CN206121682U - Vertical continuous prilling granulator - Google Patents
Vertical continuous prilling granulator Download PDFInfo
- Publication number
- CN206121682U CN206121682U CN201621088346.2U CN201621088346U CN206121682U CN 206121682 U CN206121682 U CN 206121682U CN 201621088346 U CN201621088346 U CN 201621088346U CN 206121682 U CN206121682 U CN 206121682U
- Authority
- CN
- China
- Prior art keywords
- import
- air
- binding agent
- fluidization air
- fluidization
- 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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- Glanulating (AREA)
Abstract
The utility model relates to a vertical continuous prilling granulator in petrochemical technology field, it mainly comprises casing, cyclone, reinforced import, foraminiferous swash plate, fluidization air intlet A, air sifter air intlet, big grain exports, air -blower, fluidization air intlet B, pump, binder import and binder shower nozzle. Have pump, binder import, air -blower, fluidization air intlet B at the casing left part, at inside binder shower nozzle, foraminiferous swash plate and the big grain exports of being equipped with of casing, the right part is equipped with cyclone, reinforced import, fluidization air intlet A, air sifter air intlet, the partly fluidization air intlet B entering casing of following of fluidization air that the air -blower drum is gone into, another subtotal binder mixes the back and imports the entering casing from the binder. It has the aperture to open in the foraminiferous swash plate, and the diameter is less than produces the particle diameter, fluidization air intlet A and fluidization air intlet B adopt the design of symmetrical formula, reinforced import and binder import are on same straight line.
Description
Technical field
This utility model is related to a kind of vertical continuous comminutor of technical field of petrochemical industry.
Background technology
With society and the development of production, in opposite bioplasm quantity and form, there is high requirement, wherein granular preparation has
Irreplaceable importance.China is introducing, on the basis of digesting, absorbing external advanced granulating technique, have developed fluidisation
Spray granulation, have developed vibratory liquefaction spray granulation on this basis again, but between these equipment are only used for
Have a rest production, it is impossible to continuously produced.Granulation process is extremely complex process, on chemical industries, adopts powder body for primary
Raw material or direct products are easily flown upward with poor fluidity, dust, cause production environment severe and packaging difficulty etc. lacks using
Point；Wastage of material and environmental pollution are easily caused during transport.Therefore, grain products replace powder product to become material
The trend that form updates；The manufacture process of granule is exactly the process that little particle is polymerized to larger entity, by improving granule
The product that the processed in performance and later stage finally can be wanted.
The content of the invention
This utility model purpose is for the efficiency for improving pelletize, there is provided a kind of vertical continuous comminutor, operation letter
It is single, continuously can work, the prilling granulator of easy care, simple structure.
The technical scheme adopted by this utility model is：
A kind of vertical continuous comminutor of this utility model, it is mainly by housing, cyclone separator, charging import, with holes
Swash plate, fluidization air import A, air sifter air intlet, bulky grain outlet, aerator, fluidization air import B, pump, binding agent import
Constitute with binding agent shower nozzle.There are pump, binding agent import, aerator, fluidization air import B in housing left part, set in enclosure interior
There is the outlet of binding agent shower nozzle, swash plate with holes and bulky grain, right part has cyclone separator, charging import, fluidization air import A, gas
Sieve air intlet；The fluidization air part that aerator is blasted enters housing, another part and binding agent from fluidization air import B
Housing is entered from binding agent import after mixing.Aperture is provided with swash plate with holes, diameter is less than and produces particle diameter；Fluidization air enters
Mouth A and fluidization air import B is designed using symmetrical expression；Import feed with binding agent import on the same line, binding agent shower nozzle
Using tapered design, its effect is to spray binding agent.
Advantage of the present utility model：Simple to operate, easy care, it is provided with two fluidization air imports and is shown granulation efficiency
Write and improve.
Description of the drawings
Fig. 1 is a kind of structural representation of vertical continuous comminutor of this utility model.
In figure：1. housing, 2. cyclone separator, 3. feed import, 4. swash plate with holes, 5. fluidization air import A, 6. air sifter
Air intlet, 7. bulky grain outlet, 8. aerator, 9. fluidization air import B, 10. pump, 11. binding agent imports, 12. binding agents
Shower nozzle.
