CN206683315U - Boiling drier for chenodeoxycholic acid particle drying - Google Patents
Boiling drier for chenodeoxycholic acid particle drying Download PDFInfo
- Publication number
- CN206683315U CN206683315U CN201720006837.6U CN201720006837U CN206683315U CN 206683315 U CN206683315 U CN 206683315U CN 201720006837 U CN201720006837 U CN 201720006837U CN 206683315 U CN206683315 U CN 206683315U
- Authority
- CN
- China
- Prior art keywords
- cone
- cylinder
- heater
- chenodeoxycholic acid
- acid particle
- 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
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Abstract
A kind of boiling drier for chenodeoxycholic acid particle drying, including frame, the boiling storehouse that is arranged at the heater of frame bottom, is arranged at the sack cleaner of frame upper end and is clipped between heater and sack cleaner.CDCA granulates after synthesis are added in cylinder, motor driving flabellum rotates, hot-air is sent into cylinder by stainless steel mesh I after heater work, CDCA granulates in airflow function lower shell produce boiling, drive mechanism driving cylinder rotation, cone driving cone rotation, CDCA granulates can move under airflow function through the outwardly side water conservancy diversion of cone, its blade I being rotated impacts afterwards, so that it is crushed, its blade II for continuing to be rotated again during outside lateral movement impacts simultaneously, so as to further increase crushing effect so as to which drying effect is also greatly improved, ensure that its aridity, improve the quality of CDCA granulates.
Description
Technical field
It the utility model is related to chemical machinery field, and in particular to a kind of boiling drier.
Background technology
The CDCA granulates progress to bulky grain is needed after chenodeoxycholic acid is synthesized using the bile of chicken and duck courage
Dry, but because chenodeoxycholic acid particle is excessive, so as to which CDCA granulates can not be made using traditional boiling drier
Fully dry, not only need drying for a long time to cause production efficiency relatively low, while dry the quality that also not have impact on product thoroughly.
The content of the invention
The utility model is in order to overcome the shortcomings of above technology, there is provided one kind improve chenodeoxycholic acid particle drying degree and
Crush the boiling drier of the chenodeoxycholic acid particle drying of uniformity.
Technical scheme is used by the utility model overcomes its technical problem：
A kind of boiling drier for chenodeoxycholic acid particle drying, including frame, the heating for being arranged at frame bottom
Device, the sack cleaner for being arranged at frame upper end and the boiling storehouse being clipped between heater and sack cleaner, it is described to add
Hot device is including the vapor heat exchanger being arranged in heater, the motor I being installed in heater and is installed on the output shaft of motor I
On flabellum, the vapor heat exchanger is connected to steam boiler by steam pipe, and the boiling storehouse includes outer cylinder body, passes through bearing
It is rotatablely installed the cylinder inside outer cylinder body, is arranged at drive mechanism, rotational installation for driving barrel body rotation on outer cylinder body
It is arranged at intervals in the cone in cylinder in inversed-cone shape, the cone drive mechanism of driving cone rotation, along cone circumferencial direction
It is arranged at intervals in some blades I of outer surface of cone and along cylinder circumferencial direction some blades II of cylinder inner surface, institute
The upper end open for stating outer cylinder body is connected with sack cleaner, and its lower ending opening is connected with heater, the lower end of the cylinder
Opening sealed set has stainless steel mesh I, and sealed set has stainless steel at the upper end open of the outer cylinder body above cylinder
Screen cloth II, the mesh internal diameter on the stainless steel mesh I and stainless steel mesh II are respectively less than the external diameter of CDCA granulates.
Motor II that above-mentioned drive mechanism includes being installed on outer cylinder body, the gear I that is installed on the output shaft of motor II with
And the gear II of cylinder lower end is installed on, the gear I is intermeshed with gear II.
Above-mentioned cone drive mechanism includes being arranged at the shaft coupling of cone lower end, the shaft coupling other end and motor I
Output shaft is connected.
Above-mentioned cone upper end is provided with the cone lid of cone shape.
