CN107823900A - Highspeedcentrifugingandsprayingdrier - Google Patents
Highspeedcentrifugingandsprayingdrier Download PDFInfo
- Publication number
- CN107823900A CN107823900A CN201711369746.XA CN201711369746A CN107823900A CN 107823900 A CN107823900 A CN 107823900A CN 201711369746 A CN201711369746 A CN 201711369746A CN 107823900 A CN107823900 A CN 107823900A
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- China
- Prior art keywords
- spray drying
- drying chamber
- cyclone separator
- sack cleaner
- hot
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- 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.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
- B01D1/18—Evaporating by spraying to obtain dry solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Cyclones (AREA)
Abstract
The invention discloses a kind of Highspeedcentrifugingandsprayingdrier, 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 provided 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 provided with the sack cleaner, two pockets are provided with inside the sack cleaner, connection is set side by side between the pocket, the sack cleaner input, which is provided with, concentrates rewinding blower fan, the sack cleaner output end is provided with the concentration rewinding cyclone separator.By the above-mentioned means, the present invention can be exclusively used in the drying process of blood cell, blood plasma, discharged after blood cell, blood plasma dry materials in solid state powder state.
Description
Technical field
The present invention relates to drying machine field, 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, by technological requirement can also adjust the pressure of feed pump, flow, shower nozzle size, 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 during drying process during state material, have sticky the drying inwall situations such as, and it is in chalk thing that liquid material, which is dried,
It can not unify quickly to extract screening separation out after material, reduce powder material quality.
The content of the invention
The present invention solves the technical problem of a kind of Highspeedcentrifugingandsprayingdrier is provided, can be exclusively used in blood cell,
The drying process of blood plasma, discharged in solid state powder state after blood cell, blood plasma dry materials.
In order to solve the above technical problems, one aspect of the present invention is：It is dry to provide a kind of high speed centrifugation spraying
Dry 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 remove
Dirt device and concentration rewinding cyclone separator, the spray drying chamber upper end are arranged to cylinder, and the spray drying chamber lower end is set
It is set to cone, vibrator, the spray drying chamber both ends is installed on inclined-plane on the outside of the cone of the spray drying chamber lower end
Air inlet is offered respectively and connects setting up and down with air outlet and inside, is installed on the air inlet of the spray drying chamber top
High speed centrifugal atomization device is stated, is also connected with importing hot blast body, the hot blast body one on the air inlet of the spray drying chamber top
End connection imports the spray drying interior, and the hot blast body other end is connected into the imitative direct gas hot-air of McKesson formula
In stove, the imitative direct fuel gas hot-blast stove lower end of McKesson formula is connected with pressure fan, and the pressure fan, the imitative McKesson formula are straight
Connect fuel gas hot-blast stove and hot air duct setting is located on a straight line, the spray drying chamber side is provided with the whirlwind point
From device, discharge pipe is connected between the spray drying chamber and the cyclone separator, described discharge pipe one end is connected to described
On the air outlet of spray drying chamber bottom, the discharge pipe other end tilts upward export and is connected in the cyclone separator, institute
It is consistent with the spray drying chamber lower end cone bevel angle to state discharge pipe gradient, the cyclone separator side is provided with
The sack cleaner, connected between the cyclone separator and the sack cleaner by connecting tube, the bag-type dust
Two pockets are provided with inside device, connects and sets side by side between the pocket, the sack cleaner input is provided with concentration and received
Expect blower fan, the sack cleaner output end is provided with the concentration rewinding cyclone separator.
In a preferred embodiment of the present invention, pacify between the concentration rewinding cyclone separator and the sack cleaner
Equipped with air-introduced machine, the concentration rewinding cyclone separator end is provided with Blowing stopper.
In a preferred embodiment of the present invention, the cyclone separator bottom end is provided with double-layer pneumatic valve.
In a preferred embodiment of the present invention, the spray drying chamber top, stage casing cylinder and the sack cleaner
Between be connected and installed with cat ladder frame.