Specific embodiment
Below in conjunction with the accompanying drawings this utility model is described further.
As shown in figure 1, a kind of vertical continuous comminutor of this utility model, mainly by housing 1, cyclone separator 2, charging
Import 3, swash plate with holes 4, fluidization air import A5, the outlet 7, aerator 8 of air sifter air intlet 6, bulky grain, fluidization air import
B9, pump 10, binding agent import 11 and binding agent shower nozzle 12 are constituted.It is described 1 left part of housing be provided with pump 10, binding agent import 11,
Aerator 8, fluidization air import B9, are provided with binding agent shower nozzle 12, swash plate with holes 4 and bulky grain outlet 7 inside housing 1, right
Portion is provided with cyclone separator 2, charging import 3, fluidization air import A5, air sifter air intlet 6.
As shown in figure 1, specific granulation process is：Fluidization air is passed through by aerator 8 toward at housing 1 first, while
Dust is passed through in charging import 3, while binding agent is passed through, the fluidization air being passed through from the left of housing 1 some with it is viscous
Housing 1 is passed through after knot agent mixing., by dust bonding into bulky grain, bulky grain is due to weight for the binding agent sprayed from binding agent shower nozzle 12
Power is acted on toward whereabouts, is finally flowed out from bulky grain outlet 7；Not glued dust, due to the effect that fluidization air up blows, will be to
Upper motion, dust and fluidization air are separated at cyclone separator 2 together, and the dust after separation returns to housing from newly
Interior continuation pelletize, after dust is a granulated into bulky grain, adds powder from charging import 3 while outflow from bulky grain outlet 7 again
The granulation process of dirt, i.e., one terminates.
Claims (3)
1. a kind of vertical continuous comminutor, mainly by housing (1), cyclone separator (2), charging import (3), swash plate with holes
(4), fluidization air import A (5), air sifter air intlet (6), bulky grain outlet (7), aerator (8), fluidization air import B
(9), pump (10), binding agent import (11) and binding agent shower nozzle (12) composition, it is characterised in that：Pump is provided with housing (1) left part
(10), binding agent import (11), aerator (8), fluidization air import B (9), are provided with binding agent shower nozzle inside housing (1)
(12), swash plate (4) with holes and bulky grain outlet (7), right part is provided with cyclone separator (2), charging import (3), fluidization air enters
Mouth A (5), air sifter air intlet (6)；The fluidization air part that aerator (8) is blasted enters shell from fluidization air import B (9)
From binding agent import (11) into housing (1) after body (1), another part and binding agent mixing.
2. a kind of vertical continuous comminutor according to claim 1, it is characterised in that：Swash plate (4) with holes is inner be provided with it is little
Hole, diameter are less than and produce particle diameter；Fluidization air import A (5) and fluidization air import B (9) are designed using symmetrical expression；Charging
Import (3) is with binding agent import (11) on the same line.
3. a kind of vertical continuous comminutor according to claim 1, it is characterised in that：Binding agent shower nozzle (12) is using cone
Type is designed, and its effect is to spray binding agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621088346.2U CN206121682U (en) | 2016-09-28 | 2016-09-28 | Vertical continuous prilling granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621088346.2U CN206121682U (en) | 2016-09-28 | 2016-09-28 | Vertical continuous prilling granulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206121682U true CN206121682U (en) | 2017-04-26 |
Family
ID=58572482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621088346.2U Expired - Fee Related CN206121682U (en) | 2016-09-28 | 2016-09-28 | Vertical continuous prilling granulator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206121682U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112934108A (en) * | 2021-03-05 | 2021-06-11 | 江苏道宁药业有限公司 | Refining and granulating equipment and method for lactose monohydrate fine powder |
-
2016
- 2016-09-28 CN CN201621088346.2U patent/CN206121682U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112934108A (en) * | 2021-03-05 | 2021-06-11 | 江苏道宁药业有限公司 | Refining and granulating equipment and method for lactose monohydrate fine powder |
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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: 20170426 Termination date: 20170928 |