In order to further improve the aridity of CDCA granulates, in addition to be arranged in cone helix tube, set
In cone upper end and the venthole that is connected with the helix tube port of export and it is arranged at cone lower end and is connected with solenoid inlet end
Air admission hole, swivel joint I is installed on the stainless steel mesh I, the air admission hole passes through swivel joint I and air inlet pipe phase
Even, the air inlet pipe is connected to steam boiler, swivel joint II is provided with the stainless steel mesh II, and the venthole passes through
Swivel joint II is connected with escape pipe.
In order to further improve crushing effect, some plush coppers are respectively arranged with the above-mentioned two sides of blade I.
In order to further improve crushing effect, some plush coppers are respectively arranged with the above-mentioned two sides of blade II.
The beneficial effects of the utility model are：CDCA granulates after synthesis are added in cylinder, and are placed in stainless
Between steel screen cloth I and stainless steel mesh II, vapours is entered in vapor heat exchanger by steam pipe, motor driving fan blade rotating
It is dynamic, hot-air is sent into cylinder by stainless steel mesh I after heater work, the CDCA in airflow function lower shell
Granulates produce boiling, and drive mechanism driving cylinder rotation, cone driving cone rotation, CDCA granulates are in airflow function
It can be moved through the outwardly side water conservancy diversion of cone down, its blade I being rotated impacts afterwards, so that it is crushed, simultaneously
Its blade II for continuing to be rotated again during outside lateral movement impacts, and so as to further increase crushing effect, passes through leading for cone
To can make chenodeoxycholic acid particle thermally equivalent, while chenodeoxycholic acid particle diameter is less and less, so as to drying effect
It is greatly improved, ensures that its aridity, improves the quality of CDCA granulates.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is heater position of the present utility model cross-sectional view；
Fig. 3 is boiling storehouse position cross-sectional view of the present utility model；
Fig. 4 is the outer surface mplifying structure schematic diagram of rotation flabellum of the present utility model；
Fig. 5 is cone cross-sectional view of the present utility model；
In figure, the electricity of the heater 3. of 1. frame 2. boiling storehouse 4. sack cleaner, 5. steam pipe, 6. vapor heat exchanger 7.
The stainless steel mesh I 15. of 13. helix tube of machine I 8. flabellum, 9. shaft coupling, 10. outer cylinder body, 11. cylinder, 12. bearing 14. is not
The cone 17. of steel screen cloth II 16. of becoming rusty bores the escape pipe 22. of II 20. air inlet pipe of lid 18. swivel joint, I 19. swivel joint 21.
The venthole of 28. air admission hole of motor II 23. gear, I 24. gear, II 25. blade, I 26. blade, II 27. plush copper 29..
Embodiment
1 the utility model is described further to accompanying drawing 5 below in conjunction with the accompanying drawings.
A kind of boiling drier for chenodeoxycholic acid particle drying, including frame 1, be arranged at the bottom of frame 1 plus
Hot device 2, the sack cleaner 4 for being arranged at the upper end of frame 1 and the boiling storehouse being clipped between heater 2 and sack cleaner 4
3, heater 2 is including the vapor heat exchanger 6 being arranged in heater 2, the motor I 7 being installed in heater 2 and is installed on
Flabellum 8 on the output shaft of motor I 7, vapor heat exchanger 6 are connected to steam boiler by steam pipe 5, and boiling storehouse 3 includes outer cylinder body
10th, cylinder 11 inside outer cylinder body 10 is rotatablely installed by bearing 12, is arranged on outer cylinder body 10 and is used to drive 11 turns of cylinder
Dynamic drive mechanism, it is rotatablely installed the cone driving rotated in the cone 16 in cylinder 11 in inversed-cone shape, driving cone 16
Mechanism, some blades I 25 for being arranged at intervals at along the circumferencial direction of cone 16 outer surface of cone 16 and along the circumferencial direction of cylinder 11
Some blades II 26 of the inner surface of cylinder 11 are arranged at intervals at, the upper end open of outer cylinder body 10 is connected with sack cleaner 4,
Its lower ending opening is connected with heater 2, and sealed set has stainless steel mesh I 14 at the lower ending opening of cylinder 11, positioned at cylinder
Sealed set has stainless steel mesh II 15, stainless steel mesh I 14 and stainless steel at the upper end open of the outer cylinder body 10 of 11 tops
Mesh internal diameter on screen cloth II 15 is respectively less than the external diameter of CDCA granulates.CDCA granulates after synthesis are added to
In cylinder 11, and it is placed between stainless steel mesh I 14 and stainless steel mesh II 15, vapours enters steaming by steam pipe 5
In vapour heat exchanger 6, motor 7 drives flabellum 8 to rotate, and hot-air is sent into cylinder by stainless steel mesh I 14 after heater work
In 11, the CDCA granulates in airflow function lower shell 11 produce boiling, and drive mechanism driving cylinder 11 rotates, cone
Driving cone 16 rotates, and CDCA granulates can move under airflow function through the outwardly side water conservancy diversion of cone 16,
Its blade I 25 being rotated impacts afterwards, so that it is crushed, while the blade being rotated again during its outside lateral movement of continuation
II impact, so as to further increase crushing effect, can make chenodeoxycholic acid particle thermally equivalent by the guiding of cone 16,
Chenodeoxycholic acid particle diameter is less and less simultaneously, so as to which drying effect is also greatly improved, ensures that its aridity,
Improve the quality of CDCA granulates.