The beneficial effects of the invention are as follows：The present invention can be exclusively used in the drying process of blood cell, blood plasma, blood cell, blood plasma material
Discharged after drying in solid state powder state, the present invention is selected under spray drying chamber's top cylinder body according to the characteristics of blood cell, blood plasma
Portion's cone shape design, and set vibrator in the drying process at exciting on spray drying chamber's bottom cone lateral wall
Reason, avoids sticky in spray drying chamber interior, allowing the more preferable drying process of blood cell, blood plasma, and sack cleaner designs two
Pocket processing, and sack cleaner rear end is provided with and concentrates rewinding blower fan and concentrate rewinding cyclone separator etc. to carry out Powder screen
From obtaining the powder material of more preferable quality.
Brief description of the drawings
Technical scheme in order to illustrate the embodiments of the present invention more clearly, make required in being described below to embodiment
Accompanying drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the present invention, for
For those of ordinary skill in the art, on the premise of not paying creative work, it can also be obtained according to these accompanying drawings other
Accompanying drawing, wherein：
Fig. 1 is the structural representation of the preferred embodiment of Highspeedcentrifugingandsprayingdrier one of the present invention；
Fig. 2 is the top view of the preferred embodiment of Highspeedcentrifugingandsprayingdrier one of the present invention；
Fig. 3 is the process chart of the preferred embodiment of Highspeedcentrifugingandsprayingdrier one of the present invention；
The mark of each part is as follows in accompanying drawing：1st, spray drying chamber；2nd, high speed centrifugal atomization device；3rd, McKesson formula is imitated directly to fire
Gas and hot air stove；4th, cyclone separator；5th, sack cleaner；6th, rewinding cyclone separator is concentrated；7th, vibrator；8th, hot blast
Body；9th, pressure fan；10th, discharge pipe；11st, pocket；12nd, rewinding blower fan is concentrated；13rd, air-introduced machine；14th, Blowing stopper；
15th, double-layer pneumatic valve.
Embodiment
The technical scheme in the embodiment of the present invention will be clearly and completely described below, it is clear that described implementation
Example is only the part of the embodiment of the present invention, rather than whole embodiments.It is common based on the embodiment in the present invention, this area
All other embodiment that technical staff is obtained under the premise of creative work is not made, belong to the model that the present invention protects
Enclose.
Fig. 1, Fig. 2 and Fig. 3 are referred to, the embodiment of the present invention includes：
A kind of Highspeedcentrifugingandsprayingdrier, including spray drying chamber 1, high speed centrifugal atomization device 2, the direct combustion gas of imitative McKesson formula
Hot-blast stove 3, cyclone separator 4, sack cleaner 5 and concentration rewinding cyclone separator 6, the upper end of spray drying chamber 1 is set
For cylinder, the lower end of spray drying chamber 1 is arranged to cone, on the outside of the lower end cone of spray drying chamber 1 on inclined-plane
Vibrator 7 is installed, the both ends of spray drying chamber 1 offer air inlet and connect setting up and down with air outlet and inside respectively,
The high speed centrifugal atomization device 2, the top air intake of spray drying chamber 1 are installed on the top air inlet of spray drying chamber 1
It is also connected with importing hot blast body 8 on mouthful, the one end of hot blast body 8 connection is imported in the spray drying chamber 1, the warm-air pipe
The other end of body 8 is connected in the direct fuel gas hot-blast stove 3 of imitative McKesson formula, the imitative direct fuel gas hot-blast stove 3 of McKesson formula
Lower end is connected with pressure fan 9, and the pressure fan 9, the direct fuel gas hot-blast stove 3 of the imitative McKesson formula and the hot air duct 8 are perpendicular
Vertical located on a straight line, the side of spray drying chamber 1 is provided with the cyclone separator 4, the spray drying chamber 1 with it is described
Discharge pipe 10 is connected between cyclone separator 4, described one end of discharge pipe 10 is connected to the bottom air outlet of spray drying chamber 1
On, the other end of discharge pipe 10 tilts upward export and is connected in the cyclone separator 4, the gradient of discharge pipe 10 with
The lower end cone bevel angle of spray drying chamber 1 is consistent, and the side of cyclone separator 4 is provided with the sack cleaner
5, connected between the cyclone separator 4 and the sack cleaner 5 by connecting tube, the inside of sack cleaner 5 is provided with
Two pockets 11, connection is set side by side between the pocket 11, and the input of sack cleaner 5, which is provided with, concentrates rewinding blower fan
12, the output end of sack cleaner 5 is provided with the concentration rewinding cyclone separator 6.
