-19 | Highspeedcentrifugingandsprayingdrier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721773372.3U CN207785970U (en) | 2017-12-19 | 2017-12-19 | Highspeedcentrifugingandsprayingdrier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207785970U true CN207785970U (en) | 2018-08-31 |
Family
ID=63280928
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721773372.3U Expired - Fee Related CN207785970U (en) | 2017-12-19 | 2017-12-19 | Highspeedcentrifugingandsprayingdrier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207785970U (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
- 2017-12-19 CN CN201721773372.3U patent/CN207785970U/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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180831 |