Drive mechanism can be following structure, its motor II 22 for including being installed on outer cylinder body 10, be installed on motor II
Gear I 23 on 22 output shafts and the gear II 24 for being installed on the lower end of cylinder 11, gear I 23 are mutually nibbled with gear II 24
Close.The rotational driving gear I 23 of motor II 22 rotates, and gear I 23 drives cylinder 11 to rotate by meshed gears II 24.Cone
Body drive mechanism can be following structure, and it includes the shaft coupling 9 for being arranged at the lower end of cone 16, the other end of shaft coupling 9 and motor I
7 output shaft is connected.Rotated using the motor II 22 for driving flabellum 8 to rotate by shaft coupling 9 with movable cone 16, the transmission made
Mechanism greatly simplifies, so as to improve efficiency.
Further, the upper end of cone 16 is provided with the cone lid 17 of cone shape, the goose seethed with excitement in the cylinder 11 in boiling storehouse 3
Deoxycholic aicd particle can be slid downwards after moving to the top of cone 16 by boring the conical surface around lid 17, prevent cone
The situation of chenodeoxycholic acid particle packing is caused to occur for plane in the upper end of body 16.The spiral shell being arranged in cone 16 can also be included
Coil 13, the venthole 29 for being arranged at the upper end of cone 16 and being connected with the port of export of helix tube 13 and be arranged at the lower end of cone 16 and
The air admission hole 28 being connected with the arrival end of helix tube 13, swivel joint I 18 is provided with stainless steel mesh I 14, and air admission hole 28 is logical
Cross swivel joint I 18 with air inlet pipe 20 to be connected, air inlet pipe 20 is connected to steam boiler, and rotation is provided with stainless steel mesh II 15
Adapter II 19, venthole 29 are connected by swivel joint II 19 with escape pipe 21.Vapours is by air inlet pipe 20 through air inlet
Hole 28 enters helix tube 13, and helix tube 13 heats cone 16, the goose that will further can be seethed with excitement so as to cone 16 in cylinder 11
Deoxycholic aicd particle is thermally dried, and further increases drying effect.It is respectively arranged with the two sides of blade I 25 some
Plush copper 27, be respectively arranged with some plush coppers 27 on the two sides of blade II 26, when CDCA granulates touch blade I 25 or
During blade II 26, it can be applied the small plush copper 27 of area and smash, and further increase chenodeoxycholic acid particle and crush effect
Fruit.