In addition, air-introduced machine 13 is installed between the concentration rewinding cyclone separator 6 and the sack cleaner 5, it is described
Concentrate the end of rewinding cyclone separator 6 that Blowing stopper 14 is installed.
In addition, the bottom end of cyclone separator 4 is provided with double-layer pneumatic valve 15.
In addition, it is connected and installed with cat ladder between the top of spray drying chamber 1, stage casing cylinder and the sack cleaner 5
Frame.
The operation principle of the present invention is arranged to cylinder for the upper end of spray drying chamber 1, and the lower end of spray drying chamber 1 is arranged to round
Cone, is provided with vibrator 7 on the outside of the lower end cone of spray drying chamber 1 on inclined-plane, the both ends of spray drying chamber 1 offer respectively into
Air port connects setting up and down with air outlet and inside, and high speed centrifugal atomization device 2 is provided with the top air inlet of spray drying chamber 1.
It is also connected with importing hot blast body 8 on the top air inlet of spray drying chamber 1, the connection of the one end of hot blast body 8 imports spraying
In hothouse 1, the other end of hot blast body 8 is connected in the direct fuel gas hot-blast stove 3 of imitative McKesson formula, imitates the direct combustion gas of McKesson formula
The lower end of hot-blast stove 3 is connected with pressure fan 9, and pressure fan 9, the direct fuel gas hot-blast stove 3 of imitative McKesson formula and hot air duct 8 are erect and be located at
On one straight line, the side of spray drying chamber 1 is provided with cyclone separator 4, and the bottom end of cyclone separator 4 is provided with double-layer pneumatic valve
15, discharge pipe 10 is connected between spray drying chamber 1 and cyclone separator 4, the one end of discharge pipe 10 is connected to the bottom of spray drying chamber 1
On portion's air outlet, the other end of discharge pipe 10 tilts upward export and is connected in cyclone separator 4, the gradient of discharge pipe 10 and spraying
The lower end cone bevel angle of hothouse 1 is consistent, and the side of cyclone separator 4 is provided with sack cleaner 5, and spray drying chamber 1 is pushed up
Cat ladder frame is connected and installed between end, stage casing cylinder and sack cleaner 5, is passed through between cyclone separator 4 and sack cleaner 5
Connecting tube connects, and the inside of sack cleaner 5 is provided with two pockets 11, connects and sets side by side between pocket 11, sack cleaner 5 is defeated
Enter end and concentration rewinding blower fan 12 is installed, concentrate the input of rewinding blower fan 12 to be provided with and concentrate rewinding cyclone separator 6, concentrate and receive
Air-introduced machine 13 is installed between material cyclone separator 6 and sack cleaner 5, concentrates the end installation of rewinding cyclone separator 6 relevant
Blower fan 14, the present invention can be exclusively used in the drying process of blood cell, blood plasma, be in solid state powder state after blood cell, blood plasma dry materials
Discharging, the present invention select the design of the top cylinder body lower cone body shape of spray drying chamber 1 according to the characteristics of blood cell, blood plasma, and
Vibrator 7 is set on the bottom cone lateral wall of spray drying chamber 1, and exciting is handled in the drying process, is avoided sticky dry to spraying
On the dry inside of room 1, the more preferable drying process of blood cell, blood plasma is allowed, and sack cleaner 5 designs two pockets 11 and handled, and cloth
The rear end of bag dust collector 5, which is provided with, concentrates rewinding blower fan 12 and concentrates the grade progress Powder screen of rewinding cyclone separator 6 more preferable from obtaining
The powder material of quality.
Embodiments of the invention are the foregoing is only, are not intended to limit the scope of the invention, it is every to utilize this hair
The equivalent structure or equivalent flow conversion that bright description is made, or directly or indirectly it is used in other related technology necks
Domain, it is included within the scope of the present invention.