Claims (7)
1. a kind of boiling drier for chenodeoxycholic acid particle drying, including frame（1）, be arranged at frame（1）Bottom
Heater（2）, be arranged at frame（1）The sack cleaner of upper end（4）And it is clipped on heater（2）With sack cleaner（4）
Between boiling storehouse（3）, it is characterised in that：The heater（2）Including being arranged at heater（2）Interior vapor heat exchanger（6）、
It is installed on heater（2）Interior motor I（7）And it is installed on motor I（7）Flabellum on output shaft（8）, the vapor heat exchanger
（6）Pass through steam pipe（5）It is connected to steam boiler, the boiling storehouse（3）Including outer cylinder body（10）, pass through bearing（12）Rotate peace
Loaded on outer cylinder body（10）Internal cylinder（11）, be arranged at outer cylinder body（10）It is upper to be used to drive cylinder（11）The driving machine of rotation
Structure, it is rotatablely installed in cylinder（11）The interior cone in inversed-cone shape（16）, driving cone（16）The cone drive mechanism of rotation,
Along cone（16）Circumferencial direction is arranged at intervals at cone（16）Some blades I of outer surface（25）And along cylinder（11）Circumference side
To being arranged at intervals at cylinder（11）Some blades II of inner surface（26）, the outer cylinder body（10）Upper end open and bag-type dust
Device（4）It is connected, its lower ending opening and heater（2）It is connected, the cylinder（11）Lower ending opening at sealed set have not
Become rusty steel screen cloth I（14）, positioned at cylinder（11）The outer cylinder body of top（10）Upper end open at sealed set have stainless steel mesh II
（15）, the stainless steel mesh I（14）And stainless steel mesh II（15）On mesh internal diameter be respectively less than CDCA granulates
External diameter.
2. the boiling drier according to claim 1 for chenodeoxycholic acid particle drying, it is characterised in that：The drive
Motivation structure includes being installed on outer cylinder body（10）On motor II（22）, be installed on motor II（22）Gear I on output shaft（23）
And it is installed on cylinder（11）The gear II of lower end（24）, the gear I（23）With gear II（24）Intermeshing.
3. the boiling drier according to claim 1 for chenodeoxycholic acid particle drying, it is characterised in that：The cone
Body drive mechanism includes being arranged at cone（16）The shaft coupling of lower end（9）, the shaft coupling（9）The other end and motor I（7）It is defeated
Shaft is connected.
4. the boiling drier according to claim 1 for chenodeoxycholic acid particle drying, it is characterised in that：The cone
Body（16）Upper end is provided with the cone lid of cone shape（17）.
5. the boiling drier as claimed in any of claims 1 to 4 for chenodeoxycholic acid particle drying, it is special
Sign is：Also include being arranged at cone（16）Interior helix tube（13）, be arranged at cone（16）Upper end and and helix tube（13）Go out
The connected venthole in mouth end（29）And it is arranged at cone（16）Lower end and and helix tube（13）The connected air admission hole of arrival end
（28）, the stainless steel mesh I（14）On swivel joint I is installed（18）, the air admission hole（28）Pass through swivel joint I（18）
With air inlet pipe（20）It is connected, the air inlet pipe（20）It is connected to steam boiler, the stainless steel mesh II（15）On rotation is installed
Adapter II（19）, the venthole（29）Pass through swivel joint II（19）With escape pipe（21）It is connected.
6. the boiling drier according to claim 5 for chenodeoxycholic acid particle drying, it is characterised in that：The leaf
Piece I（25）Some plush coppers are respectively arranged with two sides（27）.
7. the boiling drier according to claim 5 for chenodeoxycholic acid particle drying, it is characterised in that：The leaf
Piece II（26）Some plush coppers are respectively arranged with two sides（27）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720006837.6U CN206683315U (en) | 2017-01-04 | 2017-01-04 | Boiling drier for chenodeoxycholic acid particle drying |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720006837.6U CN206683315U (en) | 2017-01-04 | 2017-01-04 | Boiling drier for chenodeoxycholic acid particle drying |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206683315U true CN206683315U (en) | 2017-11-28 |
Family
ID=60396118
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720006837.6U Expired - Fee Related CN206683315U (en) | 2017-01-04 | 2017-01-04 | Boiling drier for chenodeoxycholic acid particle drying |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206683315U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108917293A (en) * | 2018-05-22 | 2018-11-30 | 张顺 | A kind of pharmaceutical production boiling drier |
-
2017
- 2017-01-04 CN CN201720006837.6U patent/CN206683315U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108917293A (en) * | 2018-05-22 | 2018-11-30 | 张顺 | A kind of pharmaceutical production boiling drier |
| CN108917293B (en) * | 2018-05-22 | 2020-12-08 | 阜阳市卓创科技服务生产力促进中心 | Fluidized drying machine for pharmaceutical production |
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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: 20171128 Termination date: 20220104 |