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, sack cleaner and concentration rewinding cyclone separator, it is characterised in that in the spray drying chamber
End is arranged to cylinder, and the spray drying chamber lower end is arranged to 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 set with air outlet and internal connect up and down respectively on face
Put, the high speed centrifugal atomization device, spray drying chamber top air intake are installed on the air inlet of the spray drying chamber top
It is also connected with importing hot blast body on mouthful, hot blast body one end connection importing spray drying is indoor, the hot blast body
The other end is connected 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
Pressure fan is connected to, the pressure fan, the imitative direct fuel gas hot-blast stove of McKesson formula and the hot air duct are erect positioned at always
On line, the spray drying chamber side is provided 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 provided with the sack cleaner, the cyclone separator and the cloth
Connected between bag dust collector by connecting tube, be provided with two pockets inside the sack cleaner, connect side by side between the pocket
Logical to set, the sack cleaner input, which is provided with, concentrates rewinding blower fan, and the sack cleaner output end is provided with described
Concentrate rewinding cyclone separator.
2. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that the concentration rewinding cyclone separator
Air-introduced machine is installed between the sack cleaner, the concentration rewinding cyclone separator end is provided with Blowing stopper.
3. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that the cyclone separator bottom end peace
Equipped with double-layer pneumatic valve.
4. Highspeedcentrifugingandsprayingdrier according to claim 1, it is characterised in that the spray drying chamber top, in
Cat ladder frame is connected and installed between section cylinder and the sack cleaner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711369746.XA CN107823900A (en) | 2017-12-19 | 2017-12-19 | Highspeedcentrifugingandsprayingdrier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711369746.XA CN107823900A (en) | 2017-12-19 | 2017-12-19 | Highspeedcentrifugingandsprayingdrier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107823900A true CN107823900A (en) | 2018-03-23 |
Family
ID=61645316
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711369746.XA Withdrawn CN107823900A (en) | 2017-12-19 | 2017-12-19 | Highspeedcentrifugingandsprayingdrier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107823900A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201772710U (en) * | 2010-08-11 | 2011-03-23 | 焦作健康元生物制品有限公司 | Fungus dreg spray drying system |
| CN204601643U (en) * | 2015-03-16 | 2015-09-02 | 泰兴市东圣食品科技有限公司 | A kind of spray-drying installation |
| CN205198995U (en) * | 2015-12-11 | 2016-05-04 | 天津环湖农业科技有限公司 | A spray drier for solid drink production |
| CN205953545U (en) * | 2016-08-30 | 2017-02-15 | 青川天隆新材料开发有限责任公司 | A high -speed centrifugal spray drying system for nano meter aluminium production |
| CN206535218U (en) * | 2017-03-16 | 2017-10-03 | 乳山韩威生物科技有限公司 | A kind of Highspeedcentrifugingandsprayingdrier |
| CN207785970U (en) * | 2017-12-19 | 2018-08-31 | 无锡市尚德干燥设备有限公司 | Highspeedcentrifugingandsprayingdrier |
-
2017
- 2017-12-19 CN CN201711369746.XA patent/CN107823900A/en not_active Withdrawn
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201772710U (en) * | 2010-08-11 | 2011-03-23 | 焦作健康元生物制品有限公司 | Fungus dreg spray drying system |
| CN204601643U (en) * | 2015-03-16 | 2015-09-02 | 泰兴市东圣食品科技有限公司 | A kind of spray-drying installation |
| CN205198995U (en) * | 2015-12-11 | 2016-05-04 | 天津环湖农业科技有限公司 | A spray drier for solid drink production |
| CN205953545U (en) * | 2016-08-30 | 2017-02-15 | 青川天隆新材料开发有限责任公司 | A high -speed centrifugal spray drying system for nano meter aluminium production |
| CN206535218U (en) * | 2017-03-16 | 2017-10-03 | 乳山韩威生物科技有限公司 | A kind of Highspeedcentrifugingandsprayingdrier |
| CN207785970U (en) * | 2017-12-19 | 2018-08-31 | 无锡市尚德干燥设备有限公司 | Highspeedcentrifugingandsprayingdrier |
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| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20180323 |